JPS56133302A - Production of high-purity polymer by emulsion polymerization - Google Patents
Production of high-purity polymer by emulsion polymerizationInfo
- Publication number
- JPS56133302A JPS56133302A JP3777380A JP3777380A JPS56133302A JP S56133302 A JPS56133302 A JP S56133302A JP 3777380 A JP3777380 A JP 3777380A JP 3777380 A JP3777380 A JP 3777380A JP S56133302 A JPS56133302 A JP S56133302A
- Authority
- JP
- Japan
- Prior art keywords
- surfactant
- polymer
- aqueous phase
- coagulant
- emulsion polymerization
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1868—Stationary reactors having moving elements inside resulting in a loop-type movement
- B01J19/1881—Stationary reactors having moving elements inside resulting in a loop-type movement externally, i.e. the mixture leaving the vessel and subsequently re-entering it
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1893—Membrane reactors
Abstract
PURPOSE: Emulsion polymerization is effected using a specific surfactant, the polymer is coagulated with inorganic salts or the like to separte from the aqueous phase, rinsed with water, the aqueous phase is treated with a semipermeable membrane and reused, thus economically producing the titled polymer with less surfactant remaining.
CONSTITUTION: Emulsion polymerization is conducted in a polymerization tank 1 using a surfactant with at least 50wt% distribution ratio to the aqueous phase between the polymer phase and the aqueous phase in latex. The latex is coagulated in a coagulation tank 2 using a coagulant composed of inorganic salts and/or inorganic acids and separated into the polymer and the aqueous phase using a sieve 3 for separating polymers. The polymer is rinsed with water 4. Further, the aqueous solution 10 that has been used in separation and rinsing and contains the surfactant and the coagulant is treated with a semipermeable membrane I with less than 90% and 60% exclusion rate to the surfactant and the coagulant respectively to separate into a surfactant solution 20 and a coagulant solution 30. Each of them is circulated for reuse.
COPYRIGHT: (C)1981,JPO&Japio
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3777380A JPS56133302A (en) | 1980-03-25 | 1980-03-25 | Production of high-purity polymer by emulsion polymerization |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3777380A JPS56133302A (en) | 1980-03-25 | 1980-03-25 | Production of high-purity polymer by emulsion polymerization |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS56133302A true JPS56133302A (en) | 1981-10-19 |
JPH0116841B2 JPH0116841B2 (en) | 1989-03-28 |
Family
ID=12506786
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3777380A Granted JPS56133302A (en) | 1980-03-25 | 1980-03-25 | Production of high-purity polymer by emulsion polymerization |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS56133302A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001034293A1 (en) * | 1999-11-11 | 2001-05-17 | Akzo Nobel N.V. | Emulsion polymerization process and reactor for such a process |
WO2003035244A1 (en) * | 2001-10-26 | 2003-05-01 | Octoplus Sciences B.V. | Method for the preparation of purified microparticles |
-
1980
- 1980-03-25 JP JP3777380A patent/JPS56133302A/en active Granted
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001034293A1 (en) * | 1999-11-11 | 2001-05-17 | Akzo Nobel N.V. | Emulsion polymerization process and reactor for such a process |
JP2003514072A (en) * | 1999-11-11 | 2003-04-15 | アクゾ ノーベル ナムローゼ フェンノートシャップ | Emulsion polymerization method and reactor for the method |
US6569961B1 (en) | 1999-11-11 | 2003-05-27 | Akzo Nobel Nv | Emulsion polymerization process and reactor for such a process |
WO2003035244A1 (en) * | 2001-10-26 | 2003-05-01 | Octoplus Sciences B.V. | Method for the preparation of purified microparticles |
EP1306127A1 (en) * | 2001-10-26 | 2003-05-02 | OctoPlus Technologies B.V. | Method for the preparation of purified microparticles |
US7468151B2 (en) | 2001-10-26 | 2008-12-23 | Octoplus Sciences B.V. | Method for the preparation of purified microparticles |
Also Published As
Publication number | Publication date |
---|---|
JPH0116841B2 (en) | 1989-03-28 |
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