Polymeric dispersants for polymerization production of water-in-water dispersions in presence of amines
By preparing water-soluble polymer dispersants in the presence of chain transfer agent amines, the preparation method of water-in-water polymer dispersions was optimized, solving the problems of stability and long-term stability, and meeting the requirements of efficient flocculation and dewatering in the papermaking process.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- SOLENIS TECHNOLOGIES CAYMAN LP
- Filing Date
- 2024-07-26
- Publication Date
- 2026-04-21
AI Technical Summary
In the existing technology, the stability and long-term stability of water-in-water polymer dispersions are insufficient, especially in environments with alternating temperature changes, and the preparation process is not stable enough to meet the requirements of efficient papermaking processes.
A water-soluble polymer dispersant was prepared by polymerizing monomer compositions in the presence of a chain transfer agent amine, and a water-in-water polymer dispersion was formed in an aqueous medium by free radical polymerization. The copolymerization reaction conditions were optimized using a chain transfer agent containing amine, such as quaternized trimethylammonium-propylacrylamide.
It improves the stability and long shelf life of water-in-water dispersions, ensuring good performance in the papermaking process, adapting to temperature changes, and providing efficient flocculation and dewatering properties.
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Abstract
Description
[0001] This invention relates to polymer dispersants for preparing water-in-water dispersions, methods for preparing water-in-water dispersions, and polymer dispersants and their uses.
[0002] The primary objective is to unlock the potential of water and renewable resources to build a safer, healthier, and more sustainable world. Countless industrial processes are water-based. Replacing or reducing the use of environmentally harmful substances in water-based processes is fundamental to achieving more sustainable solutions. This invention aims to achieve this primary objective in the field of water-in-water polymer dispersions (w / w polymer dispersions). Improvements in water-in-water polymer dispersions are directly related to the sustainability of downstream applications, such as papermaking processes. The better such water-in-water polymer dispersions perform as additives in water-based processes (such as papermaking), the less additive is needed in these processes. Furthermore, the substitution of hydrocarbons also supports this primary objective.
[0003] Typically, in addition to applications in other technical fields, water-in-water polymer dispersions are used as flocculants, dewatering (filtration) aids, and retention aids in papermaking. Papermaking begins with the preparation of an aqueous pulp of cellulose fibers with a water content greater than 95% by weight. The final paper has a water content of less than 5% by weight. Dewatering (filtration) and retention are key steps in papermaking and are essential for an efficient papermaking process. High-performance water-in-water polymer dispersions are a critical factor in the papermaking process.
[0004] Existing polymer dispersions are typically stabilized using low molecular weight salts. An alternative is the use of water-in-water polymer dispersions, prepared by copolymerizing an olefinic unsaturated monomer in an aqueous system containing a polymer dispersant, resulting in a dispersion comprising the polymer dispersant and a synthesized copolymer. US8476391B2 and US7323510B2 are early publications of this type of water-in-water polymer dispersion. It is known in the art that products obtained by mixing separately synthesized copolymers and polymer dispersants have entirely different properties compared to the water-in-water polymer dispersions disclosed in the aforementioned patent documents. To obtain, for example, high-performance flocculant products for use in papermaking processes, copolymerization is required within a system containing a polymer dispersant.
[0005] These factors make the preparation of water-in-water polymer dispersions a multi-parameter system. The types of olefinic unsaturated monomers, their proportions, and the molecular weight of the polymer dispersant are only a small subset of parameters affecting the properties of water-in-water polymer dispersions. Improving the performance of the final product from water-in-water polymer dispersions has been the subject of countless research and development attempts.
[0006] One of the parameters that plays a decisive role in beneficially influencing the properties of water-in-water dispersions is the polymeric dispersant, which is a polymer other than the copolymer polymerized in the water-in-water dispersion in the presence of the polymeric dispersant.
[0007] There remains a need for improved polymer dispersants that can have beneficial effects on complex polymer systems and offer the potential to improve their properties. For example, there is still a need to improve long-term stability and ensure longer storage periods under adverse conditions such as alternating temperature changes.
[0008] The fundamental problem of this invention relates to overcoming the shortcomings of the prior art. In particular, the fundamental problem of this invention relates to providing a polymer dispersant that imparts beneficial properties to water-in-water dispersions, especially regarding the stability, long-term stability, and workability of the water-in-water dispersions, particularly concerning the viscosity of the water-in-water dispersions. Furthermore, the fundamental problem of this invention relates to providing a method for preparing water-in-water polymer dispersions that yields a product that ensures improved performance during use (especially in papermaking processes). Additionally, the fundamental problem of this invention relates to providing a method for preparing water-in-water polymer dispersions that ensures high stability during preparation and a long shelf life under adverse environments (such as alternating temperature changes).
[0009] The fundamental problem of the present invention is solved by the subject matter of claim 1. Therefore, according to a first aspect, the present invention relates to a polymeric dispersant for preparing water-in-water dispersions, said polymeric dispersant being water-soluble and prepared by polymerizing a monomeric composition in the presence of a chain transfer agent, said monomeric composition comprising at least the following monomers: (a1) ,in, R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6 alkyl group; and Z - It is a counter ion; (a2) Optional (meth)acrylic acid and / or (meth)acrylamide, The chain transfer agent is characterized in that it comprises an amine.
[0010] Therefore, the polymer dispersant is prepared by polymerizing a monomer composition containing acrylates or acrylamide in the presence of an amine as a chain transfer agent. After preparing the polymer dispersant, a method for preparing a water-in-water polymer dispersion includes the following steps: providing a reaction mixture in an aqueous medium, the reaction mixture containing the polymer dispersant and a monomer composition containing a free-radical polymerizable monomer; and subjecting the monomer composition in the reaction mixture to free-radical polymerization to synthesize a dispersed polymer, thereby forming a polymer dispersion. These polymer dispersions are referred to as water-in-water (w / w) polymer dispersions.
[0011] The term "chain transfer agent" is well known to those skilled in the art (e.g., polymer chemists). Chain transfer agents typically affect chain growth in polymerization. Chain transfer agents can terminate chain growth in polymerization. In doing so, the chain transfer agent may chemically bond to the polymer. Furthermore, the use of chain transfer agents can affect molecular weight, allowing the polymer's molecular weight to be maintained at a desired low level.
