English
Tiếng Việt
(en)The present invention relates to a multistage polymer, its composition, its process of preparation, and its use as impact modifier in thermoplastic compositions. More particularly the present invention relates a process for manufacturing a multistage polymer, a multistage polymer in thermoplastic compositions, which provides the composition having satisfying thermal stability.
1.ApplicationNumber: US-201515527415-A
1.PublishNumber: US-2017355801-A1
2.Date Publish: 20171214
3.Inventor: COUFFIN Aline O.
PIRRI ROSANGELA
MALET FREDERIC
4.Inventor Harmonized: COUFFIN ALINE O(FR)
PIRRI ROSANGELA(FR)
MALET FREDERIC(FR)
5.Country: US
6.Claims:
(en)The present invention relates to a multistage polymer, its composition, its process of preparation, and its use as impact modifier in thermoplastic compositions. More particularly the present invention relates a process for manufacturing a multistage polymer, a multistage polymer in thermoplastic compositions, which provides the composition having satisfying thermal stability.
7.Description:
(en)FIELD OF THE INVENTION
The present invention relates to a multistage polymer, its composition and its process of preparation.
In particular the present invention it relates to a multistage polymer, its composition and its process of preparation and its use in thermoplastic compositions.
More particularly the present invention relates to a process for manufacturing a multistage polymer, said multistage polymer in a thermoplastic composition, gives composition is having a satisfying thermal stability.
TECHNICAL PROBLEM
Impact modifiers are widely used to improve the impact strength for thermoplastic compositions with the aim to compensate their inherent brittleness or the embrittlement that occurs at sub zero temperatures, notch sensitivity and crack propagation. So an impact modified polymer is a polymeric material whose impact resistance and toughness have been increased by the incorporation of phase nano domains of a rubbery material.
This is usually done due to the introduction of microscopic rubber particles into the polymer matrix that can absorb the energy of an impact or dissipate it. One possibility is to introduce the rubber particles in form of core-shell particles. These core-shell particles that possess very generally a rubber core and a polymeric shell, having the advantage of a proper particle size of the rubber core for effective toughening and the grafted shell in order to have the adhesion and compatibility with the thermoplastic matrix.
The performance of the impact modification is a function of the particles size, especially of the rubber part of the particle, and its quantity. There is an optimal average particle size in order to have the highest impact strength for a given quantity of added impact modifier particles.
These primary impact modifier particles are usually added in form of powder particles to the thermoplastic material. These powder particles are agglomerated primary impact modifier particles. During the blending of the thermoplastic material with the powder particles the primary impact modifier particles are regained and are dispersed more or less homogenously dispersed in the thermoplastic material.
While the particle size of the impact modifier particles in the range of nanometers, the range of the agglomerated powder particles is in the range of micrometers.
Agglomeration during the recovery can be obtained by several processes, as for example, spray drying, coagulation, shearing, or freeze drying or combination of spray drying and coagulation techniques.
It important to avoid negative influence of the impact modifier powder on the thermoplastic polymer composition to which the impact modifier is added. As negative influence, it is understood, for example the color stability, the thermal stability, the hydrolysis stability of the thermoplastic polymer comprising the impact modifier, either on function of the time or the temperature or both.
All these influences might occur due to the architecture of the core-shell but more particularly the impurities and side products employed during the synthesis and treatment of the impact modifier powder. Usually, there is no special purification step of the impact modifier, just a separation of solid versus liquid. Therefore more or less important quantities of any chemical compound (impurities, by-products) employed are still incorporated in the impact modifier. The concerned quantities of them may vary. However these chemical compounds should not influence at all or have only a minor influence on the thermoplastic material in a major way as for example degradation of optical and/or mechanical and/or rheological properties with time and/or temperature and/or hygrometry.
Extensive washing or purification might get rid of some of the compounds coming from impurities or products used during the synthesis that might have negative influence of the impact modifier powder on the performance thermoplastic polymer composition.
On the other hand all processes are extremely cost sensitive. A slight improvement in process can result in a significant market advantage.
The objective of the present invention is to propose a multistage polymer having a satisfying thermal stability.
An additional objective of the present invention is also to have a multistage polymer having a satisfying thermal stability that can be used as impact modifier.
Still another objective of the present invention is to propose a process for manufacturing a multistage polymer having a satisfying thermal stability.
An additional objective of the present invention is a thermoplastic composition comprising a multistage polymer, said composition is having a satisfying thermal stability.
Still an additional objective is having a process for preparing for manufacturing a multistage polymer, said multistage polymer in a thermoplastic composition, gives composition is having a satisfying thermal stability.
BACKGROUND OF THE INVENTION
Prior Art
The document EP0900827 discloses an impact modified carbonate polymer composition having improved resistance to degradation and improved thermal stability. According to the document the impact modifier has to be essentially free of basic compounds from the emulsion polymerization, and especially troublesome are emulsifiers of alkali salts of fatty acids as alkali metal carboxylate. The impact modifier is preferably of a shell-core structure and is prepared by an emulsion polymerization process and has a pH of about 3 to about 8. A preferred emulsifier is an alkyl sulfonate having an alkyl group of C 6 -C 18 carbons.
The document EP2189497 discloses polymer compositions containing phosphates and especially the process for obtaining them. The polymer composition is a polymer obtained by a multi stage process and is an impact modifier. The phosphate salts are introduced in order to reduce or eliminate the deleterious effects of the multivalent cations that are present in polymer obtained by a multi stage process. The use of such a process allows a coagulated polymer to be used as an impact additive to a matrix without causing the deleterious effects from the multivalent cation that would otherwise have occurred. The process implies a washing step with water to get first rid of salts and ions and then adding an aqueous alkaline phosphate solution. The process requires a lot of water and consequently also the time and energy consuming steps of separation of water from polymer composition.
The document EP 2465882 discloses improved impact modified thermoplastic compositions. The thermoplastic compositions comprise a polymeric impact modifier with a core-shell structure made by a multistage process and recovered by a special process controlling and adjusting the pH value. Coagulation is done with salts and preferably magnesium sulfate.
The document WO2009/118114 describes an impact modified polycarbonate composition with a good combination of color, hydrolysis and melt stability. The rubber core is based on polybutadiene. For the preparation of the graft rubber polymer salts of fatty acids, especially of carboxylic acids are used. The yellow index of the compositions given with injection temperature at 260° C. is quite important: 20 or higher.
The document WO2009/126373 describes functional MBS impact modifiers synthesized by a multistage emulsion polymerization. At the end of the synthesis the reaction mixture obtained is coagulated in order to separate the polymer. The coagulating treatment is performed by bringing into contact the reaction mixture with a saline solution (calcium chloride or aluminum chloride—CaCl 2 or AlCl 3 ) or a solution acidified with concentrated sulfuric acid and then to separate, by filtration, the solid product resulting from the coagulating, the solid product then being washed and dried to give a graft copolymer as a powder.
The present invention aims to avoid at least one of the inconvenient of the state of the art.
There is a need for improving the process of making a multistage polymer, by optimizing the steps involved, while allowing the obtained multistage polymer an increase of the performance as impact additive in thermoplastic compositions.
BRIEF DESCRIPTION OF THE INVENTION
Surprisingly it has been found that a polymer composition in form of polymeric particles made by a multistage process comprising
at least one stage giving layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C. and at least one subsequent stage giving layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C.,
obtained by a multistage process characterized that the polymer composition comprises less than 50 ppm of multivalent cations and at least 350 ppm of phosphorous in form of a phosphorous containing compound with phosphorous in the oxidation stage +III or +V, yields to a product having satisfying thermal aging properties.
Surprisingly it has also been found that a process for manufacturing the polymer composition comprising a multistage polymer comprising the steps of
a) polymerizing by emulsion polymerization of a monomer or monomers mixture (A m ) to obtain during this stage one layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C. b) polymerizing by emulsion polymerization in presence of the polymer obtained in step a) of a monomer or monomer mixture (B m ) to obtain during this subsequent stage a layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C. c) coagulating the multistage polymer d) adjusting the pH to a value between 5 to 10 e) washing the multistage polymer f) addition of an aqueous solution comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V
characterized that the coagulation step is not made with multivalent cations, and the polymer composition comprises at least 350 ppm of phosphorous in form of a phosphorous containing compound with phosphorous in the oxidation stage +III or +V, yields to a product having satisfying thermal aging properties.
DETAILED DESCRIPTION OF THE INVENTION
According to a first aspect, the present invention relates to a polymer composition in form of polymeric particles of a multistage polymer made by a multistage process comprising
at least one stage giving layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C. and at least one subsequent stage giving layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C.,
obtained by a multistage process characterized that the polymer composition comprises less than 50 ppm of multivalent cations and at least 350 ppm of phosphorous in form of a phosphorous containing compound with phosphorous in the oxidation stage +III or +V.
According to a second aspect the present invention relates to a process for manufacturing a polymer composition comprising a multistage polymer comprising the steps of
a) polymerizing by emulsion polymerization of a monomer or monomer mixture (Am) to obtain during this stage one layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C. b) polymerizing by emulsion polymerization in presence of the polymer obtained in step a) of a monomer or monomers mixture (B m ) to obtain during this subsequent stage a layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C. c) coagulating the multistage polymer d) adjusting the pH to a value between 5 to 10 e) washing the multistage polymer f) addition of an aqueous solution comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V
characterized that the coagulation step is not made with multivalent cations, and the polymer composition comprises at least 350 ppm of phosphorous in form of a phosphorous containing compound with phosphorous in the oxidation stage +III or +V.
According to a third aspect the present invention relates to a process for manufacturing a polymer composition in form of polymeric particles comprising a multistage polymer comprising the steps of
a) polymerizing by emulsion polymerization of a monomer or monomer mixture (A m ) to obtain during this stage one layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C. b) polymerizing by emulsion polymerization in presence of the polymer obtained in step a) of a monomer or monomers mixture (B m ) to obtain during this subsequent stage a layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C. c) coagulating the multistage polymer d) adjusting the pH to a value between 5 to 10 e) washing the multistage polymer f) addition of an aqueous solution comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V
characterized that the coagulation step is not made with multivalent cations, and the polymer composition comprises at least 350 ppm of phosphorous in form of a phosphorous containing compound with phosphorous in the oxidation stage +III or +V.
By the term “polymer powder” as used is denoted a polymer comprising powder grain in the range of at least 1 micrometer (μm) obtained by agglomeration of primary polymer comprising particles in the nanometer range.
By the term “primary particle” as used is denoted a spherical polymer comprising particle in the nanometer range. Preferably the primary particle has a weight average particle size between 20 nm and 500 nm.
By the term “particle size” as used is denoted the volume average diameter of a particle considered as spherical.
By the term “copolymer” as used is denoted that the polymer consists of at least two different monomers.
By “multistage polymer” as used is denoted a polymer formed in sequential fashion by a multi-stage polymerization process. Preferred is a multi-stage emulsion polymerization process in which the first polymer is a first-stage polymer and the second polymer is a second-stage polymer, i.e., the second polymer is formed by emulsion polymerization in the presence of the first emulsion polymer, with at least two stages that are different in composition.
By the term “(meth)acrylic” as used is denoted all kind of acrylic and methacrylic monomers.
By the term “(meth)acrylic polymer” as used is denoted that the (meth)acrylic polymer comprises essentially polymers comprising (meth)acrylic monomers that make up 50 wt % or more of the (meth)acrylic polymer.
By the term “impact modifier” as used is denoted a compound comprising an elastomer or rubber that can be added or incorporated in a thermoplastic compound to improve its impact resistance.
By the term “rubber” as used is denoted the thermodynamic state of the polymer above its glass transition
With regard to the multistage polymer of the invention, it is a polymer particle having a multilayer structure comprising at least one layer (A) comprising a polymer (A1) having a glass transition temperature below 0° C. and at least another layer (B) comprising a polymer (B1) having a glass transition temperature over 45° C.
The ratio of layer (A)/layer (B) in the multistage polymer is not particularly limited, but preferably it is in a range in weight between 10/90 and 95/5, more preferably 40/60 and 95/5 advantageously 60/40 to 90/10 and most advantageously between 70/30 and 90/10.
The polymer particle having a multilayer structure is spherical. The polymer particle having a multilayer structure is also called the primary particle. The polymer particle has a weight average particle size between 20 nm and 500 nm. Preferably the weight average particle size of the polymer particle is between 50 nm and 400 nm, more preferably between 75 nm and 350 nm and advantageously between 80 nm and 300 nm.
