Ultrafiltration process for the concentration of polymeric latices

Claim 2

In a process for the concentration or separation of an aqueous polymeric latex, which comprises polymer particles dispersed in an aqueous-liquid phase, by a semipermeable membrane which permits the passage of the liquid phase and retains the polymer particles, the improvement which comprises: adding to the latex a sufficient amount of a compatible surfactant to maintain the dispersion of the polymer particles in the liquid phase during the concentration or separation process, thereby preventing the formation of coagulum into the latex and the degradation of the flux rate of the process.

Claim 3

The process of claim 1 which includes adding about 0.05 to 2.0 weight percent of the surfactant based on the weight of the polymer in the latex.

Claim 4

The process of claim 1 wherein the process is an ultrafiltration process carried out at a pressure of about 10 to 200 psi.

Claim 5

The process of claim 1 wherein the process is an ultrafiltration process carried out at a temperature of from about 70° to 180° F.

Claim 6

The process of claim 1 wherein the latex is a vinylchloride resin, a styrene-butadiene or a natural rubber latex.

Claim 7

The process of claim 1 wherein the latex contains from about 0.1 to 2% by weight polymer, and is concentrated to about 10 to 20%.

Claim 8

The process of claim 1 wherein the latex contains from about 20 to 40% by weight polymer, and is concentrated to about 45 to 70%.

Claim 9

The process of claim 1 wherein the latex contains a surfactant and the surfactant added is the same surfactant as in the latex.

Claim 10

The process of claim 1 wherein the surfactant is an anionic or a nonionic surfactant.

Claim 11

The process of claim 1 wherein the surfactant is an anionic surfactant which comprises a water-soluble salt of a long-chain alcohol sulfate.

Claim 12

The process of claim 1 wherein the surfactant is a nonionic surfactant which comprises an alkylaryl polyether alcohol.

Claim 13

The process of claim 1 wherein the latex is introduced into contact with the semipermeable membrane by an openedface impeller centrifugal pump.

Claim 14

The process of claim 1 which includes adding the surfactant to a batch of the latex prior to concentration and separation and pumping the latex into contact with the semipermeable membrane.

Claim 15

The process of claim 1 wherein the latex is withdrawn from and recirculated into contact with the semipermeable membrane until the desired concentration level is obtained.

Claim 16

The process of claim 1 wherein the semipermeable membrane is disposed in an ultrafiltration apparatus containing tubes to support the membrane or in a spiral module apparatus.

Claim 17

The process of claim 1 which includes adding surfactant continuously to the latex.

Claim 18

In a process for the concentration or separation of an aqueous polymeric latex, which comprises polymer particles dispersed in an aqueous liquid phase, by an ultrafiltration semipermeable membrane process wherein the membrane permits the passage of the liquid phase and retains the polymer particles, the improvement which comprises: (a) providing a latex selected from the group of polymers consisting of vinyl-chloride, butadiene-styrene and natural rubber, which latex, under the process conditions of the ultrafiltration process, becomes destabilized; (b) adding to the latex a sufficient amount of a compatible anionic or nonionic surfactant to maintain the dispersion of the polymer particles in the liquid phase during the concentration or separation process, thereby preventing the formation of coagulum from the latex and the degradation of the flux rate of the process; (c) pumping the stabilized latex into the inlet of a feed zone of an ultrafiltration membrane device; (d) withdrawing a permeate fraction from the permeate zone of the ultrafiltration device; (e) withdrawing a concentrated latex from the feed zone and recycling by pumping at least a portion of the concentrated latex to the inlet of the feed zone; and (f) recovering a concentrated latex from the feed zone.

Claim 19

In a process for the concentration or separation of an aqueous polymeric latex, which comprises polymer particles dispersed in an aqueous liquid phase, by an ultrafiltration semipermeable membrane process wherein the membrane permits the passage of the liquid phase and retains the polymer particles, the improvement which comprises: (a) providing a latex selected from the group of polymers consisting of vinyl-chloride, butadiene-styrene and natural rubber, which latex, under the process conditions of the ultrafiltration process, becomes destabilized; (b) adding to the latex a sufficient amount of a compatible anionic or nonionic surfactant to maintain the dispersion of the polymer particles in the liquid phase during the concentration or separation process, thereby preventing the formation of coagulum from the latex and the degradation of the flux rate of the process; (c) pumping the stabilized latex into the inlet of a feed zone of an ultrafiltration membrane device; (d) withdrawing a permeate fraction from the permeate zone of the ultrafiltration device; (e) withdrawing a concentrated latex from the feed zone and recycling by pumping at least a portion of the concentrated latex to the inlet of the feed zone; and (f) recovering a concentrated latex from the feed zone.