[0012] In this application, the chain transfer agent comprises an amine. Amines have been found to be readily available chain transfer agents that can improve the properties of the final product (i.e., the water-in-water dispersion). Without being bound by theory, chain transfer agents may cause the termination of growing polymer chains.
[0013] The term "polymer dispersant made by polymerizing a monomer composition in the presence of a chain transfer agent" refers to a polymer dispersant composed of monomers derived from a monomer composition, or monomers derived from a monomer composition and constituents of a chain transfer agent. Polymerization causes these constituents to combine to form a polymer.
[0014] The monomer composition must contain the monomer of item a1 above. Preferably, the monomer of item a1 above is a cationic monomer, more preferably selected from: (alkyl)acrylamidoalkyltrialkylammonium halides (e.g., trimethylammonium-alkyl(meth)acrylamide halides), (alkyl)acryloyloxyalkyltrialkylammonium halides (e.g., trimethylammonium alkyl(meth)acrylate halides), alkenyltrialkylammonium halides, and diallyldialkylammonium halides (e.g., diallyldialkylammonium halides). More preferably, the polymer dispersant is a cationic polymer derived from a monomer composition containing a cationic monomer selected from: trimethylammonium-alkyl(meth)acrylate halides, trimethylammonium alkyl(meth)acrylamide halides, and diallyldialkylammonium halides. Preferably, the aforementioned cationic monomer contains 6 to 25 carbon atoms, more preferably 7 to 20 carbon atoms, most preferably 7 to 15 carbon atoms, and particularly 8 to 12 carbon atoms.
[0015] In a highly preferred embodiment, the polymer dispersant is a polymer comprising quaternized trimethylammonium-propylacrylamide (DIMAPA quaternary ammonium salt).
[0016] According to the present invention, quaternization can be carried out using dimethyl sulfate, diethyl sulfate, chloromethane, or chloroethane. In a preferred embodiment, the monomer is quaternized using chloromethane.
[0017] Optionally, the monomer composition may contain (meth)acrylic acid and / or (meth)acrylamide (a2). In this case, the resulting polymeric dispersant is a copolymer containing monomer a1 and (meth)acrylic acid and / or amide. The amount of (meth)acrylic acid and / or (meth)acrylamide is preferably less than 5% by weight, more preferably between 0.001% and 2% by weight, and most preferably between 0.01% and 1% by weight.
[0018] According to a preferred embodiment, the monomer composition further comprises (a3) a divalent olefinically unsaturated monomer. The divalent olefinically unsaturated monomer used according to this preferred embodiment is preferably a (meth)acrylate containing an allyl functional group, preferably wherein said divalent olefinically unsaturated monomer is N-allylacrylamide. According to an alternative, the divalent olefinically unsaturated monomer used according to the invention is preferably a (meth)acrylamide ester containing an allyl functional group, preferably wherein said divalent olefinically unsaturated monomer is N-allylacrylamide. The divalent olefinically unsaturated monomer may cause branching of the polymer dispersant.
[0019] Unbound by theory, the use of divalent olefinic unsaturated monomers with amines as chain transfer agents results in a more compact polymer dispersant structure, despite its lower molecular weight.
[0020] According to a preferred embodiment, the amount of the divalent olefinic unsaturated monomer is from 0.0001% to 1.25% by weight, preferably from 0.001% to 0.5% by weight, and more preferably from 0.005% to 0.05% by weight, based on the total weight of the monomer composition.
[0021] In a preferred embodiment, the chain transfer agent is a mixture of an amine and a thiol. Thiols are well known as chain transfer agents. According to this preferred embodiment, it is a mixture that acts as a chain transfer agent. As for the thiol, any alkyl thiol can be used. The most preferred is mercaptoethanol.
[0022] According to a preferred embodiment, the amine comprises two or more amine functional groups.
[0023] According to a preferred embodiment, the amine comprises two or more, preferably two or three tertiary amine functional groups.
[0024] According to a particularly preferred embodiment, the amine is represented by N-[3-(dimethylamino)propyl]-3-{[3-(dimethylamino)propyl]amino}acrylamide (CAS No. 86551-24-8), N-[3-(dimethylamino)propyl]-3-{[3-(dimethylamino)propyl](2-{[3-(dimethylamino)propyl]carbamoyl}ethyl)amino}acrylamide, or a mixture thereof.
[0025] Regarding the amine content, beneficial properties can be observed if the amount of amine present, based on the total weight of the monomer composition, is 0.1 to 10% by weight, preferably 0.5 to 8% by weight, more preferably 1 to 5% by weight. According to a preferred embodiment, the amine is selected from N-[3-(dimethylamino)propyl]-3-{[3-(dimethylamino)propyl]amino}acrylamide, N-[3-(dimethylamino)propyl]-3-{[3-(dimethylamino)propyl](2-{[3-(dimethylamino)propyl]carbamoyl}ethyl)amino}acrylamide, and mixtures thereof, wherein the amount of amine present, based on the total weight of the monomer composition, is 0.1 to 10% by weight, preferably 0.5 to 8% by weight, more preferably 1 to 5% by weight.
[0026] The aforementioned characteristics of divalent olefinic unsaturated monomers and chain transfer agents endow polymer dispersants with beneficial properties, thereby imparting beneficial properties to water-in-water dispersions.
[0027] The polymerization reaction for preparing the polymer dispersant according to the present invention preferably yields a polymer dispersant with the following weight-average molecular weight Mw (determined by size exclusion chromatography): 40,000 to less than 150,000 g / mol, preferably 50,000 to 140,000 g / mol, more preferably 60,000 to 130,000 g / mol, and most preferably 85,000 to 125,000 g / mol.