The polymer particle according to the invention is obtained by a multistage process such as two or three stages or more stages.
Preferably the polymer (A1) having a glass transition temperature below 0° C. in the layer (A) is not made during the last stage of the multistage process. The polymer (A1) is having a glass transition temperature below 0° C. in the layer (A) never forms the external layer or outer shell of the polymer particle having the multilayer structure.
Preferably the polymer (B1) having a glass transition temperature above 45° C. in the layer (B) is the external layer of the polymer particle having the multilayer structure.
There could be additional intermediate layers made by intermediate steps between the polymer (A1) having a glass transition temperature below 0° C. in the layer (A) and the layer (B) comprising a polymer (B1) having a glass transition temperature over 45° C. This would lead to a multilayered particle.
The glass transition temperature (Tg) of the polymer (A1) is less than 0° C., preferably less than −10° C., advantageously less than −20° C. and most advantageously less than −25° C. and more most advantageously less than −40° C.
More preferably the glass transition temperature Tg of the polymer (A1) is between −120° C. and 0° C., even more preferably between −90° C. and −10° C. and advantageously between −80° C. and −25° C.
Preferably the glass transition temperature Tg of the polymer (B1) is between 45° C. and 150° C. The glass transition temperature of the polymer (B1) is more preferably between 60° C. and 150° C., still more preferably between 80° C. and 150° C. and advantageously between 90° C. and 150° C.
The glass transition temperature Tg can be estimated for example by dynamic methods as thermo mechanical analysis.
The polymer composition of the invention in form of polymeric particles of a multistage polymer can also be in form of a polymer powder. The polymer powder comprises agglomerated primary polymer particles made by the multistage process.
With regard to the polymer powder of the invention, it has a volume median particle size D50 between 1 μm and 500 μm. Preferably the volume median particle size of the polymer powder is between 10 μm and 400 μm, more preferably between 15 μm and 350 μm and advantageously between 20 μm and 300 μm.
The D10 of the particle size distribution in volume is at least 7 μm and preferably 10 μm.
The D90 of the particle size distribution in volume is at most 800 μm and preferably 500 μm, more preferably at most 350 μm.
With regard to the polymer (A1), mention may be made of homopolymers and copolymers comprising monomers with double bonds and/or vinyl monomers.
In a first embodiment the polymer (A1) is chosen from isoprene homopolymers or butadiene homopolymers, isoprene-butadiene copolymers, copolymers of isoprene with at most 98 wt % of a vinyl monomer and copolymers of butadiene with at most 98 wt % of a vinyl monomer. The vinyl monomer may be styrene, an alkylstyrene, acrylonitrile, an alkyl (meth)acrylate, or butadiene or isoprene. In a specific embodiment polymer (A1) is a butadiene homopolymer.
In a second embodiment the polymer (A1) is a (meth)acrylic polymer. A (meth)acrylic polymer according to the invention is a polymer comprising at least 50 wt % preferably at least 60 wt % and more preferably at least 70 wt % of monomers coming from acrylic or methacrylic monomers. The (meth)acrylic polymer according to the invention comprise less than 50 wt % preferably less than 40 wt % and more preferably less than 30 wt % of non acrylic or methacrylic monomers, which can copolymerize with the acrylic or methacrylic monomers.
More preferably the polymer (A1) of the second embodiment comprises at least 70 wt % monomers chosen from C1 to C12 alkyl (meth)acrylates. Still more preferably the polymer (A1) comprises at least 80 wt % of monomers C1 to C4 alkyl methacrylate and/or C1 to C8 alkyl acrylate monomers.
Most preferably the acrylic or methacrylic monomers of the polymer (A1) are chosen from methyl acrylate, ethyl acrylate, propyl acrylate, isopropyl acrylate, butyl acrylate, tert-butyl acrylate, methyl methacrylate, ethyl methacrylate, butyl methacrylate and mixtures thereof, as long as polymer (A1) is having a glass transition temperature of less then 0° C.
The polymer (A1) may be completely or partly crosslinked. All that is required is to add at least one difunctional monomer during the preparation of the polymer (A1). These difunctional monomers may be chosen from poly(meth)acrylic esters of polyols, such as butanediol di(meth)acrylate and trimethylolpropane trimethacrylate. Other multifunctional monomers are, for example, divinylbenzene, trivinylbenzene, and triallyl cyanurate. The core can also be crosslinked by introducing into it, by grafting or as a comonomer during the polymerization, unsaturated functional monomers such as anhydrides of unsaturated carboxylic acids, unsaturated carboxylic acids and unsaturated epoxides. Mention may be made, by way of example, of maleic anhydride, (meth)acrylic acid and glycidyl methacrylate. The crosslinking may also be carried out by using the intrinsic reactivity of the monomers, for example in the case of the diene monomers.
With regard to the polymer (B1), mention may be made of homopolymers and copolymers comprising monomers with double bonds and/or vinyl monomers.
The polymer (B1) is chosen from styrene homopolymers, alkylstyrene homopolymers or methyl methacrylate homopolymers, or copolymers comprising at least 70 wt % of one of the above monomers and at least one comonomer chosen from the other above monomers, another alkyl (meth)acrylate, vinyl acetate and acrylonitrile. The shell may be functionalized by introducing into it, by grafting or as a comonomer during the polymerization, unsaturated functional monomers such as anhydrides of unsaturated carboxylic acids, unsaturated carboxylic acids and unsaturated epoxides. Mention may be made, for example, of maleic anhydride, (meth)acrylic acid glycidyl methacrylate, hydroxyethyl methacrylate and alkyl(meth)acrylamides.
Preferably the polymer (B1) is also a (meth)acrylic polymer.
Preferably the polymer (B1) comprises at least 70 wt % monomers chosen from C1 to C12 alkyl (meth)acrylates. Still more preferably the polymer (B1) comprises at least 80 wt % of monomers C1 to C4 alkyl methacrylate and/or C1 to C8 alkyl acrylate monomers.
Most preferably the acrylic or methacrylic monomers of the polymer (B1) are chosen from methyl acrylate, ethyl acrylate, butyl acrylate, methyl methacrylate, ethyl methacrylate, butyl methacrylate and mixtures thereof, as long as polymer (B1) is having a glass transition temperature of at least 60° C.
Advantageously the polymer (B1) comprises at least 70 wt % of monomer units coming from methyl methacrylate.
The polymer (B1) may be crosslinked by adding at least one multifunctional monomer during the preparation of the polymer (B1).
The multistage polymer of the invention, having a multilayer structure comprising at least one layer (A) comprising a polymer (A1) having a glass transition temperature below 0° C. and another layer (B) comprising a polymer (B1) having a glass transition temperature over 45° C., comprises no voluntary added earth alkali metals neither as ions nor in form of salts. The polymer composition in form of polymeric particles made by the multistage process comprises no voluntary added multivalent cations chosen from earth alkali metal.
By no voluntary added is meant that traces of earth alkali metals in form of ions or salts could be accidently added as a minor impurity with other ions or salts to the composition. Example notably impurities of calcium in sodium compounds are mentioned.
The earth alkali metals as traces or minor impurity present less than 30 ppm, preferably less than 20 ppm and more preferably less than 10 ppm, advantageously less than 9 ppm of the multistage polymer composition. The multivalent cation is chosen from Ca2+ or Mg2+.
Furthermore multivalent cations present less than 50 ppm, preferably less than 40 ppm, more preferably less than 30 ppm, still more preferably less than 25 ppm and advantageously less than 20 ppm of the multistage polymer composition and preferably the final dry multistage polymer composition. Multivalent cations have the general formula M b+ , wherein M present the cation, with b>1, and preferably 5>b>1.
The multivalent cations is the sum of all the eventually non-voluntary added traces of earth alkali metals in form of ions or salts and the eventually voluntary added multivalent cations. The voluntary added multivalent cations have the general formula M b+ , wherein M present the cation, with b≧2, and preferably 4≧b≧2. The voluntary added multivalent cations exclude earth alkali metals.
The multivalent cations including the earth alkali metals in the composition can be analysed by Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES).
The multistage polymer of the invention, having a multilayer structure has a pH value between 5 and 10 and preferable between 6 and 9, more preferable between 6 and 7.5 and advantageously between 6 and 7.
The multistage polymer of the invention comprises a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V.
The multistage polymer comprises at least 350 ppm, preferably at least 360 ppm, more preferably at least 370 ppm, still more preferably at least 380 ppm, advantageously at least 390 ppm and more advantagously at least 400 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound. The content of the phosphorous containing compound is calculated and expressed as phosphorous in view of the multistage polymer composition and not as phosphorous containing compound.
The multistage polymer comprises at most 2000 ppm, preferably at most 1900 ppm and more preferably at most 1800 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound.
The multistage polymer comprises between 350 ppm and 2000 ppm, preferable between 370 pmm and 1900 ppm and more preferably between 390 ppm and 1800 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound.
The quantity of phosphorous in the multistage polymer can be estimated by by Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES).
The oxidation stage is linked to the nature of the phosphorous containing compound added to the composition. Preferably there is no voluntary addition of any reducing or oxidizing agents, in order to change the oxidation stage of the phosphorous in the phosphorous containing compound.
The phosphorous containing compound is preferably chosen from organophosphorous compound, a phosphate salt, phosphoric acid, phosphonate salts, phosphonic acid and their respective esters and mixtures thereof.
By organophosphorous compound in the present invention are understood compounds with P—C and P—O—C bonds.
More preferably the phosphorous containing compound is chosen from organophosphorous compound having a P—O—C bond, a phosphate salt, phosphoric acid, phosphonate salts, phosphonic acid and ester and mixtures thereof.
Phosphate salts are salts that have as anion dihydrogenophosphate (H 2 PO 4 − ), hydrogenophosphate (HPO 4 2− ) or phosphate (PO 4 3− ).
Phosphonate salts are salts that have as anion dihydrogenophosphonate (H 2 PO 3 − ) or hydrogenophosphate (HPO 3 2− ).
With regard to the process for manufacturing a polymer composition comprising a multistage polymer comprising the steps of
a) polymerizing by emulsion polymerization of a monomer or monomer mixture (A m ) to obtain during this stage one layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C., b) polymerizing by emulsion polymerization in presence of the polymer obtained in step a) of a monomer or monomer mixture (B m ) to obtain during this subsequent stage a layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C., c) coagulating the multistage polymer, d) adjusting the pH to a value between 5 to 10, e) washing the multistage polymer, f) addition of an aqueous solution comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V.
Also with regard to the process for manufacturing a polymer composition in form of polymeric particles comprising a multistage polymer comprising the steps of
a) polymerizing by emulsion polymerization of a monomer or monomer mixture (A m ) to obtain during this stage one layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C., b) polymerizing by emulsion polymerization in presence of the polymer obtained in step a) of a monomer or monomer mixture (B m ) to obtain during this subsequent stage a layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C., c) coagulating the multistage polymer, d) adjusting the pH to a value between 5 to 10, e) washing the multistage polymer, f) addition of an aqueous solution comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V.
The polymer composition comprising the multistage polymer or the polymer composition in form of polymeric particles comprising the multistage polymer obtained by said process comprises at least 350 ppm, preferably at least 360 ppm, more preferably at least 370 ppm, still more preferably at least 380 ppm, advantageously at least 390 ppm and more advantageously at least 400 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound. The content of the phosphorous containing compound is calculated and expressed as phosphorous in view of the multistage polymer composition and not as phosphorous containing compound.
The polymer composition comprising the multistage polymer or the polymer composition in form of polymeric particles comprising the multistage polymer obtained by said process comprises at most 2000 ppm, preferably at most 1900 ppm and more preferably at most 1800 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound.
The polymer composition comprising the multistage polymer or the polymer composition in form of polymeric particles comprising the multistage polymer obtained by said process comprises between 350 ppm and 2000 ppm, preferable between 370 pmm and 1900 ppm and more preferably between 390 ppm and 1800 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound.
The quantity of phosphorous in the multistage polymer can be estimated by by Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES).
The phosphorous containing compound is the same as defended before.
Preferably in step d) the pH value is adjusted between 6 and 9 more preferable between 6 and 7.5 and advantageously between 6 and 7.
