Process for obtaining a cationic polymer with an at least bimodal molecular weight distribution

Patent metadata

Field	Value
Publication number	US-10920001-B2
Application number	US-201716072552-A
Country	US
Kind code	B2
Filing date	Jan 16, 2017
Priority date	Jan 25, 2016
Publication date	Feb 16, 2021
Grant date	Feb 16, 2021

Abstract

The present invention relates to a process for obtaining a cationic polymer by polymerization of at least one cationic monomer, at least one crosslinker and optionally further monomers, such as nonionic monomers, associative monomers and/or chain transfer agents. The cationic polymer has an at least bimodal molecular weight distribution with at least one first peak (P1) and at least one second peak (P2), wherein the first peak has a lower average sedimentation coefficient of ≤100 Sved and the second peak has a higher average sedimentation coefficient of ≥1000 Sved. The polymerization is carried out in two subsequent steps I) and II). In step II), the crosslinker is either completely absent or present in a very limited amount. Step II) is carried out after the polymerization of step I is finished or vice versa.

First claim

The invention claimed is:

1. A process for obtaining a cationic polymer by polymerization of
a) at least one cationic monomer and at least one nonionic monomer (monomer component a), wherein
the cationic monomer according to monomer component a) in the cationic polymer is selected from a compound of the formula (II)

where
R 1 is H or C 1 -C 4 -alkyl,
R 2 is H or methyl,
R 3 is C 1 -C 4 -alkylene,
R 4 , R 5 and R 6 are each independently H or C 1 -C 30 -alkyl,
X is —O— or —NH— and
Y is Cl; Br; I; hydrogensulfate or methosulfate,
wherein monomer component a) in the cationic polymer comprises 30 to 99.5% by weight of at least one cationic monomer and 0.5 to 70% by weight of at least one nonionic monomer,
b) at least one crosslinker (monomer component b),
c) optionally at least one chain transfer agent (monomer component c),
wherein the cationic polymer has an at least bimodal molecular weight distribution with at least one first peak (P1) with an average sedimentation coefficient of ≤100 Sved and with at least one second peak (P2) with an average sedimentation coefficient of ≥1000 Sved, and
wherein the polymerization is carried out in two steps I) and II) with:
I) polymerization of monomer component a) and monomer component b),
II) polymerization of monomer component a), optionally monomer component c) and in a complete absence or in a presence of <10 ppm (related to a total amount of cationic polymer) of monomer component b),
wherein step II) is carried out after the polymerization of step I) is finished or step I) is carried out after the polymerization of step II) is finished.

2. The process according to claim 1 , wherein
i) the nonionic monomer according to monomer component a) in the cationic polymer is selected from N-vinylpyrrolidone, N-vinylimidazole or a compound of the formula (III)

where
R 7 is H or C 1 -C 4 -alkyl,
R 8 is H or methyl, and
R 9 and R 10 are each independently H or C 1 -C 30 -alkyl, and/or
ii) the crosslinker (monomer component b) in the cationic polymer is selected from
divinylbenzene; tetraallylammonium chloride; allyl acrylates; allyl methacrylates; diacrylates and dimethacrylates of glycols or polyglycols; butadiene; 1,7-octadiene; allylacrylamides or allylmethacrylamides; bisacrylamidoacetic acid; N,N′-methylenebisacrylamide; polyol polyallyl ethers such as polyallyl sucrose or pentaerythritol triallyl ether; pentaerythrityl triacrylate; pentaerythrityl tetraacrylate; 1,1,1-trimethylolpropane tri(meth)acrylate; the ethoxylated compounds thereof or a mixture thereof, and/or
iii) the chain transfer agent (monomer component c) in the cationic polymer is selected from mercaptans, lactic acid, formic acid, isopropanol or hypophosphites.

3. The process according to claim 1 , wherein the monomer component a) contains at least one cationic monomer and at least one nonionic monomer.

4. The process according to claim 1 , wherein the polymerization is an emulsion polymerization, and/or steps I) and II) are carried out in the same polymerization vessel.