[0028] According to a preferred embodiment, the polymer dispersant is a cationic polymer dispersant. Particularly preferred is that the polymer dispersant is water-soluble and is prepared by polymerizing a monomer composition comprising at least one monomer of item a1 above, wherein Z1 is O, NH, or NR4, preferably NH or NR4, and wherein R4 represents methyl. Y is
[0029] Y1 is ethylene or propylene, optionally substituted with a hydroxyl group; Y5, Y6, and Y7 are each methyl groups; and Z - It is selected from halogens, halogen-like substances, acetate, and SO4CH3. - Counterions.
[0030] The fundamental problem of the present invention is also solved by the subject matter of claim 9. Therefore, according to a second aspect, the present invention relates to a method for preparing a water-in-water polymer dispersion, the method comprising subjecting an aqueous reaction mixture to a free radical polymerization reaction, said aqueous reaction mixture comprising: (a) The polymer dispersant according to the invention, and (b) A composition comprising one or more of the following monomers: i. Nonionic monomers of formula (I) ,in R 1 Indicates hydrogen or methyl; R 2 and R 3 Each of them is independently hydrogen, C1-C5-alkyl, or C1-C5-hydroxyalkyl. ii. Cationic monomers of formula (II) ,in R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups, preferably ethylene or propylene, optionally substituted with one hydroxyl group; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6-alkyl group, preferably methyl; and Z - It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ;and iii. Amphiphilic monomers of formula (III) or (IV) ,in Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl. R 1 Indicates hydrogen or methyl. R8 is a C1-C6 alkylene group, preferably ethylene or propylene. R5 and R6 are each independently C1-C6-alkyl, preferably methyl. R7 is C8-C 32 Alkyl groups, optionally substituted with one or more hydroxyl groups, preferably C10. 12 -C 20Alkyl group, optionally substituted with a hydroxyl group, and Z - It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ;or ,in Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl. R 1 Indicates hydrogen or methyl. R 10 Indicates hydrogen, C8-C 32 Alkyl, C8-C 32 Aryl and / or C8-C 32 Aryl alkyl group, preferably C 12 -C 20 alkyl, R9 is a C1-C6 alkylene group, preferably ethylene or propylene. n is an integer from 1 to 50, preferably from 2 to 30, more preferably from 3 to 15, and most preferably from 4 to 8; and iv. An olefinically unsaturated crosslinking agent containing 2, 3, 4 or 5 olefinically unsaturated groups.
[0031] The method includes providing a reaction mixture comprising a monomer to be copolymerized and a polymeric dispersant according to the first aspect. The monomer is polymerized in an aqueous medium in the presence of the polymeric dispersant. It should be noted that the term "monomer composition" is different from the term "monomer group". "Monomer composition" is used to obtain a polymeric dispersant, while "monomer group" produces a copolymer present in a water-in-water dispersion. According to known technical knowledge, it is impossible to obtain the polymeric dispersion obtained by the method of the second aspect of the invention by copolymerizing the monomer composition and then adding the polymeric dispersant after the copolymerization reaction. By applying the method of the invention, the polymeric dispersion is endowed with unique properties, representing a final product comprising a copolymer obtained from a free radical polymerizable monomer and a polymeric dispersant.
[0032] It has been found that using polymer dispersants made from amines as chain transfer agents to prepare polymer dispersions produces water-in-water dispersions with beneficial effects. On the one hand, it is speculated that amines have an effect on polymer dispersants. On the other hand, amines are still present during the copolymerization of the monomer composition. The presence of amines has a positive effect on the copolymerization process. Therefore, it is preferable that the step of subjecting the aqueous reaction mixture to free radical polymerization is carried out with the polymer dispersant according to the invention (i.e., using the polymer dispersant directly). This means that the polymer dispersant is first prepared, and then the resulting polymer dispersant is used in the step of copolymerizing the monomer composition. Subsequently, the amine plays a role in the copolymerization reaction. Results show that the water-in-water polymer dispersions thus prepared perform well in the papermaking process.
[0033] According to a preferred embodiment, one or more monomers given in items i. to iv. above are used as monomers in the monomer composition to be polymerized. Preferably, a copolymer is used, i.e., the monomer composition to be polymerized provides two monomers given in items i. to iv. above. Preferably, the monomer composition undergoing the copolymerization reaction provides a monomer of item i. and a monomer of item ii. In a preferred embodiment, the radical-polymerizable monomer comprises a radical-polymerizable nonionic monomer according to general formula (I); and a radical-polymerizable cationic monomer according to general formula (II). These copolymerized monomers are advantageous for solving the aforementioned problems.
[0034] Furthermore, the monomer composition for copolymerization preferably provides a monomer of item i, a monomer of item ii, and a monomer of item iv.
[0035] In a preferred embodiment, the method is characterized in that the monomer composition comprising a free radical polymerizable monomer comprises at least a nonionic monomer selected from formula (I) of the following: wherein R 1 R represents hydrogen or methyl. 2 and R 3 All are hydrogen, hydrogen and C1-C3 alkyl, hydrogen and hydroxyethyl, or all are C 1- C3 alkyl, and / or selected from the following formula (II) cationic monomers: wherein R 1 Z1 represents hydrogen or methyl, where R4 represents methyl, Y1 is a C2-C6 alkylene group, preferably ethylene or propylene, Y5, Y6, and Y7 are all methyl, and Z... - It is halogen.
[0036] In a preferred embodiment, the radical-polymerizable monomer comprises a radical-polymerizable nonionic monomer according to general formula (I), selected from: (meth)acrylamide, N-methyl(meth)acrylamide, N,N'-dimethyl(meth)acrylamide, N-ethyl(meth)acrylamide, N,N'-diethyl(meth)acrylamide, N-methyl-N-ethyl(meth)acrylamide, N-isopropyl(meth)acrylamide, and N-hydroxyethyl(meth)acrylamide.
[0037] In another preferred embodiment, the radical-polymerizable monomer comprises a radical-polymerizable cationic monomer according to general formula (II), selected from: trimethylammonium-C2-C6-alkyl (meth)acrylate halides and trimethylammonium-C2-C6-alkyl (meth)acrylamide halides. In a most preferred embodiment, the monomer composition comprises (meth)acrylamide as a radical-polymerizable monomer and a radical-polymerizable monomer selected from trimethylammonium-C2-C6-alkyl (meth)acrylate halides, particularly acryloyloxyethyltrimethylammonium halides.