The process might comprise the additional step g) of drying the polymer composition. A dry polymer composition according to the invention is a composition that comprises less than 1% of humidity or water. The humidity of a polymer composition can be measure with a thermo balance.
The drying of the polymer can be made in a oven or vacuum oven with heating of the composition for 48 hours at 50° C.
The process of the invention, for manufacturing the polymer composition comprising the multistage polymer having a multilayer structure comprising at least one layer (A) comprising a polymer (A1) having a glass transition temperature below 0° C. and another layer (B) comprising a polymer (B1) having a glass transition temperature over 45° C., said process comprises no voluntary added earth alkali metals neither as ions nor in form of salts.
By no voluntary added is meant that traces of earth alkali metals in form of ions or salts could be accidently added as a minor impurity with other ions or salts during the respective process steps for manufacturing the composition. As examples notably impurities of calcium in sodium compounds are mentioned.
The earth alkali metals as traces or minor impurity present less than 30 ppm, preferably less than 20 ppm and more preferably less than 10 ppm and advantageously less than 9 ppm of the final multistage polymer composition and preferably the final dry multistage polymer composition.
Furthermore multivalent cations present less than 50 ppm, preferably less than 40 ppm, more preferably less than 30 ppm, still more preferably less than 25 ppm and advantageously less than 20 ppm of the multistage polymer composition. Multivalent cations have the general formula M b+ , wherein M present the cation, with b>1, and preferably 5>b>1.
The multivalent cations is the sum of all the eventually non-voluntary added traces of earth alkali metals in form of ions or salts and the eventually voluntary added multivalent cations. The voluntary added multivalent cations have the general formula M b+ , wherein M present the cation, with b≧2, and preferably 4≧b≧2. The voluntary added multivalent cations exclude earth alkali metals.
The respective monomers or monomer mixtures (A m ) and (B m ) for forming the layers (A) and (B) respectively comprising the polymers (A1) and (B1) respectively and the characteristics of the respective polymers (A1) and (B1) are the same as defined before for the definition of the polymers (A1) and (B1) for the composition.
The emulsion polymerization during the stage for layer (A) can be a grow-out process, a seeded grow-out process or an microagglomeration process.
Chain transfer agents are also useful in forming the polymer (A1). Useful chain transfer agents include those known in the art, including but not limited to ter-dodecylmercaptan, n-dodecylmercaptan, n-octylmercaptan, and mixtures of chain transfer agents. The chain transfer agent is used at levels from 0 to 2 percent by weight, based on the total core monomer content in monomer mixture (A m ).
Preferably the polymer (B1) is grafted on the polymer made in the previous stage and more preferably on the polymer (A1) made in the previous stage.
Polymerization initiators useful in producing the polymer (A1) and (B1) include, but are not limited to a persulfate salt such as potassium persulfate, ammonium persulfate, and sodium persulfate; an organic peroxide such as tert-butyl hydroperoxide, cumene hydroperoxide, benzoyl peroxide, lauroyl peroxide, p-menthane hydroperoxide, and diisopropylbenzene hydroperoxide; an azo compound such as azobisisobutyronitrile, and azobisisovaleronitrile; or a redox initiator. However, it is preferable to use catalytic systems of redox type formed by the combination of a peroxide compound, for example as mentioned above, with a reducing agent, in particular such as alkali metal sulfite, alkali metal bisulfite, sodium formaldehyde sulfoxylate (NaHSO 2 HCHO), an alkali salt of an organic sulfinic acid derivative, ascorbic acid, glucose, and in particular those of the said catalytic systems which are water-soluble, for example potassium persulfate/sodium metabisulfite or alternatively diisopropylbenzene hydroperoxide/sodium formaldehyde sulfoxylate or even more complicate systems as for example ferrous sulfate/dextrose/sodium pyrophosphate.
The initiators do not contain any voluntary added earth alkali metals (group IIA from the periodic system of elements). The initiator might contain however other multivalent cations that are not earth alkali metals.
For the emulsion polymerization during the two stages for making layer (A) comprising polymer (A1) and layer (B) comprising a polymer (B1) as emulsifying agent any one of the known surface-active agents, whether anionic, nonionic or even cationic may be used. In particular, the emulsifying agent may be chosen from anionic emulsifying agents, such as sodium or potassium salts of fatty acids, in particular sodium laurate, sodium stearate, sodium palmitate, sodium oleate, mixed sulphates of sodium or of potassium and of fatty alcohols, in particular sodium lauryl sulphate, sodium or potassium salts of sulphosuccinic esters, sodium or potassium salts of alkylarylsulphonic acids, in particular sodium dodecylbenzenesulphonate, and sodium or potassium salts of fatty monoglyceride monosulphonates, or alternatively from nonionic surfactants, such as the reaction products of ethylene oxide and of alkylphenol or of aliphatic alcohols, alkylphenols. Use may also be made of mixtures of such surface-active agents, if necessary.
More preferably the emulsifying agent is chosen from an anoinic surface-active agent. Advantageously the emulsifying agent is chosen from anionic surface-active agents that comprise a carboxylate group or a phosphate group.
More advantageously the emulsifying agent is a carboxylate or carboxylic acid salt.
Coagulation in step c) of the process of the invention is made by aggregation of the primary polymer particles at the end of the emulsion polymerization by adding an aqueous electrolyte solution under stirring. The coagulation is not made with multivalent cations. Multivalent cations are to be avoided in the electrolyte solution. No multivalent cations are voluntary added to the electrolyte solution.
Preferably the coagulation is made with a solution comprising an inorganic acid or a salt of an alkali metal. More preferably the inorganic acid is chosen from but not limited to HCl, H 2 S0 4 , H 3 PO 4 . Advantageously a 1 molar aqueous solution of the inorganic acid has a pH≦1.
More preferably the alkali metal salt is a sodium or potassium salt. For example the alkali metal salt can be chosen from NaCl, KCl, Na 2 SO 4 , Na 3 PO 4 Na 2 HPO 4 , but is not limited on this list.
In a first more preferably embodiment the coagulation is made with a solution comprising an inorganic acid. Advantageously the inorganic acid is chosen from but not limited to HCl, H 2 S0 4 , H 3 PO 4 .
In a second more preferably embodiment the coagulation is made with a solution comprising a salt of an alkali metal. Advantageously the alkali metal salt is chosen from NaCl, KCl, Na 2 SO 4 , Na 3 PO 4 Na 2 HPO 4 or mixtures therof.
Adjusting the pH in step d) of the process of the invention is preferably made by adding sodium or potassium hydroxide or aqueous buffer solution after the coagulation step.
The washing in step e) of the process of the invention is made by water, diluted aqueous solutions or aqueous buffer solutions. After the washing step the pH is between 5 and 10. The coagulated multistage polymer after step e) is in form of a wet cake. The wet cake contains less than 60% of water.
Step f) concerns the addition of an aqueous solution or dispersion comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V.
Preferably the step f) concerning the addition of an aqueous solution or dispersion comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V is made after the coagulation step c).
In order to add aqueous solution or dispersion comprising a phosphorous containing compound, said the solution or dispersion is prepared by simple mixing of a known defined quantity of the phosphorous containing compound with water.
In one embodiment the aqueous solution or dispersion comprising the phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V is added by washing the multistage polymer which contains less than 60 wt % of water with said aqueous solution or dispersion comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V.
In a second embodiment the aqueous solution or dispersion comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V is added on the wet cake after coagulation step and filtration step. After the filtration a wet cake is obtained that contains less than 60 wt % of water. Afterwards the wet cake is dried.
In a third embodiment the aqueous solution or dispersion comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V is added during drying step of the multistage polymer, when the multistage polymer composition comprises still at least 10 wt % of water. No further separation between liquid phase that can contain solids or salts and solid phase takes place. All added phosphorous stays with the multistage polymer.
The phosphorous containing compound is preferably chosen from organophosphorous compound, a phosphate salt, phosphoric acid, phosphonate salts, phosphonic acid and their respective esters and mixtures thereof.
Phosphate ester general structure P(═O)(OR) 3 , where at least one group R is an alkyl group. Phosphonates are esters of phosphonic acid and have the general formula RP(═O) (OR′) 2 , where at least one group R or R′ is an alkyl group.
By organophosphorous compound in the present invention are understood compounds with P—C and P—O—C bonds.
More preferably the phosphorous containing compound is chosen from organophosphorous compound having a P—O—C bond, a phosphate salt, phosphoric acid, phosphonate salts, phosphonic acid and ester and mixtures thereof.
Phosphate salts are salts that have as anion dihydrogenophosphate (H 2 PO 4 − ), hydrogenophosphate (HPO 4 2− ) or phosphate (PO 4 3− ).
Phosphonate salts are salts that have as anion dihydrogenophosphonate (H 2 PO 3 − ) or hydrogenophosphate (HPO 3 2− ).
The present invention relates also to the use of the multistage polymer as impact modifier in thermoplastic polymers.
The present invention relates further to a thermoplastic composition comprising the multistage polymer and a thermoplastic polymer.
With regard to the thermoplastic polymer that is part of the thermoplastic composition according to the invention it can be chosen among poly(vinyl chloride) (PVC), chlorinated poly(vinyl chloride) (C-PVC), polyesters as for example poly (ethylene terephtalate) (PET) or poly(butylen terephtalate) (PBT) polyhydroxyalkanoates (PHA) or polylactic acid (PLA), cellulose acetate, polystyrene (PS), polycarbonates (PC), polyethylene, poly (methyl methacrylate)s (PMMA), (meth)acrylic copolymers, thermoplastic poly(methyl methacrylate-co-ethylacrylates), poly(alkylene-terephtalates), poly vinylidene fluoride, poly(vinylidenchloride), polyoxymethylen (POM), semi-crystalline polyamides, amorphous polyamides, semi-crystalline copolyamides, amorphous copolyamides, polyetheramides, polyesteramides, copolymers of styrene and acrylonitrile (SAN), and their respective mixtures or alloys. According to a preferred embodiment the thermoplastic resin composition comprises polycarbonate (PC) and/or polyester (PET or PBT) or PC or polyester alloys. The alloys for example may be PC/ABS (poly(Acrylonitrile-co-butadiene-co-styrene), PC/ASA, PC/polyester or PC/PLA.
Preferably, if the thermoplastic polymer in the thermoplastic polymer composition comprises polycarbonate (PC) and/or polyester (PET or PBT) or PC or polyester alloys the polymer (A) of the multistage polymer is chosen from isoprene homopolymers or butadiene homopolymers, isoprene-butadiene copolymers, copolymers of isoprene with at most 98 wt % of a vinyl monomer and copolymers of butadiene with at most 98 wt % of a vinyl monomer.
Concerning the polycarbonate (PC), it can be aromatic, semi-aromatic and/or aliphatic (particularly based on isosorbide).
With regard to the thermoplastic composition comprising the multistage polymer and a thermoplastic polymer, the proportions between the multistage polymer of the invention and the thermoplastic polymer are between 0.5/99.5 and 50/50, preferably between 1/98 and 30/70, more preferably between 2/98 and 20/80 and advantageously between 2/98 and 15/85.
[Methods of Evaluation]
Glass Transition Temperature
The glass transitions (Tg) of the polymers are measured with equipment able to realize a thermo mechanical analysis. A RDAII “RHEOMETRICS DYNAMIC ANALYSER” proposed by the Rheometrics Company has been used. The thermo mechanical analysis measures precisely the visco-elastics changes of a sample in function of the temperature, the strain or the deformation applied. The apparatus records continuously, the sample deformation, keeping the stain fixed, during a controlled program of temperature variation.
The results are obtained by drawing, in function of the temperature, the elastic modulus (G′), the loss modulus and the tan delta. The Tg is higher temperature value read in the tan delta curve, when the derived of tan delta is equal to zero.
Particle Size Analysis
The particle size of the primary particles after the multistage polymerization is measured with a Zetasizer Nano S90 from MALVERN. The particle size of the polymer powder after coagulation is measured with Malvern Mastersizer 3000 from MALVERN.
For the estimation of weight average powder particle size, particle size distribution and ratio of fine particles a Malvern Mastersizer 3000 apparatus with a 300 mm lenses, measuring a range from 0.5-880 μm is used.
D (v, 0.5) or more short D50 is the particle size at which 50% of the sample has size less then and 50% of the sample have a size larger then that size, or in other words the equivalent volume diameter at 50% cumulative volume. This size is also known as volume median diameter that is related to the mass median diameter by the density of the particles by the density of the particles assuming a size independent density for the particles.