5. The process according to claim 1 , wherein
i) the at least one first peak (P1) is splitted into at least two peaks and a weight average sum of said peaks has a sedimentation coefficient of ≤50 Sved, and/or
ii) the at least one first peak (P1) is not splitted into more than one peak and the at least one first peak (P1) has an average sedimentation coefficient of ≤50 Sved, and/or iii) the at least one second peak (P2) has an average sedimentation coefficient of ≥10,000 Sved, and/or
iv) the cationic polymer has an at least trimodal molecular weight distribution.

6. The process according to claim 1 , wherein the at least one first peak (P1) is splitted into at least two peaks wherein
i) a lower molecular weight peak (P1.1) has a weight average peak maximum of ≤1,000,000 g/mol, and a higher molecular weight peak (P1.2) has a weight average peak maximum of ≥1,000,000 g/mol, and/or
ii) the lower molecular weight peak (P1.1) has an average sedimentation coefficient of ≤Sved, and the higher molecular weight peak (P1.2) has an average sedimentation coefficient of >10 Sved.

7. The process according to claim 1 , wherein the polymer is obtainable by additional polymerization of
d) at least one associative monomer (monomer component d),
the at least one associative monomer according to monomer component d) in the cationic polymer is selected from the group consisting of a compound of the formula (I)
R—O—(CH 2 —CHR′—O) n —CO—CR″═CH 2   (I)

where
R is C 6 -C 50 -alkyl,
R′ is H or C 1 -C 4 -alkyl,
R″ is H or methyl,
n is an integer from 0 to 100.

8. The process according to claim 1 , wherein water-soluble polymer components of the cationic polymer are between 5 to 95% by weight, related to the total amount of cationic polymer.

9. The process according to claim 8 , wherein in step II) ≥5%, by weight of the water-soluble polymer components of the cationic polymer are produced related to the total amount of cationic polymer.

10. The process according to claim 7 , wherein
i) step II) is carried out after the polymerization of step I) is finished, and/or
ii) step II) is carried out by polymerization of monomer component a), monomer component c) and optionally monomer component d), and/or
iii) monomer component b) is completely absent during the polymerization according to step II), and/or
iv) step I) is carried out by polymerization of monomer component a), 10 to 10,000 ppm, (related to the total amount of cationic polymer) of monomer component b) and optionally monomer component c), and/or
v) in step II), 5 to 95% by weight of water-soluble polymer components of the cationic polymer are produced related to the total amount of cationic polymer.

11. The process according to claim 1 , wherein
i) in both steps I) and II), an aqueous phase and an oil phase are employed, and/or
ii) the aqueous phase in step I) contains at least one cationic monomer, at least one crosslinker and optionally at least one nonionic monomer, and/or
iii) the oil phase in step I) and/or step II) contains at least one stabilizing agent, at least one first oil, at least one second oil and optionally at least one associative monomer, wherein the at least one first oil is selected from dearomatized aliphatic hydrocarbons or mineral oils of low viscosity and the at least one second oil is selected from 2-ethylhexyl stearate and hydroheated heavy naphtha, and/or
iv) the aqueous phase in step II) contains at least one cationic monomer, at least one nonionic monomer, and optionally at least one chain transfer agent, and/or
v) in step II), a mixture of the aqueous phase and the oil phase is completely added to a polymerization vessel (batch reaction) and afterwards at least one initiator is added continuously, and/or
vi) in step II), the mixture of the aqueous phase and the oil phase is continuously added to the polymerization vessel (continuous reaction) and the at least one initiator is added prior to said mixture or the at least one initiator is added continuously and in parallel to said mixture into the polymerization vessel.

12. The process according to claim 1 , wherein
i) step I) is initiated at a lower temperature than a temperature of step II), and/or
ii) step I) is carried out at a temper

Assignees

• Basf Se

Inventors

• Leyrer Reinhold J
• Fonseca Gledison
• Flores-Figueroa Aaron
• Boyko Volodymyr
• Dykstra Robert Richard
• Sivik Mark Robert

Classifications

• C08F2/22 Primary

  Emulsion polymerisation · CPC title

• C08L39/06

  Homopolymers or copolymers of N-vinyl-pyrrolidones · CPC title

• C08L39/04

  Homopolymers or copolymers of monomers containing heterocyclic rings having nitrogen as ring member · CPC title

• C08F226/12

  N-Vinylcarbazole · CPC title

• C08F226/10

  N-Vinyl-pyrrolidone · CPC title