[0038] Within the framework of this invention, a cationic monomer is a monomer that is permanently positively charged.
[0039] Within the framework of this application, the terms "halogen" or "halogen" can be any acceptable halogen or halide, such as chloride, bromide, or iodide; the counter ion of the salt can be any acceptable counter ion, such as halide ion, methylsulfate, sulfate, or others.
[0040] According to one embodiment, the monomer composition comprising a free radical polymerizable monomer includes a crosslinking agent. Crosslinking agents are known to those skilled in the art. In this preferred embodiment, the monomer composition preferably contains 0.0001 to 1.25% by weight of one or more preferred olefin unsaturated crosslinking agents based on the total weight of the monomers. If olefin unsaturated crosslinking agents are present, they contain 2, 3, 4, or 5 free radical polymerizable olefin unsaturated groups.
[0041] Examples of crosslinking agents having two free radical polymerizable olefinic unsaturated groups include: (1) Alkenyl di(meth)acrylates, such as 1,6-hexanediol di(meth)acrylate, 1,10-decanediol di(meth)acrylate, 1,12-dodecanediol di(meth)acrylate, 1,18-octadecanediol di(meth)acrylate, neopentyl glycol di(meth)acrylate, methylene di(meth)acrylate, 2,2'-bis(hydroxymethyl)-1,3-propanediol di(meth)acrylate, and preferably, ethylene glycol di(meth)acrylate, 1,3-propanediol di(meth)acrylate, 1,3-butanediol di(meth)acrylate and 1,4-butanediol di(meth)acrylate; (2) Alkylene di(meth)acrylamide, such as N-methylene di(meth)acrylamide, N,N'-3-methyl-butylene bis(meth)acrylamide, N,N'-(1,2-dihydroxyethylene)bis(meth)acrylamide, and preferably, N,N'-hexamethylene bis(meth)acrylamide, and particularly preferably, N,N'-methylene bis(meth)acrylamide; (3) Polyalkoxydi(meth)acrylates according to general formula (V) (V), in, R 10 It is hydrogen or methyl; R 11 Selected from -CH2CH2-, -CH2CH2CH2-, -CH2CH2CH2CH2-, -CH2CH2CH2CH2CH2- or -CH2CH2CH2CH2CH2CH2-; and m is an integer in the range of 2-50.
[0042] Examples of crosslinking agents according to general formula (V) include polypropylene glycol di(meth)acrylate with m ranging from 4 to 25; polybutylene glycol di(meth)acrylate with m ranging from 5 to 40; and preferably, polyethylene glycol di(meth)acrylate with m ranging from 2 to 45, such as diethylene glycol di(meth)acrylate, triethylene glycol di(meth)acrylate, tetraethylene glycol di(meth)acrylate; and more preferably, polyethylene glycol di(meth)acrylate with m ranging from 5 to 20. (4) Other examples of di(meth)acrylates that may be used include benzyl di(meth)acrylate, bisphenol A di(meth)acrylate, 1,3-di(meth)acryloyloxy-2-propanol, hydroquinone di(meth)acrylate, ethylene dithiol di(meth)acrylate, propylene dithiol di(meth)acrylate, polyethylene dithiol di(meth)acrylate and polypropylene dithiol di(meth)acrylate; (5) Divinyl compounds, such as 1,4-butanediol divinyl ether, divinylbenzene, butadiene, 1,6-hexadiene; di(meth)allyl compounds, such as di(meth)allyl phthalate or di(meth)allyl succinate; vinyl(meth)acrylic acid compounds, such as vinyl(meth)acrylate; or preferably (meth)allyl(meth)acrylic acid compounds, such as allyl(meth)acrylate.
[0043] Examples of crosslinking agents having three or more olefinically unsaturated free radical polymerizable groups include glycerol tri(meth)acrylate, 2,2-dimethylol-1-butanol tri(meth)acrylate, trimethylolpropane triethoxytri(meth)acrylate, trimethacrylamide, (meth)allylide di(meth)acrylate, 3-allyloxy-1,2-propanediol di(meth)acrylate, triallylamine, triallyl cyanurate, or triallyl isocyanurate; and also (as representative compounds having more than three olefinically unsaturated free radical polymerizable groups) pentaerythritol tetra(meth)acrylate and N,N,N',N'-tetra(meth)acryloyl-1,5-pentanediamine.
[0044] An example of a crosslinking agent having five olefinically unsaturated free radical polymerizable groups is dipentaerythritol pentaacrylate.
[0045] The preferred crosslinking agent is selected from methylenebisacrylamide, polyethylene glycol diacrylate and triallylamine.
[0046] Further preferred crosslinking agents include asymmetric crosslinkable monomers, i.e., crosslinkable monomers that rely on different functional groups for main chain introduction and crosslinking reactions. Examples of such asymmetric crosslinkable monomers include N'-hydroxymethylacrylamide, N'-hydroxymethylmethacrylamide, and glycidyl (meth)acrylate.
[0047] The advantage of this type of crosslinking agent is that it can subsequently initiate crosslinking. Therefore, crosslinking can occur under conditions different from those of main-chain free radical polymerization. Preferably, crosslinking is initiated after changing the reaction conditions, such as pH (addition of acid or alkali), temperature, etc. Optionally, the monomer composition also comprises a hydrophobic monomer, preferably a hydrophobic (meth)acrylic acid C4- 18 -alkyl esters; and / or olefinic unsaturated monomers.
[0048] In a preferred embodiment, the method is characterized in that the free radical polymerizable monomer is selected from nonionic monomers of formula (I) and / or cationic monomers of formula (II), wherein, based on the total amount of free radical polymerizable monomers, the amount of free radical polymerizable monomers selected from nonionic monomers of formula (I) and / or cationic monomers of formula (II) is 80 to less than 100 wt%, preferably 85 to 99 wt%, most preferably 90 to 95 wt%, and the balance is selected from any other olefin polymerizable monomers, monomers of formula (III), monomers of formula (IV), and olefin unsaturated crosslinking agents containing 2, 3, 4, or 5 olefin unsaturated groups.