D (v, 0.1) or D10 is the particle size at which 10% of the sample is smaller then that size, or in other words the equivalent volume diameter at 10% cumulative volume.
D (v, 0.9) or D90 is the particle size at which 90% of the sample are smaller then that size.
Analyses of Phosphor Content and Multivalent Cations.
The phosphorous content is measured with Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES). The result is expressed in ppm based on phosphor (P) or the respective multivalent cation (M b+ with b>1) in relation to the multistage polymer. The analysis does not allow to give the structure of the composition containing phosphorus or multivalent cation.
pH Measurement
The pH value of the respective products is measured with Procedure to obtain the pH of the final powder:
5 g of dried powder are dispersed in 20 mL of demineralized water under stirring during 10 minutes at 45° C. Then, the slurry is filtrated on a Wattman filter in paper. The pH of the filtrated water is measured at room temperature.
The pH value is obtained using a Fisher Scientific glass probe connected to a Eutech Instrument pH 200 series pH-meter preliminary calibrated with standard buffer solutions.
EXAMPLES
Example 1
Synthesis of Multistage Polymer (Core-Shell Particles)
First stage—polymerization of core: To a 20 litres high-pressure reactor was charged: de-ionized water 116.5 parts, emulsifier potassium salt of beef tallow fatty acid 0.1 part, 1,3-butadiene 21.9 parts, t-dodecyl mercaptan 0.1 parts, and p-menthane hydroperoxide 0.1 parts as an initial kettle charge. The solution was heated, with agitation, to 43° C. at which time a redox-based catalyst solution was charged (water 4.5 parts, sodium tetrapyrophosphate 0.3 parts, ferrous sulphate 0.004 parts and dextrose 0.3 parts), effectively initiating the polymerization. Then the solution was further heated to 56° C. and held at this temperature for a period of three hours. Three hours after polymerization initiation, a second monomer charge (77.8 parts BD, t-dodecyl mercaptan 0.2 parts), one-half of an additional emulsifier and reductant charge (de-ionized water 30.4 parts, emulsifier potassium salt of beef tallow fatty acid 2.8 parts, dextrose 0.5 parts) and additional initiator (p-menthane hydroperoxide 0.8 parts) were continuously added over eight hours. Following the completion of the second monomer addition, the remaining emulsifier and reductant charge plus initiator was continuously added over an additional five hours. Thirteen hours after polymerization initiation, the solution was heated to 68° C. and allowed to react until at least twenty hours had elapsed since polymerization initiation, producing polybutadiene rubber latex, R1. The resultant polybutadiene rubber latex (R1) contained 38% solids and had a weight average particle size of about 160 nm.
Second stage—Polymerization of shell 1 (outer shell): into a 3.9 litres reactor was charged 75.0 parts, on a solids basis, of polybutadiene rubber latex R1, 37.6 parts de-ionized water, and 0.1 parts sodium formaldehyde sulfoxylate. The solution was agitated, purged with nitrogen, and heated to 77° C. When the solution reached 77° C., a mixture of 22.6 parts methyl methacrylate, 1.4 parts divinyl benzene and 0.1 parts t-butyl hydroperoxide initiator was continuously added over 70 minutes, followed by o hold period of 80 minutes. Thirty minutes after the onset of the hold period, 0.1 parts of sodium formaldehyde sulfoxylate and 0.1 parts t-butyl hydroperoxide were added to the reactor at once. Following the 80-minute hold period, a stabilization emulsion was added to the graft copolymer latex. The stabilization emulsion was prepared by mixing 3.2 parts de-ionized water (based on graft copolymer mass), 0.1 parts oleic acid, 0.1 parts potassium hydroxyde, and 0.9 parts octadecyl-3-(3,5-di-tertbutyl-4-hydroxyphenyl)propionate. The resultant core shell latex (G1) had a weight average particle size of about 180 nm.
Coagulation: In a jacketed vessel of 3 L, equipped with a stirrer is put successively 500 g of latex of core-shell particles (G1) for having a solid content of 14.1%. Under stirring at 300 r/min, the heat of the solution is raised at 52° C. and then injected a 1.6% aqueous sulphuric acid solution resulting in a coagulated material that was heat treated at 96° C. The pH was adjusted with NaOH during the coagulation between 2 and 6. Subsequently, the coagulated material was filtered on centrifuge and washed with de-ionized water. Then, the pH is measured and adjusted with aqueous solution of sodium hydroxide for being between 5 and 9. The resultant polymer (P1) had a neutral pH (6<pH<7) and an average particle size of about 141 μm.
Addition of phosphate buffer solution: in a 2 litres calibrated flask is put 750 g of graft copolymer P1 (solid content 60 wt %) and is added 99 mL of a aqueous solution of Na 2 HPO 4 (disodium hydrogen phosphate) and KH 2 PO 4 (potassium dihydrogen phosphate) comprising expressed in phosphorous a concentration of 2.97 mg/ml.
Drying. The final powder PP1 (P1+phosphate) is put in a ventilated oven during 48 h at 50° C. and recovered after complete drying, humidity<1 wt %.
Example 2
The synthesis of multistage polymer (core-shell particles) is the same as in example 1.
Coagulation without pH adjusting after the coagulation: in a jacketed vessel of 3 L, equipped with a stirrer is put successively 500 g of latex of core-shell particles (G1) for having a solid content of 14.1%. Under stirring at 300 r/min, the heat of the solution is raised at 52° C. and then injected a 1.6% aqueous sulfuric acid solution resulting in a coagulated material that was heat treated at 96° C. The pH was adjusted during the coagulation between 2 and 6. Subsequently, the coagulated material was filtered on centrifuge and washed with de-ionized water to give P2.
Addition of phosphate buffer solution: in a 2 litres calibrated flask is put 750 g of graft copolymer (solid content 60 wt %), P2 and are added 99 mL of a aqueous solution of Na 2 HPO 4 (disodium hydrogeno phosphate) and KH 2 PO 4 (potassium dihydrogen phosphate) comprising expressed in phosphorous a concentration of 2.97 mg/ml.
Drying. The final powder PP2 is put in a ventilated oven during 48 h at 50° C. and recovered after complete drying.
Example 3 ((Comparative))
The synthesis of multistage polymer (core-shell particles) is the same as in example 1.
Coagulation: in a jacketed vessel of 3 L, equipped with a stirrer is put successively 500 g of latex of core-shell particles (G1) from example 1 for having a solid content of 14.1%. Under stirring at 300 r/min, the heat of the solution is raised at 52° C. and then injected a 1.6% aqueous sulphuric acid solution resulting in a coagulated material that was heat treated at 96° C. The pH was adjusted during the coagulation between 2 and 6. Subsequently, the coagulated material was filtered on centrifuge and washed with de-ionized water. Then, the pH is measured and adjusted with aqueous solution of sodium hydroxide for being between 5 and 9. The resultant polymer (P1) had a neutral pH (5<ph<8) and an average particle size of about 141 μm (method, meme taille que example 1!)
Addition of phosphate buffer solution: in a 2 litres calibrated flask is put 750 g of graft copolymer P1 (solid content 60 wt %) and are added 46 mL of an aqueous solution of Na 2 HPO 4 (disodium hydrogeno phosphate) and KH 2 PO 4 (potassium dihydrogen phosphate) comprising expressed in phosphorous a concentration of 2.97 mg/ml.
Drying: the final powder PP3 is put in a ventilated oven during 48 h at 50° C. and recovered after complete drying
Example 4 (Comparative)
The synthesis of multistage polymer (core-shell particles) is the same as in example 1.
Coagulation: in a jacketed vessel of 3 L, equipped with a stirrer is put successively 500 g of latex of core-shell particles (G1) from example 1 for having a solid content of 14.1%. Under stirring at 300 r/min, the heat of the solution is raised at 52° C. and then injected a 1.6% aqueous sulfuric acid solution resulting in a coagulated material that was heat treated at 96° C. The pH was adjusted during the coagulation between 2 and 6. Subsequently, the coagulated material was filtered on centrifuge and washed with de-ionized water. Then, the pH is measured and adjusted with aqueous solution of sodium hydroxide for being between 5 and 9. The resultant polymer (P1) had a neutral pH (6<ph<7) and a weight average particle size of about 141 μm.
Addition of phosphate buffer solution: in a 2 litres calibrated flask is put 750 g of graft copolymer P1 (solid content 60 wt %) and are added 15 mL of an aqueous solution of Na 2 HPO 4 (disodium hydrogeno phosphate) and KH 2 PO 4 (potassium dihydrogen phosphate) comprising expressed in phosphorous a concentration of 2.97 mg/ml.
Drying: the final powder PP4 is put in a ventilated oven during 48 h at 50° C. and recovered after complete drying.
Example 5 (Comparative)
The synthesis of multistage polymer (core-shell particles) is the same as in example 1.
Coagulation: in a jacketed vessel of 3 L, equipped with a stirrer is put successively 500 g of latex of core-shell particles (G1) from example 1 for having a solid content of 14.1%. Under stirring at 300 r/min, the heat of the solution is raised at 52° C. and then injected a 1.6% aqueous sulphuric acid solution resulting in a coagulated material that was heat treated at 96° C. The pH was adjusted during the coagulation between 2 and 6. Subsequently, the coagulated material was filtered on centrifuge and washed with warm de-ionized water. Then, the pH is measured and adjusted with aqueous solution of sodium hydroxide for being between 5 and 9. The resultant polymer (P1) had a neutral pH (6<ph<7) and an average particle size of about 141 μm.
No addition of phosphate buffer solution.
Drying: the final powder P5 is put in a ventilated oven during 48 h at 50° C. and recovered after complete drying.
The phosphor content of all powders is estimated with Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES). The results are summarized in table 1.
TABLE 1
Summery of the powder characteristics
Coagulation
Agent
P/[ppm]
Example 1
Sulphuric acid
650
Example 2
Sulphuric acid
650
Example 3
Sulphuric acid
300
Example 4
Sulphuric acid
100
Example 5
Sulphuric acid
80
Table 1 indicates that the phosphor content decreases with the examples 3 and 4, as lesser quantity of the phosphate buffer solution is added to the polymer powder after coagulation. In example 5 the phosphor content is the lowest as no phosphate buffer solution is added to the polymer powder after coagulation. The phosphorous in example 5 is due to the products used during the synthesis of the multistage polymer.
The dry multistage polymer powders P1 to P5 are compounded with polycarbonate at 5 wt % for producing compounds 1 to 5.
Preparation of the impact modified compound compositions, the respective impact modifier powders P1 to P6 are mixed with the thermoplastic resin polycarbonate Lexan ML5221 from SABIC (at 5 wt % with the help of an extruder type Clextral (double diameter 25 mm, length 700 mm) using temperatures between from 100° C. up to 320° C. depending on the respective zones throughout the whole extruder.
The respective obtained compounds are heat aged at 120° C. The optical properties of the compounds are evaluated. The color change is observed by measuring the parameter b*. The b* value is used to characterize the principal yellowing off the samples. The b* value measures the blue and the yellow of the colour. Colours tending toward the yellow have a positive b* value while those tending toward the blue have a negative b* value. The b* values is measured using a colorimeter (especially according to the ASTM E 308 standard). The colour change is observed as a function of time: samples kept at 120° C. for 4 days.
If the initial color is close to zero it is considered that the thermoplastic composition comprising the impact modifiers of the invention is acceptable. The b* value should not larger than 10 after 4 days of thermal aging.
TABLE 2
color of heat aged compounds
Multistage polymer
b*
b*
from
initial
after 4 days at 120° C.
Compound 1
Example 1
0.43
4.02
Compound 2
Example 2
−1.55
5.47
Compound 3
Example 3
0.73
13.77
Compound 4
Example 4
−2.45
15.34
Compound 5
Example 5
−0.84
20.74
TABLE 3
impact strength of thermoplastic compositions
Multistage
IZOD impact strength
IZOD impact
polymer
[kJ/m2]
strength [kJ/m2]
from
at 23° C.
at −30° C
Compound 1
Example 1
48.0
37.0
Compound 2
Example 3
—
—
Compound 3
Example 4
45.4
35.6
Compound 4
Example 5
—
—
Compound 5
Example 6
45.9
41.0
1.PublishNumber: US-2017355801-A1
2.Date Publish: 20171214
3.Inventor: COUFFIN Aline O.
PIRRI ROSANGELA
MALET FREDERIC
4.Inventor Harmonized: COUFFIN ALINE O(FR)
PIRRI ROSANGELA(FR)
MALET FREDERIC(FR)
5.Country: US
6.Claims:
(en)The present invention relates to a multistage polymer, its composition, its process of preparation, and its use as impact modifier in thermoplastic compositions. More particularly the present invention relates a process for manufacturing a multistage polymer, a multistage polymer in thermoplastic compositions, which provides the composition having satisfying thermal stability.
7.Description:
(en)FIELD OF THE INVENTION
The present invention relates to a multistage polymer, its composition and its process of preparation.
In particular the present invention it relates to a multistage polymer, its composition and its process of preparation and its use in thermoplastic compositions.
More particularly the present invention relates to a process for manufacturing a multistage polymer, said multistage polymer in a thermoplastic composition, gives composition is having a satisfying thermal stability.
TECHNICAL PROBLEM
Impact modifiers are widely used to improve the impact strength for thermoplastic compositions with the aim to compensate their inherent brittleness or the embrittlement that occurs at sub zero temperatures, notch sensitivity and crack propagation. So an impact modified polymer is a polymeric material whose impact resistance and toughness have been increased by the incorporation of phase nano domains of a rubbery material.
This is usually done due to the introduction of microscopic rubber particles into the polymer matrix that can absorb the energy of an impact or dissipate it. One possibility is to introduce the rubber particles in form of core-shell particles. These core-shell particles that possess very generally a rubber core and a polymeric shell, having the advantage of a proper particle size of the rubber core for effective toughening and the grafted shell in order to have the adhesion and compatibility with the thermoplastic matrix.
The performance of the impact modification is a function of the particles size, especially of the rubber part of the particle, and its quantity. There is an optimal average particle size in order to have the highest impact strength for a given quantity of added impact modifier particles.
These primary impact modifier particles are usually added in form of powder particles to the thermoplastic material. These powder particles are agglomerated primary impact modifier particles. During the blending of the thermoplastic material with the powder particles the primary impact modifier particles are regained and are dispersed more or less homogenously dispersed in the thermoplastic material.
While the particle size of the impact modifier particles in the range of nanometers, the range of the agglomerated powder particles is in the range of micrometers.
Agglomeration during the recovery can be obtained by several processes, as for example, spray drying, coagulation, shearing, or freeze drying or combination of spray drying and coagulation techniques.
It important to avoid negative influence of the impact modifier powder on the thermoplastic polymer composition to which the impact modifier is added. As negative influence, it is understood, for example the color stability, the thermal stability, the hydrolysis stability of the thermoplastic polymer comprising the impact modifier, either on function of the time or the temperature or both.
All these influences might occur due to the architecture of the core-shell but more particularly the impurities and side products employed during the synthesis and treatment of the impact modifier powder. Usually, there is no special purification step of the impact modifier, just a separation of solid versus liquid. Therefore more or less important quantities of any chemical compound (impurities, by-products) employed are still incorporated in the impact modifier. The concerned quantities of them may vary. However these chemical compounds should not influence at all or have only a minor influence on the thermoplastic material in a major way as for example degradation of optical and/or mechanical and/or rheological properties with time and/or temperature and/or hygrometry.
Extensive washing or purification might get rid of some of the compounds coming from impurities or products used during the synthesis that might have negative influence of the impact modifier powder on the performance thermoplastic polymer composition.
On the other hand all processes are extremely cost sensitive. A slight improvement in process can result in a significant market advantage.
The objective of the present invention is to propose a multistage polymer having a satisfying thermal stability.
An additional objective of the present invention is also to have a multistage polymer having a satisfying thermal stability that can be used as impact modifier.
Still another objective of the present invention is to propose a process for manufacturing a multistage polymer having a satisfying thermal stability.
An additional objective of the present invention is a thermoplastic composition comprising a multistage polymer, said composition is having a satisfying thermal stability.
Still an additional objective is having a process for preparing for manufacturing a multistage polymer, said multistage polymer in a thermoplastic composition, gives composition is having a satisfying thermal stability.
BACKGROUND OF THE INVENTION
Prior Art
The document EP0900827 discloses an impact modified carbonate polymer composition having improved resistance to degradation and improved thermal stability. According to the document the impact modifier has to be essentially free of basic compounds from the emulsion polymerization, and especially troublesome are emulsifiers of alkali salts of fatty acids as alkali metal carboxylate. The impact modifier is preferably of a shell-core structure and is prepared by an emulsion polymerization process and has a pH of about 3 to about 8. A preferred emulsifier is an alkyl sulfonate having an alkyl group of C 6 -C 18 carbons.
The document EP2189497 discloses polymer compositions containing phosphates and especially the process for obtaining them. The polymer composition is a polymer obtained by a multi stage process and is an impact modifier. The phosphate salts are introduced in order to reduce or eliminate the deleterious effects of the multivalent cations that are present in polymer obtained by a multi stage process. The use of such a process allows a coagulated polymer to be used as an impact additive to a matrix without causing the deleterious effects from the multivalent cation that would otherwise have occurred. The process implies a washing step with water to get first rid of salts and ions and then adding an aqueous alkaline phosphate solution. The process requires a lot of water and consequently also the time and energy consuming steps of separation of water from polymer composition.
The document EP 2465882 discloses improved impact modified thermoplastic compositions. The thermoplastic compositions comprise a polymeric impact modifier with a core-shell structure made by a multistage process and recovered by a special process controlling and adjusting the pH value. Coagulation is done with salts and preferably magnesium sulfate.
The document WO2009/118114 describes an impact modified polycarbonate composition with a good combination of color, hydrolysis and melt stability. The rubber core is based on polybutadiene. For the preparation of the graft rubber polymer salts of fatty acids, especially of carboxylic acids are used. The yellow index of the compositions given with injection temperature at 260° C. is quite important: 20 or higher.
The document WO2009/126373 describes functional MBS impact modifiers synthesized by a multistage emulsion polymerization. At the end of the synthesis the reaction mixture obtained is coagulated in order to separate the polymer. The coagulating treatment is performed by bringing into contact the reaction mixture with a saline solution (calcium chloride or aluminum chloride—CaCl 2 or AlCl 3 ) or a solution acidified with concentrated sulfuric acid and then to separate, by filtration, the solid product resulting from the coagulating, the solid product then being washed and dried to give a graft copolymer as a powder.
The present invention aims to avoid at least one of the inconvenient of the state of the art.
There is a need for improving the process of making a multistage polymer, by optimizing the steps involved, while allowing the obtained multistage polymer an increase of the performance as impact additive in thermoplastic compositions.
BRIEF DESCRIPTION OF THE INVENTION
Surprisingly it has been found that a polymer composition in form of polymeric particles made by a multistage process comprising
at least one stage giving layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C. and at least one subsequent stage giving layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C.,
obtained by a multistage process characterized that the polymer composition comprises less than 50 ppm of multivalent cations and at least 350 ppm of phosphorous in form of a phosphorous containing compound with phosphorous in the oxidation stage +III or +V, yields to a product having satisfying thermal aging properties.
Surprisingly it has also been found that a process for manufacturing the polymer composition comprising a multistage polymer comprising the steps of
a) polymerizing by emulsion polymerization of a monomer or monomers mixture (A m ) to obtain during this stage one layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C. b) polymerizing by emulsion polymerization in presence of the polymer obtained in step a) of a monomer or monomer mixture (B m ) to obtain during this subsequent stage a layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C. c) coagulating the multistage polymer d) adjusting the pH to a value between 5 to 10 e) washing the multistage polymer f) addition of an aqueous solution comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V
characterized that the coagulation step is not made with multivalent cations, and the polymer composition comprises at least 350 ppm of phosphorous in form of a phosphorous containing compound with phosphorous in the oxidation stage +III or +V, yields to a product having satisfying thermal aging properties.
DETAILED DESCRIPTION OF THE INVENTION
According to a first aspect, the present invention relates to a polymer composition in form of polymeric particles of a multistage polymer made by a multistage process comprising
at least one stage giving layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C. and at least one subsequent stage giving layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C.,
obtained by a multistage process characterized that the polymer composition comprises less than 50 ppm of multivalent cations and at least 350 ppm of phosphorous in form of a phosphorous containing compound with phosphorous in the oxidation stage +III or +V.
According to a second aspect the present invention relates to a process for manufacturing a polymer composition comprising a multistage polymer comprising the steps of
a) polymerizing by emulsion polymerization of a monomer or monomer mixture (Am) to obtain during this stage one layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C. b) polymerizing by emulsion polymerization in presence of the polymer obtained in step a) of a monomer or monomers mixture (B m ) to obtain during this subsequent stage a layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C. c) coagulating the multistage polymer d) adjusting the pH to a value between 5 to 10 e) washing the multistage polymer f) addition of an aqueous solution comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V
characterized that the coagulation step is not made with multivalent cations, and the polymer composition comprises at least 350 ppm of phosphorous in form of a phosphorous containing compound with phosphorous in the oxidation stage +III or +V.
According to a third aspect the present invention relates to a process for manufacturing a polymer composition in form of polymeric particles comprising a multistage polymer comprising the steps of
a) polymerizing by emulsion polymerization of a monomer or monomer mixture (A m ) to obtain during this stage one layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C. b) polymerizing by emulsion polymerization in presence of the polymer obtained in step a) of a monomer or monomers mixture (B m ) to obtain during this subsequent stage a layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C. c) coagulating the multistage polymer d) adjusting the pH to a value between 5 to 10 e) washing the multistage polymer f) addition of an aqueous solution comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V
characterized that the coagulation step is not made with multivalent cations, and the polymer composition comprises at least 350 ppm of phosphorous in form of a phosphorous containing compound with phosphorous in the oxidation stage +III or +V.
By the term “polymer powder” as used is denoted a polymer comprising powder grain in the range of at least 1 micrometer (μm) obtained by agglomeration of primary polymer comprising particles in the nanometer range.
By the term “primary particle” as used is denoted a spherical polymer comprising particle in the nanometer range. Preferably the primary particle has a weight average particle size between 20 nm and 500 nm.
By the term “particle size” as used is denoted the volume average diameter of a particle considered as spherical.
By the term “copolymer” as used is denoted that the polymer consists of at least two different monomers.
By “multistage polymer” as used is denoted a polymer formed in sequential fashion by a multi-stage polymerization process. Preferred is a multi-stage emulsion polymerization process in which the first polymer is a first-stage polymer and the second polymer is a second-stage polymer, i.e., the second polymer is formed by emulsion polymerization in the presence of the first emulsion polymer, with at least two stages that are different in composition.
By the term “(meth)acrylic” as used is denoted all kind of acrylic and methacrylic monomers.
By the term “(meth)acrylic polymer” as used is denoted that the (meth)acrylic polymer comprises essentially polymers comprising (meth)acrylic monomers that make up 50 wt % or more of the (meth)acrylic polymer.
By the term “impact modifier” as used is denoted a compound comprising an elastomer or rubber that can be added or incorporated in a thermoplastic compound to improve its impact resistance.
By the term “rubber” as used is denoted the thermodynamic state of the polymer above its glass transition
With regard to the multistage polymer of the invention, it is a polymer particle having a multilayer structure comprising at least one layer (A) comprising a polymer (A1) having a glass transition temperature below 0° C. and at least another layer (B) comprising a polymer (B1) having a glass transition temperature over 45° C.
The ratio of layer (A)/layer (B) in the multistage polymer is not particularly limited, but preferably it is in a range in weight between 10/90 and 95/5, more preferably 40/60 and 95/5 advantageously 60/40 to 90/10 and most advantageously between 70/30 and 90/10.
The polymer particle having a multilayer structure is spherical. The polymer particle having a multilayer structure is also called the primary particle. The polymer particle has a weight average particle size between 20 nm and 500 nm. Preferably the weight average particle size of the polymer particle is between 50 nm and 400 nm, more preferably between 75 nm and 350 nm and advantageously between 80 nm and 300 nm.
The polymer particle according to the invention is obtained by a multistage process such as two or three stages or more stages.
Preferably the polymer (A1) having a glass transition temperature below 0° C. in the layer (A) is not made during the last stage of the multistage process. The polymer (A1) is having a glass transition temperature below 0° C. in the layer (A) never forms the external layer or outer shell of the polymer particle having the multilayer structure.