[0049] In this regard, the sum of the values expressed as % by weight need not reach 100% by weight, because in addition to the monomers of formula (I) and / or (II), the monomer composition (i.e., the reaction mixture) may contain other olefinically unsaturated monomers, which must be taken into account when determining the total amount of monomers. However, in a preferred embodiment, the monomer composition consists of (a) and (b), so the sum of the two % by weight values is 100% by weight, meaning that no other monomers are present.
[0050] In a preferred embodiment, the monomer composition comprises: - At least 5% by weight, preferably at least 20% by weight, of the nonionic monomer of formula (I). ,in R 1 Indicates hydrogen or methyl; R 2 and R 3 Each of them is independently hydrogen, C1-C5-alkyl, or C1-C5-hydroxyalkyl; At least 5% by weight, preferably at least 20% by weight, more preferably 25 to 47% by weight, and most preferably 50.5 to 80% by weight of the cationic monomer of formula (II). ,in R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups, preferably ethylene or propylene, optionally substituted with one hydroxyl group; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6-alkyl group, preferably methyl; and Z -It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ; - 0.0001 to 1.25% by weight, preferably 0.0005 to 1% by weight, of an olefinically unsaturated crosslinking agent containing 2, 3, 4, or 5 olefinically unsaturated groups; and - Optional other olefinic unsaturated monomers.
[0051] To reiterate in this regard, the sum of the values expressed as % by weight need not reach 100% by weight, because in addition to the monomers of formula (I) and / or (II), the monomer composition (i.e., the reaction mixture) may contain other olefinically unsaturated monomers, which must be taken into account when determining the total amount of monomers. However, in a preferred embodiment, the monomer composition consists of (a) and (b), so the sum of the two % by weight values is 100% by weight, meaning that no other monomers are present.
[0052] In this application, all percentages relating to monomer compositions are based on the total amount of monomers used in the copolymerization reaction. Percentages relating to monomer compositions are based on the total amount of monomers used to prepare the polymer dispersant.
[0053] In a preferred embodiment, the method is characterized in that the viscosity of the polymer dispersion is from 1,800 mPa·s to less than 6,700 mPa·s, preferably from 2,000 mPa·s to 6,000 mPa·s, more preferably from 2,200 mPa·s to 5,500 mPa·s, and most preferably from 2,500 mPa·s to 5,000 mPa·s, measured using a Brookfield viscometer with a No. 4 rotor at 20°C and an angular velocity of 10 rpm.
[0054] The viscosity is preferably the bulk viscosity, which refers to the viscosity of the product immediately after it has cooled.
[0055] According to a preferred embodiment, the ratio of polymer dispersant to dispersing polymer in the polymer dispersion is in the range of 0.45:1 to 1:0.9, preferably in the range of 0.5:1 to 1:1, more preferably in the range of 0.55:1 to less than 1:1, even more preferably in the range of 0.6:1 to 0.99:1, and particularly in the range of 0.65:1 to 0.9:1.
[0056] The invention is particularly effective if the method is characterized in that, based on the total weight of the polymer dispersion, the total weight of the polymer dispersant is in the range of 10 to 28 wt%, preferably 12 to 26 wt%, more preferably 14 to 24 wt%, and even more preferably 16 to 22 wt%. According to another embodiment, the method is characterized in that, based on the total weight of the polymer dispersion, the total weight of the polymer dispersant is between 18 and 26 wt%, preferably 19 to 25 wt%.
[0057] According to another preferred embodiment, the method is characterized in that the monomer composition does not contain any hydrophobic monomers.
[0058] The fundamental problem of the present invention is also solved by the subject matter of claim 13. Therefore, according to a third aspect, the present invention relates to a water-in-water polymer dispersion comprising: (a) A polymer dispersant according to a second aspect of the invention, and (b) A copolymer derived from a monomer composition comprising one or more of the following: i. Nonionic monomers of formula (I) ,in R 1 Indicates hydrogen or methyl; R 2 and R 3 Each of them is independently hydrogen, C1-C5-alkyl, or C1-C5-hydroxyalkyl. ii. Cationic monomers of formula (II) ,in R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups, preferably ethylene or propylene, optionally substituted with one hydroxyl group; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6-alkyl group, preferably methyl; and Z - It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ;and iii. Amphiphilic monomers of formula (III) or (IV) ,in Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl. R 1 Indicates hydrogen or methyl. R8 is a C1-C6 alkylene group, preferably ethylene or propylene. R5 and R6 are each independently C1-C6-alkyl, preferably methyl. R7 is C8-C 32 Alkyl groups, optionally substituted with one or more hydroxyl groups, preferably C10. 12 -C 20 Alkyl group, optionally substituted with a hydroxyl group, and Z - It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ;or ,in Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl. R 1 Indicates hydrogen or methyl. R 10 Indicates hydrogen, C8-C 32 Alkyl, C8-C 32 Aryl and / or C8-C 32 Aryl alkyl group, preferably C 12 -C 20 alkyl, R9 is a C1-C6 alkylene group, preferably ethylene or propylene, and n is an integer from 1 to 50, preferably from 2 to 30, more preferably from 3 to 15, and most preferably from 4 to 8; and iv. An olefinically unsaturated crosslinking agent containing 2, 3, 4 or 5 olefinically unsaturated groups.
[0059] According to a preferred embodiment, the polymer dispersion is obtained by a method for preparing a polymer dispersion, wherein the weight-average molecular weight Mw of the polymer dispersion is 40,000 to less than 150,000 g / mol, preferably 50,000 to 140,000 g / mol, more preferably 60,000 to 130,000 g / mol, and most preferably 85,000 to 120,000 g / mol, as determined by size exclusion chromatography.
[0060] According to a preferred embodiment, the polymer dispersion is obtained by a method for preparing a polymer dispersion, wherein the bulk viscosity of the polymer dispersion is less than 6,700 mPa·s, preferably less than 6,000 mPa·s, more preferably less than 5,500 mPa·s, and most preferably less than 5,000 mPa·s, measured at 20°C using a Brookfield viscometer, a No. 4 rotor, and a rotation speed of 10 rpm.