Preferably the polymer (B1) having a glass transition temperature above 45° C. in the layer (B) is the external layer of the polymer particle having the multilayer structure.
There could be additional intermediate layers made by intermediate steps between the polymer (A1) having a glass transition temperature below 0° C. in the layer (A) and the layer (B) comprising a polymer (B1) having a glass transition temperature over 45° C. This would lead to a multilayered particle.
The glass transition temperature (Tg) of the polymer (A1) is less than 0° C., preferably less than −10° C., advantageously less than −20° C. and most advantageously less than −25° C. and more most advantageously less than −40° C.
More preferably the glass transition temperature Tg of the polymer (A1) is between −120° C. and 0° C., even more preferably between −90° C. and −10° C. and advantageously between −80° C. and −25° C.
Preferably the glass transition temperature Tg of the polymer (B1) is between 45° C. and 150° C. The glass transition temperature of the polymer (B1) is more preferably between 60° C. and 150° C., still more preferably between 80° C. and 150° C. and advantageously between 90° C. and 150° C.
The glass transition temperature Tg can be estimated for example by dynamic methods as thermo mechanical analysis.
The polymer composition of the invention in form of polymeric particles of a multistage polymer can also be in form of a polymer powder. The polymer powder comprises agglomerated primary polymer particles made by the multistage process.
With regard to the polymer powder of the invention, it has a volume median particle size D50 between 1 μm and 500 μm. Preferably the volume median particle size of the polymer powder is between 10 μm and 400 μm, more preferably between 15 μm and 350 μm and advantageously between 20 μm and 300 μm.
The D10 of the particle size distribution in volume is at least 7 μm and preferably 10 μm.
The D90 of the particle size distribution in volume is at most 800 μm and preferably 500 μm, more preferably at most 350 μm.
With regard to the polymer (A1), mention may be made of homopolymers and copolymers comprising monomers with double bonds and/or vinyl monomers.
In a first embodiment the polymer (A1) is chosen from isoprene homopolymers or butadiene homopolymers, isoprene-butadiene copolymers, copolymers of isoprene with at most 98 wt % of a vinyl monomer and copolymers of butadiene with at most 98 wt % of a vinyl monomer. The vinyl monomer may be styrene, an alkylstyrene, acrylonitrile, an alkyl (meth)acrylate, or butadiene or isoprene. In a specific embodiment polymer (A1) is a butadiene homopolymer.
In a second embodiment the polymer (A1) is a (meth)acrylic polymer. A (meth)acrylic polymer according to the invention is a polymer comprising at least 50 wt % preferably at least 60 wt % and more preferably at least 70 wt % of monomers coming from acrylic or methacrylic monomers. The (meth)acrylic polymer according to the invention comprise less than 50 wt % preferably less than 40 wt % and more preferably less than 30 wt % of non acrylic or methacrylic monomers, which can copolymerize with the acrylic or methacrylic monomers.
More preferably the polymer (A1) of the second embodiment comprises at least 70 wt % monomers chosen from C1 to C12 alkyl (meth)acrylates. Still more preferably the polymer (A1) comprises at least 80 wt % of monomers C1 to C4 alkyl methacrylate and/or C1 to C8 alkyl acrylate monomers.
Most preferably the acrylic or methacrylic monomers of the polymer (A1) are chosen from methyl acrylate, ethyl acrylate, propyl acrylate, isopropyl acrylate, butyl acrylate, tert-butyl acrylate, methyl methacrylate, ethyl methacrylate, butyl methacrylate and mixtures thereof, as long as polymer (A1) is having a glass transition temperature of less then 0° C.
The polymer (A1) may be completely or partly crosslinked. All that is required is to add at least one difunctional monomer during the preparation of the polymer (A1). These difunctional monomers may be chosen from poly(meth)acrylic esters of polyols, such as butanediol di(meth)acrylate and trimethylolpropane trimethacrylate. Other multifunctional monomers are, for example, divinylbenzene, trivinylbenzene, and triallyl cyanurate. The core can also be crosslinked by introducing into it, by grafting or as a comonomer during the polymerization, unsaturated functional monomers such as anhydrides of unsaturated carboxylic acids, unsaturated carboxylic acids and unsaturated epoxides. Mention may be made, by way of example, of maleic anhydride, (meth)acrylic acid and glycidyl methacrylate. The crosslinking may also be carried out by using the intrinsic reactivity of the monomers, for example in the case of the diene monomers.
With regard to the polymer (B1), mention may be made of homopolymers and copolymers comprising monomers with double bonds and/or vinyl monomers.
The polymer (B1) is chosen from styrene homopolymers, alkylstyrene homopolymers or methyl methacrylate homopolymers, or copolymers comprising at least 70 wt % of one of the above monomers and at least one comonomer chosen from the other above monomers, another alkyl (meth)acrylate, vinyl acetate and acrylonitrile. The shell may be functionalized by introducing into it, by grafting or as a comonomer during the polymerization, unsaturated functional monomers such as anhydrides of unsaturated carboxylic acids, unsaturated carboxylic acids and unsaturated epoxides. Mention may be made, for example, of maleic anhydride, (meth)acrylic acid glycidyl methacrylate, hydroxyethyl methacrylate and alkyl(meth)acrylamides.
Preferably the polymer (B1) is also a (meth)acrylic polymer.
Preferably the polymer (B1) comprises at least 70 wt % monomers chosen from C1 to C12 alkyl (meth)acrylates. Still more preferably the polymer (B1) comprises at least 80 wt % of monomers C1 to C4 alkyl methacrylate and/or C1 to C8 alkyl acrylate monomers.
Most preferably the acrylic or methacrylic monomers of the polymer (B1) are chosen from methyl acrylate, ethyl acrylate, butyl acrylate, methyl methacrylate, ethyl methacrylate, butyl methacrylate and mixtures thereof, as long as polymer (B1) is having a glass transition temperature of at least 60° C.
Advantageously the polymer (B1) comprises at least 70 wt % of monomer units coming from methyl methacrylate.
The polymer (B1) may be crosslinked by adding at least one multifunctional monomer during the preparation of the polymer (B1).
The multistage polymer of the invention, having a multilayer structure comprising at least one layer (A) comprising a polymer (A1) having a glass transition temperature below 0° C. and another layer (B) comprising a polymer (B1) having a glass transition temperature over 45° C., comprises no voluntary added earth alkali metals neither as ions nor in form of salts. The polymer composition in form of polymeric particles made by the multistage process comprises no voluntary added multivalent cations chosen from earth alkali metal.
By no voluntary added is meant that traces of earth alkali metals in form of ions or salts could be accidently added as a minor impurity with other ions or salts to the composition. Example notably impurities of calcium in sodium compounds are mentioned.
The earth alkali metals as traces or minor impurity present less than 30 ppm, preferably less than 20 ppm and more preferably less than 10 ppm, advantageously less than 9 ppm of the multistage polymer composition. The multivalent cation is chosen from Ca2+ or Mg2+.
Furthermore multivalent cations present less than 50 ppm, preferably less than 40 ppm, more preferably less than 30 ppm, still more preferably less than 25 ppm and advantageously less than 20 ppm of the multistage polymer composition and preferably the final dry multistage polymer composition. Multivalent cations have the general formula M b+ , wherein M present the cation, with b>1, and preferably 5>b>1.
The multivalent cations is the sum of all the eventually non-voluntary added traces of earth alkali metals in form of ions or salts and the eventually voluntary added multivalent cations. The voluntary added multivalent cations have the general formula M b+ , wherein M present the cation, with b≧2, and preferably 4≧b≧2. The voluntary added multivalent cations exclude earth alkali metals.
The multivalent cations including the earth alkali metals in the composition can be analysed by Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES).
The multistage polymer of the invention, having a multilayer structure has a pH value between 5 and 10 and preferable between 6 and 9, more preferable between 6 and 7.5 and advantageously between 6 and 7.
The multistage polymer of the invention comprises a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V.
The multistage polymer comprises at least 350 ppm, preferably at least 360 ppm, more preferably at least 370 ppm, still more preferably at least 380 ppm, advantageously at least 390 ppm and more advantagously at least 400 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound. The content of the phosphorous containing compound is calculated and expressed as phosphorous in view of the multistage polymer composition and not as phosphorous containing compound.
The multistage polymer comprises at most 2000 ppm, preferably at most 1900 ppm and more preferably at most 1800 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound.
The multistage polymer comprises between 350 ppm and 2000 ppm, preferable between 370 pmm and 1900 ppm and more preferably between 390 ppm and 1800 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound.
The quantity of phosphorous in the multistage polymer can be estimated by by Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES).
The oxidation stage is linked to the nature of the phosphorous containing compound added to the composition. Preferably there is no voluntary addition of any reducing or oxidizing agents, in order to change the oxidation stage of the phosphorous in the phosphorous containing compound.
The phosphorous containing compound is preferably chosen from organophosphorous compound, a phosphate salt, phosphoric acid, phosphonate salts, phosphonic acid and their respective esters and mixtures thereof.
By organophosphorous compound in the present invention are understood compounds with P—C and P—O—C bonds.
More preferably the phosphorous containing compound is chosen from organophosphorous compound having a P—O—C bond, a phosphate salt, phosphoric acid, phosphonate salts, phosphonic acid and ester and mixtures thereof.
Phosphate salts are salts that have as anion dihydrogenophosphate (H 2 PO 4 − ), hydrogenophosphate (HPO 4 2− ) or phosphate (PO 4 3− ).
Phosphonate salts are salts that have as anion dihydrogenophosphonate (H 2 PO 3 − ) or hydrogenophosphate (HPO 3 2− ).
With regard to the process for manufacturing a polymer composition comprising a multistage polymer comprising the steps of
a) polymerizing by emulsion polymerization of a monomer or monomer mixture (A m ) to obtain during this stage one layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C., b) polymerizing by emulsion polymerization in presence of the polymer obtained in step a) of a monomer or monomer mixture (B m ) to obtain during this subsequent stage a layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C., c) coagulating the multistage polymer, d) adjusting the pH to a value between 5 to 10, e) washing the multistage polymer, f) addition of an aqueous solution comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V.
Also with regard to the process for manufacturing a polymer composition in form of polymeric particles comprising a multistage polymer comprising the steps of
a) polymerizing by emulsion polymerization of a monomer or monomer mixture (A m ) to obtain during this stage one layer (A) comprising polymer (A1) having a glass transition temperature of less than 0° C., b) polymerizing by emulsion polymerization in presence of the polymer obtained in step a) of a monomer or monomer mixture (B m ) to obtain during this subsequent stage a layer (B) comprising a polymer (B1) having a glass transition temperature of at least 45° C., c) coagulating the multistage polymer, d) adjusting the pH to a value between 5 to 10, e) washing the multistage polymer, f) addition of an aqueous solution comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V.
The polymer composition comprising the multistage polymer or the polymer composition in form of polymeric particles comprising the multistage polymer obtained by said process comprises at least 350 ppm, preferably at least 360 ppm, more preferably at least 370 ppm, still more preferably at least 380 ppm, advantageously at least 390 ppm and more advantageously at least 400 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound. The content of the phosphorous containing compound is calculated and expressed as phosphorous in view of the multistage polymer composition and not as phosphorous containing compound.
The polymer composition comprising the multistage polymer or the polymer composition in form of polymeric particles comprising the multistage polymer obtained by said process comprises at most 2000 ppm, preferably at most 1900 ppm and more preferably at most 1800 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound.
The polymer composition comprising the multistage polymer or the polymer composition in form of polymeric particles comprising the multistage polymer obtained by said process comprises between 350 ppm and 2000 ppm, preferable between 370 pmm and 1900 ppm and more preferably between 390 ppm and 1800 ppm of phosphorous that has the oxidation stage of +III or +V. The phosphorous is part of a phosphorous containing compound.
The quantity of phosphorous in the multistage polymer can be estimated by by Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES).
The phosphorous containing compound is the same as defended before.
Preferably in step d) the pH value is adjusted between 6 and 9 more preferable between 6 and 7.5 and advantageously between 6 and 7.
The process might comprise the additional step g) of drying the polymer composition. A dry polymer composition according to the invention is a composition that comprises less than 1% of humidity or water. The humidity of a polymer composition can be measure with a thermo balance.
The drying of the polymer can be made in a oven or vacuum oven with heating of the composition for 48 hours at 50° C.
The process of the invention, for manufacturing the polymer composition comprising the multistage polymer having a multilayer structure comprising at least one layer (A) comprising a polymer (A1) having a glass transition temperature below 0° C. and another layer (B) comprising a polymer (B1) having a glass transition temperature over 45° C., said process comprises no voluntary added earth alkali metals neither as ions nor in form of salts.
By no voluntary added is meant that traces of earth alkali metals in form of ions or salts could be accidently added as a minor impurity with other ions or salts during the respective process steps for manufacturing the composition. As examples notably impurities of calcium in sodium compounds are mentioned.
The earth alkali metals as traces or minor impurity present less than 30 ppm, preferably less than 20 ppm and more preferably less than 10 ppm and advantageously less than 9 ppm of the final multistage polymer composition and preferably the final dry multistage polymer composition.
Furthermore multivalent cations present less than 50 ppm, preferably less than 40 ppm, more preferably less than 30 ppm, still more preferably less than 25 ppm and advantageously less than 20 ppm of the multistage polymer composition. Multivalent cations have the general formula M b+ , wherein M present the cation, with b>1, and preferably 5>b>1.
The multivalent cations is the sum of all the eventually non-voluntary added traces of earth alkali metals in form of ions or salts and the eventually voluntary added multivalent cations. The voluntary added multivalent cations have the general formula M b+ , wherein M present the cation, with b≧2, and preferably 4≧b≧2. The voluntary added multivalent cations exclude earth alkali metals.
The respective monomers or monomer mixtures (A m ) and (B m ) for forming the layers (A) and (B) respectively comprising the polymers (A1) and (B1) respectively and the characteristics of the respective polymers (A1) and (B1) are the same as defined before for the definition of the polymers (A1) and (B1) for the composition.
The emulsion polymerization during the stage for layer (A) can be a grow-out process, a seeded grow-out process or an microagglomeration process.
Chain transfer agents are also useful in forming the polymer (A1). Useful chain transfer agents include those known in the art, including but not limited to ter-dodecylmercaptan, n-dodecylmercaptan, n-octylmercaptan, and mixtures of chain transfer agents. The chain transfer agent is used at levels from 0 to 2 percent by weight, based on the total core monomer content in monomer mixture (A m ).
Preferably the polymer (B1) is grafted on the polymer made in the previous stage and more preferably on the polymer (A1) made in the previous stage.
Polymerization initiators useful in producing the polymer (A1) and (B1) include, but are not limited to a persulfate salt such as potassium persulfate, ammonium persulfate, and sodium persulfate; an organic peroxide such as tert-butyl hydroperoxide, cumene hydroperoxide, benzoyl peroxide, lauroyl peroxide, p-menthane hydroperoxide, and diisopropylbenzene hydroperoxide; an azo compound such as azobisisobutyronitrile, and azobisisovaleronitrile; or a redox initiator. However, it is preferable to use catalytic systems of redox type formed by the combination of a peroxide compound, for example as mentioned above, with a reducing agent, in particular such as alkali metal sulfite, alkali metal bisulfite, sodium formaldehyde sulfoxylate (NaHSO 2 HCHO), an alkali salt of an organic sulfinic acid derivative, ascorbic acid, glucose, and in particular those of the said catalytic systems which are water-soluble, for example potassium persulfate/sodium metabisulfite or alternatively diisopropylbenzene hydroperoxide/sodium formaldehyde sulfoxylate or even more complicate systems as for example ferrous sulfate/dextrose/sodium pyrophosphate.
The initiators do not contain any voluntary added earth alkali metals (group IIA from the periodic system of elements). The initiator might contain however other multivalent cations that are not earth alkali metals.
For the emulsion polymerization during the two stages for making layer (A) comprising polymer (A1) and layer (B) comprising a polymer (B1) as emulsifying agent any one of the known surface-active agents, whether anionic, nonionic or even cationic may be used. In particular, the emulsifying agent may be chosen from anionic emulsifying agents, such as sodium or potassium salts of fatty acids, in particular sodium laurate, sodium stearate, sodium palmitate, sodium oleate, mixed sulphates of sodium or of potassium and of fatty alcohols, in particular sodium lauryl sulphate, sodium or potassium salts of sulphosuccinic esters, sodium or potassium salts of alkylarylsulphonic acids, in particular sodium dodecylbenzenesulphonate, and sodium or potassium salts of fatty monoglyceride monosulphonates, or alternatively from nonionic surfactants, such as the reaction products of ethylene oxide and of alkylphenol or of aliphatic alcohols, alkylphenols. Use may also be made of mixtures of such surface-active agents, if necessary.
More preferably the emulsifying agent is chosen from an anoinic surface-active agent. Advantageously the emulsifying agent is chosen from anionic surface-active agents that comprise a carboxylate group or a phosphate group.
More advantageously the emulsifying agent is a carboxylate or carboxylic acid salt.
Coagulation in step c) of the process of the invention is made by aggregation of the primary polymer particles at the end of the emulsion polymerization by adding an aqueous electrolyte solution under stirring. The coagulation is not made with multivalent cations. Multivalent cations are to be avoided in the electrolyte solution. No multivalent cations are voluntary added to the electrolyte solution.
Preferably the coagulation is made with a solution comprising an inorganic acid or a salt of an alkali metal. More preferably the inorganic acid is chosen from but not limited to HCl, H 2 S0 4 , H 3 PO 4 . Advantageously a 1 molar aqueous solution of the inorganic acid has a pH≦1.
More preferably the alkali metal salt is a sodium or potassium salt. For example the alkali metal salt can be chosen from NaCl, KCl, Na 2 SO 4 , Na 3 PO 4 Na 2 HPO 4 , but is not limited on this list.
In a first more preferably embodiment the coagulation is made with a solution comprising an inorganic acid. Advantageously the inorganic acid is chosen from but not limited to HCl, H 2 S0 4 , H 3 PO 4 .
In a second more preferably embodiment the coagulation is made with a solution comprising a salt of an alkali metal. Advantageously the alkali metal salt is chosen from NaCl, KCl, Na 2 SO 4 , Na 3 PO 4 Na 2 HPO 4 or mixtures therof.
Adjusting the pH in step d) of the process of the invention is preferably made by adding sodium or potassium hydroxide or aqueous buffer solution after the coagulation step.
The washing in step e) of the process of the invention is made by water, diluted aqueous solutions or aqueous buffer solutions. After the washing step the pH is between 5 and 10. The coagulated multistage polymer after step e) is in form of a wet cake. The wet cake contains less than 60% of water.
Step f) concerns the addition of an aqueous solution or dispersion comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V.
Preferably the step f) concerning the addition of an aqueous solution or dispersion comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V is made after the coagulation step c).
In order to add aqueous solution or dispersion comprising a phosphorous containing compound, said the solution or dispersion is prepared by simple mixing of a known defined quantity of the phosphorous containing compound with water.
In one embodiment the aqueous solution or dispersion comprising the phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V is added by washing the multistage polymer which contains less than 60 wt % of water with said aqueous solution or dispersion comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V.
In a second embodiment the aqueous solution or dispersion comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V is added on the wet cake after coagulation step and filtration step. After the filtration a wet cake is obtained that contains less than 60 wt % of water. Afterwards the wet cake is dried.
In a third embodiment the aqueous solution or dispersion comprising a phosphorous containing compound wherein the phosphorous has the oxidation stage of +III or +V is added during drying step of the multistage polymer, when the multistage polymer composition comprises still at least 10 wt % of water. No further separation between liquid phase that can contain solids or salts and solid phase takes place. All added phosphorous stays with the multistage polymer.
The phosphorous containing compound is preferably chosen from organophosphorous compound, a phosphate salt, phosphoric acid, phosphonate salts, phosphonic acid and their respective esters and mixtures thereof.
Phosphate ester general structure P(═O)(OR) 3 , where at least one group R is an alkyl group. Phosphonates are esters of phosphonic acid and have the general formula RP(═O) (OR′) 2 , where at least one group R or R′ is an alkyl group.
By organophosphorous compound in the present invention are understood compounds with P—C and P—O—C bonds.
More preferably the phosphorous containing compound is chosen from organophosphorous compound having a P—O—C bond, a phosphate salt, phosphoric acid, phosphonate salts, phosphonic acid and ester and mixtures thereof.
Phosphate salts are salts that have as anion dihydrogenophosphate (H 2 PO 4 − ), hydrogenophosphate (HPO 4 2− ) or phosphate (PO 4 3− ).
Phosphonate salts are salts that have as anion dihydrogenophosphonate (H 2 PO 3 − ) or hydrogenophosphate (HPO 3 2− ).
The present invention relates also to the use of the multistage polymer as impact modifier in thermoplastic polymers.
The present invention relates further to a thermoplastic composition comprising the multistage polymer and a thermoplastic polymer.
With regard to the thermoplastic polymer that is part of the thermoplastic composition according to the invention it can be chosen among poly(vinyl chloride) (PVC), chlorinated poly(vinyl chloride) (C-PVC), polyesters as for example poly (ethylene terephtalate) (PET) or poly(butylen terephtalate) (PBT) polyhydroxyalkanoates (PHA) or polylactic acid (PLA), cellulose acetate, polystyrene (PS), polycarbonates (PC), polyethylene, poly (methyl methacrylate)s (PMMA), (meth)acrylic copolymers, thermoplastic poly(methyl methacrylate-co-ethylacrylates), poly(alkylene-terephtalates), poly vinylidene fluoride, poly(vinylidenchloride), polyoxymethylen (POM), semi-crystalline polyamides, amorphous polyamides, semi-crystalline copolyamides, amorphous copolyamides, polyetheramides, polyesteramides, copolymers of styrene and acrylonitrile (SAN), and their respective mixtures or alloys. According to a preferred embodiment the thermoplastic resin composition comprises polycarbonate (PC) and/or polyester (PET or PBT) or PC or polyester alloys. The alloys for example may be PC/ABS (poly(Acrylonitrile-co-butadiene-co-styrene), PC/ASA, PC/polyester or PC/PLA.
Preferably, if the thermoplastic polymer in the thermoplastic polymer composition comprises polycarbonate (PC) and/or polyester (PET or PBT) or PC or polyester alloys the polymer (A) of the multistage polymer is chosen from isoprene homopolymers or butadiene homopolymers, isoprene-butadiene copolymers, copolymers of isoprene with at most 98 wt % of a vinyl monomer and copolymers of butadiene with at most 98 wt % of a vinyl monomer.
Concerning the polycarbonate (PC), it can be aromatic, semi-aromatic and/or aliphatic (particularly based on isosorbide).
With regard to the thermoplastic composition comprising the multistage polymer and a thermoplastic polymer, the proportions between the multistage polymer of the invention and the thermoplastic polymer are between 0.5/99.5 and 50/50, preferably between 1/98 and 30/70, more preferably between 2/98 and 20/80 and advantageously between 2/98 and 15/85.
[Methods of Evaluation]
Glass Transition Temperature
The glass transitions (Tg) of the polymers are measured with equipment able to realize a thermo mechanical analysis. A RDAII “RHEOMETRICS DYNAMIC ANALYSER” proposed by the Rheometrics Company has been used. The thermo mechanical analysis measures precisely the visco-elastics changes of a sample in function of the temperature, the strain or the deformation applied. The apparatus records continuously, the sample deformation, keeping the stain fixed, during a controlled program of temperature variation.
The results are obtained by drawing, in function of the temperature, the elastic modulus (G′), the loss modulus and the tan delta. The Tg is higher temperature value read in the tan delta curve, when the derived of tan delta is equal to zero.
Particle Size Analysis
The particle size of the primary particles after the multistage polymerization is measured with a Zetasizer Nano S90 from MALVERN. The particle size of the polymer powder after coagulation is measured with Malvern Mastersizer 3000 from MALVERN.
For the estimation of weight average powder particle size, particle size distribution and ratio of fine particles a Malvern Mastersizer 3000 apparatus with a 300 mm lenses, measuring a range from 0.5-880 μm is used.
D (v, 0.5) or more short D50 is the particle size at which 50% of the sample has size less then and 50% of the sample have a size larger then that size, or in other words the equivalent volume diameter at 50% cumulative volume. This size is also known as volume median diameter that is related to the mass median diameter by the density of the particles by the density of the particles assuming a size independent density for the particles.