[0061] The fundamental problem of the present invention is also solved by the subject matter of claim 14. Therefore, according to a fourth aspect, the present invention relates to a water-in-water polymer dispersion, characterized in that the water-in-water polymer dispersion is obtained by a method according to a second aspect of the present invention. Therefore, the present invention relates to a water-in-water polymer dispersion obtained by a method for preparing a water-in-water polymer dispersion, the method comprising subjecting an aqueous reaction mixture to a free radical polymerization reaction, the aqueous reaction mixture comprising: (a) A polymer dispersant according to a second aspect of the invention, and (b) A composition comprising one or more of the following monomers: i. Nonionic monomers of formula (I) ,in R 1 Indicates hydrogen or methyl; R 2 and R 3 Each of them is independently hydrogen, C1-C5-alkyl, or C1-C5-hydroxyalkyl. ii. Cationic monomers of formula (II) ,in R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups, preferably ethylene or propylene, optionally substituted with one hydroxyl group; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6-alkyl group, preferably methyl; and Z - It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ;and iii. Amphiphilic monomers of formula (III) or (IV) ,in Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl. R 1 Indicates hydrogen or methyl. R8 is a C1-C6 alkylene group, preferably ethylene or propylene. R5 and R6 are each independently C1-C6-alkyl, preferably methyl. R7 is C8-C 32 Alkyl groups, optionally substituted with one or more hydroxyl groups, preferably C10. 12 -C 20 Alkyl group, optionally substituted with a hydroxyl group, and Z - It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ;or ,in Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl. R 1 Indicates hydrogen or methyl. R 10 Indicates hydrogen, C8-C 32 Alkyl, C8-C 32 Aryl and / or C8-C 32 Aryl alkyl group, preferably C 12 -C 20 alkyl, R9 is a C1-C6 alkylene group, preferably ethylene or propylene. n is an integer from 1 to 50, preferably from 2 to 30, more preferably from 3 to 15, and most preferably from 4 to 8; and iv. An olefinically unsaturated crosslinking agent containing 2, 3, 4 or 5 olefinically unsaturated groups.
[0062] According to a preferred embodiment, the polymer dispersion is obtained by a method for preparing a polymer dispersion, wherein the weight-average molecular weight Mw of the polymer dispersion is 40,000 to less than 150,000 g / mol, preferably 50,000 to 140,000 g / mol, more preferably 60,000 to 130,000 g / mol, and most preferably 85,000 to 120,000 g / mol, as determined by size exclusion chromatography.
[0063] According to a preferred embodiment, the polymer dispersion is obtained by a method for preparing a polymer dispersion, wherein the bulk viscosity of the polymer dispersion is less than 6,700 mPa·s, preferably less than 6,000 mPa·s, more preferably less than 5,500 mPa·s, and most preferably less than 5,000 mPa·s, measured at 20°C using a Brookfield viscometer, a No. 4 rotor, and a rotation speed of 10 rpm.
[0064] The fundamental problem of the present invention is also solved by the subject matter of claim 15. Therefore, according to a fifth aspect, the present invention relates to the use of polymer dispersions according to the third and fourth aspects of the present invention in the following aspects: a. Used as a flocculant in solid sedimentation, flotation, or filtration. b. Used as a thickener c. Used as a pollutant control agent, d. Used as a dry strength agent; e. Or used as a retention aid or filter aid in papermaking.
[0065] Features relating to the preferred embodiments of the first aspect of the invention (these features are disclosed only with respect to the first aspect of the invention) also constitute features of the preferred embodiments of the second, third, fourth and fifth aspects of the invention.
[0066] Exemplary embodiments (A) to (C) representing particularly preferred embodiments are disclosed below.
[0067] (A) A polymeric dispersant for preparing water-in-water dispersions, said polymeric dispersant being water-soluble, prepared by polymerizing a monomer composition in the presence of a chain transfer agent, said monomer composition comprising at least the following monomers: (a1) ,in R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6 alkyl group; and Z - It is a counter ion; (a2) Optional (meth)acrylic acid and / or (meth)acrylamide, The chain transfer agent is characterized in that it comprises an amine having two or three tertiary amine functional groups.
[0068] (B) A method for preparing a water-in-water polymer dispersion, the method comprising subjecting an aqueous reaction mixture to a free radical polymerization reaction, the aqueous reaction mixture comprising: (a) A polymeric dispersant for preparing water-in-water dispersions, said polymeric dispersant being water-soluble and prepared in advance by polymerizing a monomeric composition in the presence of a chain transfer agent, said monomeric composition comprising at least the following monomers: (a1) ,in R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6 alkyl group; and Z - It is a counter ion; (a2) Optional (meth)acrylic acid and / or (meth)acrylamide, The chain transfer agent comprises an amine having two or three tertiary amine functional groups; and (b) Monomer compositions comprising the following monomers: i. Nonionic monomers of formula (I) ,in R 1 Indicates hydrogen or methyl; R 2 and R 3 Each of them is independently hydrogen, C1-C5-alkyl, or C1-C5-hydroxyalkyl. ii. Cationic monomers of formula (II) ,in R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups, preferably ethylene or propylene, optionally substituted with one hydroxyl group; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6-alkyl group, preferably methyl; and Z - It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ;and iv. An olefinically unsaturated crosslinking agent containing 2, 3, 4 or 5 olefinically unsaturated groups.
[0069] (C) A method for preparing a water-in-water polymer dispersion, the method comprising subjecting an aqueous reaction mixture to a free radical polymerization reaction, the aqueous reaction mixture comprising (a) and (b), wherein (a) is a polymeric dispersant for preparing water-in-water dispersions, said polymeric dispersant being water-soluble and prepared in advance by polymerizing a monomeric composition in the presence of a chain transfer agent, said monomeric composition comprising at least the following monomers: (a1) ,in R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6 alkyl group; and Z - It is a counter ion; (a2) Optional (meth)acrylic acid and / or (meth)acrylamide, The chain transfer agent comprises an amine having two or three tertiary amine functional groups; and (b) is a monomer composition comprising the following monomers: i. (Meth)acrylic acid or (meth)acrylamide, ii. Quaternized trimethylammonium-propyl (meth)acrylamide; and iv. An olefinically unsaturated crosslinking agent containing 2 or 3 olefinically unsaturated groups.
[0070] Example The testing methods used are described in detail below: Bulk viscosity measurements are as follows: Use the product directly for measurement. Slowly immerse rotor #4 into the product and measure the viscosity using a Brookfield RVT viscometer at 10 rpm. Stop the measurement when the reading remains constant for 30 seconds.
[0071] Molecular weight measurements are as follows: Molar mass is measured by size exclusion chromatography (SEC). This measurement is particularly useful for determining the molecular weight of dispersants.
[0072] Molecular weight was characterized using an aqueous SEC calibrated with Pullulan standards.
[0073] Sample preparation: The sample was diluted with eluent (the polymer was dissolved in a volumetric flask) and filtered through a 1µm filter cartridge (M&N) (using a syringe) before injection.
[0074] If the instrument is equipped with an autosampler filter, the solution is filtered into a vial through a 1µm filter cartridge.
[0075] Parameters used: Instrument: SEC (Agilent) Column: Novema 3000 (PSS) Detector: RI Eluent: 1.5 wt% formic acid aqueous solution Flow rate: 1 ml / min Calibration standards: Pullland of different Mw The following embodiments further illustrate the present invention, but should not be construed as limiting its scope.
[0076] Example 1: Synthesis of Polymer Dispersants First, 294.06 g of water, 666.7 g of acrylamidopropyltrimethylammonium chloride (DIMAPA quaternary ammonium salt) (60 wt%), and sulfuric acid (50 wt%) were weighed into a 2 L container to adjust the pH to 5.0 ± 0.2. Then, the monomer solution was purged with nitrogen for 30 minutes with stirring. Subsequently, the aqueous solution was heated to 65°C, and N-[3-(dimethylamino)propyl]-3-{[3-(dimethylamino)propyl](2-{[3-(dimethylamino)propyl]carbamoyl}ethyl)amino}acrylamide, 2-mercaptoethanol, and V-50 (2,2'-azobis(2-amidinylpropane)dihydrochloride) were added to the solution. After reaching Tmax, the container was cooled to ≤80°C. Then, additional initiator (V-50) was added to the product in two portions over 10 minutes to consume the remaining monomer. The product was stirred at 70°C for 1 hour. The final aqueous product is cooled to 30°C. The dispersant is provided as a 40% by weight aqueous solution.
[0077] Example 2: Synthesis of polymer dispersion (charge density 15 mol%) In a batch process (batch size of 1,000 kg), acrylamide and acryloyloxyethyltrimethylammonium chloride (ADAME quaternary ammonium salt) were polymerized in an aqueous solution in the presence of acrylamidopropyltrimethylammonium chloride (the polymer dispersant of Example 1). The aqueous phase was prepared at 200 rpm.
[0078] First, 206.90 kg of soft water, 261.80 kg of bio-based acrylamide (49 wt%), 77.20 kg of acryloyloxyethyltrimethylammonium chloride (ADAME quaternary ammonium salt) (80 wt%), 412.50 kg of the polymer dispersant from Example 1, 10.00 kg of ammonium sulfate, and 0.20 kg of Trilon C were added to the reaction vessel. The pH was adjusted to pH 5.0 ± 0.2 with approximately 0.10 kg of sulfuric acid (50%). The vessel was evacuated five times before being purged with nitrogen. The initiator composition was added under a negative pressure of 0.5 bar and at maximum stirrer speed. Initiation was started at 22±1°C by adding 0.34 kg of V-50 dissolved in 3.05 kg of soft water, 0.025 kg of sodium persulfate dissolved in 0.47 kg of soft water, 0.014 kg of sodium bisulfite dissolved in 0.27 kg of soft water, and 0.003 kg of tert-butyl hydroperoxide (70%) dissolved in 1 kg of soft water. The container was then purged with nitrogen again. After reaching the maximum temperature, 0.17 kg of V-50 solution dissolved in 1.53 kg of soft water was added to reduce the monomer content. After a one-hour post-reaction time, the product was cooled to below 40°C. Then, 8.30 kg of citric acid and 0.82 kg of the fungicide Acticide SPX were added, and the product was cooled to below 30°C.
Claims
1. A polymeric dispersant for preparing water-in-water dispersions, said polymeric dispersant being water-soluble and prepared by polymerizing a monomer composition in the presence of a chain transfer agent, said monomer composition comprising at least the following monomers: (a1) ,in R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6 alkyl group; and Z - It is a counter ion; (a2) Optional (meth)acrylic acid and / or (meth)acrylamide, Its features are, The chain transfer agent contains an amine.
2. The polymer dispersant according to claim 1, characterized in that, The monomer composition further comprises (a3) a divalent olefin unsaturated monomer, wherein preferably the divalent olefin unsaturated monomer is a (meth)acrylate containing an allyl functional group or a (meth)acrylamide ester containing an allyl functional group, and more preferably the divalent olefin unsaturated monomer is N-allylacrylamide.
3. The polymer dispersant according to claim 1 or 2, characterized in that, The chain transfer agent is a mixture of amines and thiols.
4. The polymer dispersant according to any one of claims 1 to 3, characterized in that, The amine comprises two or more amine functional groups; and / or is characterized in that, The amine contains two or more, preferably two or three tertiary amine functional groups.
5. The polymer dispersant according to any one of claims 1 to 4, characterized in that, The amine is N-[3-(dimethylamino)propyl]-3-{[3-(dimethylamino)propyl]amino}acrylamide, N-[3-(dimethylamino)propyl]-3-{[3-(dimethylamino)propyl](2-{[3-(dimethylamino)propyl]carbamoyl}ethyl)amino}acrylamide, or a mixture thereof.