D (v, 0.1) or D10 is the particle size at which 10% of the sample is smaller then that size, or in other words the equivalent volume diameter at 10% cumulative volume.
D (v, 0.9) or D90 is the particle size at which 90% of the sample are smaller then that size.
Analyses of Phosphor Content and Multivalent Cations.
The phosphorous content is measured with Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES). The result is expressed in ppm based on phosphor (P) or the respective multivalent cation (M b+ with b>1) in relation to the multistage polymer. The analysis does not allow to give the structure of the composition containing phosphorus or multivalent cation.
pH Measurement
The pH value of the respective products is measured with Procedure to obtain the pH of the final powder:
5 g of dried powder are dispersed in 20 mL of demineralized water under stirring during 10 minutes at 45° C. Then, the slurry is filtrated on a Wattman filter in paper. The pH of the filtrated water is measured at room temperature.
The pH value is obtained using a Fisher Scientific glass probe connected to a Eutech Instrument pH 200 series pH-meter preliminary calibrated with standard buffer solutions.
EXAMPLES
Example 1
Synthesis of Multistage Polymer (Core-Shell Particles)
First stage—polymerization of core: To a 20 litres high-pressure reactor was charged: de-ionized water 116.5 parts, emulsifier potassium salt of beef tallow fatty acid 0.1 part, 1,3-butadiene 21.9 parts, t-dodecyl mercaptan 0.1 parts, and p-menthane hydroperoxide 0.1 parts as an initial kettle charge. The solution was heated, with agitation, to 43° C. at which time a redox-based catalyst solution was charged (water 4.5 parts, sodium tetrapyrophosphate 0.3 parts, ferrous sulphate 0.004 parts and dextrose 0.3 parts), effectively initiating the polymerization. Then the solution was further heated to 56° C. and held at this temperature for a period of three hours. Three hours after polymerization initiation, a second monomer charge (77.8 parts BD, t-dodecyl mercaptan 0.2 parts), one-half of an additional emulsifier and reductant charge (de-ionized water 30.4 parts, emulsifier potassium salt of beef tallow fatty acid 2.8 parts, dextrose 0.5 parts) and additional initiator (p-menthane hydroperoxide 0.8 parts) were continuously added over eight hours. Following the completion of the second monomer addition, the remaining emulsifier and reductant charge plus initiator was continuously added over an additional five hours. Thirteen hours after polymerization initiation, the solution was heated to 68° C. and allowed to react until at least twenty hours had elapsed since polymerization initiation, producing polybutadiene rubber latex, R1. The resultant polybutadiene rubber latex (R1) contained 38% solids and had a weight average particle size of about 160 nm.
Second stage—Polymerization of shell 1 (outer shell): into a 3.9 litres reactor was charged 75.0 parts, on a solids basis, of polybutadiene rubber latex R1, 37.6 parts de-ionized water, and 0.1 parts sodium formaldehyde sulfoxylate. The solution was agitated, purged with nitrogen, and heated to 77° C. When the solution reached 77° C., a mixture of 22.6 parts methyl methacrylate, 1.4 parts divinyl benzene and 0.1 parts t-butyl hydroperoxide initiator was continuously added over 70 minutes, followed by o hold period of 80 minutes. Thirty minutes after the onset of the hold period, 0.1 parts of sodium formaldehyde sulfoxylate and 0.1 parts t-butyl hydroperoxide were added to the reactor at once. Following the 80-minute hold period, a stabilization emulsion was added to the graft copolymer latex. The stabilization emulsion was prepared by mixing 3.2 parts de-ionized water (based on graft copolymer mass), 0.1 parts oleic acid, 0.1 parts potassium hydroxyde, and 0.9 parts octadecyl-3-(3,5-di-tertbutyl-4-hydroxyphenyl)propionate. The resultant core shell latex (G1) had a weight average particle size of about 180 nm.
Coagulation: In a jacketed vessel of 3 L, equipped with a stirrer is put successively 500 g of latex of core-shell particles (G1) for having a solid content of 14.1%. Under stirring at 300 r/min, the heat of the solution is raised at 52° C. and then injected a 1.6% aqueous sulphuric acid solution resulting in a coagulated material that was heat treated at 96° C. The pH was adjusted with NaOH during the coagulation between 2 and 6. Subsequently, the coagulated material was filtered on centrifuge and washed with de-ionized water. Then, the pH is measured and adjusted with aqueous solution of sodium hydroxide for being between 5 and 9. The resultant polymer (P1) had a neutral pH (6<pH<7) and an average particle size of about 141 μm.
Addition of phosphate buffer solution: in a 2 litres calibrated flask is put 750 g of graft copolymer P1 (solid content 60 wt %) and is added 99 mL of a aqueous solution of Na 2 HPO 4 (disodium hydrogen phosphate) and KH 2 PO 4 (potassium dihydrogen phosphate) comprising expressed in phosphorous a concentration of 2.97 mg/ml.
Drying. The final powder PP1 (P1+phosphate) is put in a ventilated oven during 48 h at 50° C. and recovered after complete drying, humidity<1 wt %.
Example 2
The synthesis of multistage polymer (core-shell particles) is the same as in example 1.
Coagulation without pH adjusting after the coagulation: in a jacketed vessel of 3 L, equipped with a stirrer is put successively 500 g of latex of core-shell particles (G1) for having a solid content of 14.1%. Under stirring at 300 r/min, the heat of the solution is raised at 52° C. and then injected a 1.6% aqueous sulfuric acid solution resulting in a coagulated material that was heat treated at 96° C. The pH was adjusted during the coagulation between 2 and 6. Subsequently, the coagulated material was filtered on centrifuge and washed with de-ionized water to give P2.
Addition of phosphate buffer solution: in a 2 litres calibrated flask is put 750 g of graft copolymer (solid content 60 wt %), P2 and are added 99 mL of a aqueous solution of Na 2 HPO 4 (disodium hydrogeno phosphate) and KH 2 PO 4 (potassium dihydrogen phosphate) comprising expressed in phosphorous a concentration of 2.97 mg/ml.
Drying. The final powder PP2 is put in a ventilated oven during 48 h at 50° C. and recovered after complete drying.
Example 3 ((Comparative))
The synthesis of multistage polymer (core-shell particles) is the same as in example 1.
Coagulation: in a jacketed vessel of 3 L, equipped with a stirrer is put successively 500 g of latex of core-shell particles (G1) from example 1 for having a solid content of 14.1%. Under stirring at 300 r/min, the heat of the solution is raised at 52° C. and then injected a 1.6% aqueous sulphuric acid solution resulting in a coagulated material that was heat treated at 96° C. The pH was adjusted during the coagulation between 2 and 6. Subsequently, the coagulated material was filtered on centrifuge and washed with de-ionized water. Then, the pH is measured and adjusted with aqueous solution of sodium hydroxide for being between 5 and 9. The resultant polymer (P1) had a neutral pH (5<ph<8) and an average particle size of about 141 μm (method, meme taille que example 1!)
Addition of phosphate buffer solution: in a 2 litres calibrated flask is put 750 g of graft copolymer P1 (solid content 60 wt %) and are added 46 mL of an aqueous solution of Na 2 HPO 4 (disodium hydrogeno phosphate) and KH 2 PO 4 (potassium dihydrogen phosphate) comprising expressed in phosphorous a concentration of 2.97 mg/ml.
Drying: the final powder PP3 is put in a ventilated oven during 48 h at 50° C. and recovered after complete drying
Example 4 (Comparative)
The synthesis of multistage polymer (core-shell particles) is the same as in example 1.
Coagulation: in a jacketed vessel of 3 L, equipped with a stirrer is put successively 500 g of latex of core-shell particles (G1) from example 1 for having a solid content of 14.1%. Under stirring at 300 r/min, the heat of the solution is raised at 52° C. and then injected a 1.6% aqueous sulfuric acid solution resulting in a coagulated material that was heat treated at 96° C. The pH was adjusted during the coagulation between 2 and 6. Subsequently, the coagulated material was filtered on centrifuge and washed with de-ionized water. Then, the pH is measured and adjusted with aqueous solution of sodium hydroxide for being between 5 and 9. The resultant polymer (P1) had a neutral pH (6<ph<7) and a weight average particle size of about 141 μm.
Addition of phosphate buffer solution: in a 2 litres calibrated flask is put 750 g of graft copolymer P1 (solid content 60 wt %) and are added 15 mL of an aqueous solution of Na 2 HPO 4 (disodium hydrogeno phosphate) and KH 2 PO 4 (potassium dihydrogen phosphate) comprising expressed in phosphorous a concentration of 2.97 mg/ml.
Drying: the final powder PP4 is put in a ventilated oven during 48 h at 50° C. and recovered after complete drying.
Example 5 (Comparative)
The synthesis of multistage polymer (core-shell particles) is the same as in example 1.
Coagulation: in a jacketed vessel of 3 L, equipped with a stirrer is put successively 500 g of latex of core-shell particles (G1) from example 1 for having a solid content of 14.1%. Under stirring at 300 r/min, the heat of the solution is raised at 52° C. and then injected a 1.6% aqueous sulphuric acid solution resulting in a coagulated material that was heat treated at 96° C. The pH was adjusted during the coagulation between 2 and 6. Subsequently, the coagulated material was filtered on centrifuge and washed with warm de-ionized water. Then, the pH is measured and adjusted with aqueous solution of sodium hydroxide for being between 5 and 9. The resultant polymer (P1) had a neutral pH (6<ph<7) and an average particle size of about 141 μm.
No addition of phosphate buffer solution.
Drying: the final powder P5 is put in a ventilated oven during 48 h at 50° C. and recovered after complete drying.
The phosphor content of all powders is estimated with Inductively Coupled Plasma-Atomic Emission Spectroscopy (ICP-AES). The results are summarized in table 1.
TABLE 1
Summery of the powder characteristics
Coagulation
Agent
P/[ppm]
Example 1
Sulphuric acid
650
Example 2
Sulphuric acid
650
Example 3
Sulphuric acid
300
Example 4
Sulphuric acid
100
Example 5
Sulphuric acid
80
Table 1 indicates that the phosphor content decreases with the examples 3 and 4, as lesser quantity of the phosphate buffer solution is added to the polymer powder after coagulation. In example 5 the phosphor content is the lowest as no phosphate buffer solution is added to the polymer powder after coagulation. The phosphorous in example 5 is due to the products used during the synthesis of the multistage polymer.
The dry multistage polymer powders P1 to P5 are compounded with polycarbonate at 5 wt % for producing compounds 1 to 5.
Preparation of the impact modified compound compositions, the respective impact modifier powders P1 to P6 are mixed with the thermoplastic resin polycarbonate Lexan ML5221 from SABIC (at 5 wt % with the help of an extruder type Clextral (double diameter 25 mm, length 700 mm) using temperatures between from 100° C. up to 320° C. depending on the respective zones throughout the whole extruder.
The respective obtained compounds are heat aged at 120° C. The optical properties of the compounds are evaluated. The color change is observed by measuring the parameter b*. The b* value is used to characterize the principal yellowing off the samples. The b* value measures the blue and the yellow of the colour. Colours tending toward the yellow have a positive b* value while those tending toward the blue have a negative b* value. The b* values is measured using a colorimeter (especially according to the ASTM E 308 standard). The colour change is observed as a function of time: samples kept at 120° C. for 4 days.
If the initial color is close to zero it is considered that the thermoplastic composition comprising the impact modifiers of the invention is acceptable. The b* value should not larger than 10 after 4 days of thermal aging.
TABLE 2
color of heat aged compounds
Multistage polymer
b*
b*
from
initial
after 4 days at 120° C.
Compound 1
Example 1
0.43
4.02
Compound 2
Example 2
−1.55
5.47
Compound 3
Example 3
0.73
13.77
Compound 4
Example 4
−2.45
15.34
Compound 5
Example 5
−0.84
20.74
TABLE 3
impact strength of thermoplastic compositions
Multistage
IZOD impact strength
IZOD impact
polymer
[kJ/m2]
strength [kJ/m2]
from
at 23° C.
at −30° C
Compound 1
Example 1
48.0
37.0
Compound 2
Example 3
—
—
Compound 3
Example 4
45.4
35.6
Compound 4
Example 5
—
—
Compound 5
Example 6
45.9
41.0
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