6. The polymer dispersant according to any one of claims 1 to 5, characterized in that, The amine is present in an amount of 0.1 to 10% by weight, preferably 0.5 to 8% by weight, more preferably 1 to 5% by weight, based on the total weight of the monomer composition; preferably characterized in that the amine is N-[3-(dimethylamino)propyl]-3-{[3-(dimethylamino)propyl]amino}acrylamide, N-[3-(dimethylamino)propyl]-3-{[3-(dimethylamino)propyl](2-{[3-(dimethylamino)propyl]carbamoyl}ethyl)amino}acrylamide or a mixture thereof, and is present in an amount of 0.1 to 10% by weight, preferably 0.5 to 8% by weight, more preferably 1 to 5% by weight, based on the total weight of the monomer composition.
7. The polymer dispersant according to any one of claims 1 to 6, characterized in that, The polymer dispersant is a cationic polymer dispersant, preferably characterized in that, In monomer a1, Z1 is O, NH or NR4, preferably NH or NR4, wherein R4 represents methyl; Y is ; Y1 is ethylene or propylene, optionally substituted with a hydroxyl group; Y5, Y6, and Y7 are each methyl groups; and Z - It is selected from halogens, halogen-like substances, acetate, and SO4CH3. - Counterions.
8. The polymer dispersant according to any one of claims 1 to 7, characterized in that, The polymer dispersant has a weight-average molecular weight (Mw) of 40,000 to less than 150,000 g / mol, preferably 50,000 to 140,000 g / mol, more preferably 60,000 to 130,000 g / mol, and most preferably 85,000 to 125,000 g / mol, as determined by size exclusion chromatography.
9. A method for preparing a water-in-water polymer dispersion, the method comprising subjecting an aqueous reaction mixture to a free radical polymerization reaction, said aqueous reaction mixture comprising: (a) The polymer dispersant according to any one or more of claims 1 to 8, and (b) A composition comprising one or more of the following monomers: i. Nonionic monomers of formula (I) ,in R 1 Indicates hydrogen or methyl; R 2 and R 3 Each of them is independently hydrogen, C1-C5-alkyl, or C1-C5-hydroxyalkyl. ii. Cationic monomers of formula (II) ,in R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups, preferably ethylene or propylene, optionally substituted with one hydroxyl group; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6-alkyl group, preferably methyl; and Z - It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ; iii. Amphiphilic monomers of formula (III) or (IV) ,in Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl. R1 represents hydrogen or methyl. R8 is a C1-C6 alkylene group, preferably ethylene or propylene. R5 and R6 are each independently C1-C6-alkyl, preferably methyl. R7 is C8-C 32 Alkyl groups, optionally substituted with one or more hydroxyl groups, preferably C10. 12 -C 20 Alkyl group, optionally substituted with a hydroxyl group, and Z - It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ;or ,in Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl. R1 represents hydrogen or methyl. R 10 Indicates hydrogen, C8-C 32 Alkyl, C8-C 32 Aryl and / or C8-C 32 Aryl alkyl group, preferably C 12 -C 20 alkyl, R9 is a C1-C6 alkylene group, preferably ethylene or propylene. n is an integer from 1 to 50, preferably from 2 to 30, more preferably from 3 to 15, and most preferably from 4 to 8; and iv. An olefinically unsaturated crosslinking agent containing 2, 3, 4 or 5 olefinically unsaturated groups.
10. The method according to claim 9, characterized in that, The monomer composition comprises at least a nonionic monomer of formula (I) and a cationic monomer of formula (II).
11. The method according to claim 9 or 10, characterized in that, The nonionic monomer of formula (I) is acrylamide.
12. The method according to any one of claims 9 to 11, characterized in that, The olefin unsaturated crosslinking agent containing 2, 3, 4 or 5 olefin unsaturated groups is a crosslinking agent containing 2 or 3 olefin unsaturated groups, preferably selected from methylene bisacrylamide, polyethylene glycol diacrylate and triallylamine.
13. A water-in-water polymer dispersion comprising: (a) The polymer dispersant according to any one or more of claims 1 to 8, and (b) A copolymer derived from a monomer composition comprising one or more of the following: i. Nonionic monomers of formula (I) ,in R 1 Indicates hydrogen or methyl; R 2 and R 3 Each of them is independently hydrogen, C1-C5-alkyl, or C1-C5-hydroxyalkyl. ii. Cationic monomers of formula (II) ,in R 1 Indicates hydrogen or methyl; Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl, and Y is one of the following groups: or ,in Y0 and Y1 are C1-C6 alkylene groups, optionally substituted with one or more hydroxyl groups, preferably ethylene or propylene, optionally substituted with one hydroxyl group; Y2, Y3, Y5, Y6, and Y7 are each independently a C1-C6-alkyl group, preferably methyl; and Z - It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ; iii. Amphiphilic monomers of formula (III) or (IV) ,in Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl. R 1 Indicates hydrogen or methyl. R8 is a C1-C6 alkylene group, preferably ethylene or propylene. R5 and R6 are each independently C1-C6-alkyl, preferably methyl. R7 is C8-C 32 Alkyl groups, optionally substituted with one or more hydroxyl groups, preferably C10. 12 -C 20 Alkyl group, optionally substituted with a hydroxyl group, and Z - It is a counterion, preferably a halogen, a halogen-like ion, an acetate ion, or SO4CH3. - ;or ,in Z1 is O, NH, or NR4, where R4 represents a C1-C4-alkyl group, preferably methyl. R 1 Indicates hydrogen or methyl. R 10 Indicates hydrogen, C8-C 32 Alkyl, C8-C 32 Aryl and / or C8-C 32 Aryl alkyl group, preferably C 12 -C 20 alkyl, R9 is a C1-C6 alkylene group, preferably ethylene or propylene, and n is an integer from 1 to 50, preferably from 2 to 30, more preferably from 3 to 15, and most preferably from 4 to 8; and iv. An olefinically unsaturated crosslinking agent containing 2, 3, 4 or 5 olefinically unsaturated groups.
14. A water-in-water polymer dispersion, characterized in that, The water-in-water polymer dispersion is obtained by the method according to any one of claims 9 to 12.
15. Use of the polymer dispersion according to claim 13 or 14 in the following respects: • Used as a flocculant in solid sedimentation, flotation, or filtration. • Used as a thickener • Used as a pollutant control agent, • Used as a dry strength agent; • Or it can be used as a retention aid or filter aid in papermaking.
Citation Information
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