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polymer with releasable gas

A technology of polymers and compositions, applied in the direction of cation exchange materials, etc., can solve the problems of long time and difficulty that cannot be completed

Active Publication Date: 2020-07-21
ROHM & HAAS CO
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Attempts to perform free radical polymerization in aqueous media without one or more of these additives have resulted in one or more difficulties
For example, some such attempts have resulted in aggregation methods that either cannot complete or take an undesirably long time to complete

Method used

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  • polymer with releasable gas
  • polymer with releasable gas
  • polymer with releasable gas

Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0116] Preparation of the reaction mixture

[0117] Suspensions of droplets suspended in an aqueous medium were prepared using the spraying procedure described in US 4,444,960 and US 4,623,706. The droplets contain styrene, DVB and BPO. The aqueous medium contains deionized water, CMMC, PVOH and sodium nitrite. The composition of the composition intended for droplets is as follows:

[0118] Droplet Composition:

[0119] Element

quantity (1)

Styrene balance (2)

DVB 5.2% BPO 0.5%

[0120] Note (1): % by weight, based on the total weight of the droplet components.

[0121] Note (2): To constitute 100% by weight

[0122] The composition intended for the aqueous liquid medium is as follows:

[0123] water phase composition

[0124]

[0125]

[0126] Note (3): % by weight, based on the total weight of the aqueous phase ingredients

[0127] During the preparation of the reaction mixture, some individual ingredients or por...

example 1

[0129] Example 1: Addition of NaOH at 53% reaction degree

[0130] Preparation of Example 1.

[0131] The reaction mixture was subjected to aqueous suspension polymerization as follows. The reaction mixture was heated to 80°C, and the extent of the reaction was monitored. At some point, a portion of the NaOH solution was added to the reaction mixture. The amount of NaOH added is characterized by the weight of ppm of NaOH based on the weight of water. Prepared as follows

[0132]

[0133] At the beginning of the polymerization, the pH was 6.5. At the completion of the polymerization, the pH was 10.8. The product was polymer beads with a harmonic mean size of 210 μm.

[0134] The results of Example 1 are as follows:

[0135]

[0136] Note (4): Addition of NaOH solution

[0137] All measurements made after the 90% degree showed a rate of 20% / hr or less. Before NaOH addition at the level of 53%, the rate leveled off at ~30% / hr; after NaOH addition, the rate increased ...

example 2

[0143] Example 2: Addition of NaOH at levels from 32.5% to 51%, and pH measurements

[0144] Three additional polymerizations (Example 2-1, Example 2-2, and Example 2-3) were performed using the same materials and methods as Example 1. In Example 2, the degree of NaOH addition varied, and the overall batch size in Example 2 was smaller than in Example 1. In Example 2, the pH was measured immediately after the addition of NaOH. The result is as follows:

[0145] Example 2

[0146] 2-1 2-2 2-3 initial pH 6.4 6.5 6.5 The extent of the first NaOH addition 42% 51% 32.5% ppm of NaOH added for the first time 210 210 210 pH immediately after the first NaOH addition 11.26 11.27 11.58 The extent of the second NaOH addition 87.5% 86.0% 87.5% The pH just before the second NaOH addition 7.31 7.75 7.24 ppm of the second NaOH addition 100 100 100 pH immediately after the second NaOH addition 11.0 10.78 10.89 ...

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Abstract

The present invention provides a method of forming a polymer comprising: (a) providing a reaction mixture comprising (i) one or more vinyl monomers, (ii) one or more pH-sensitive suppression systems, (iii) one or more initiators, and (iv) water; (b) establishing conditions in the reaction mixture such that free radical polymerization of the vinyl monomer occurs at one location, and (c) After steps (a) and (b) and before completion of the free radical polymerization, the pH of the reaction mixture is changed to increase the rate of generation of the free radical polymerization at the site of the free radical polymerization.

Description

Background technique [0001] Carrying out free radical polymerization processes in aqueous media is generally carried out in the presence of one or more of various additives other than initiators and monomers. For example, inhibitors are sometimes present, eg, to prevent certain undesired polymerization reactions in favor of desired polymerization(s). For example, when suspension polymerization is desired, inhibitors may be present in order to inhibit the process of emulsion polymerization. One commonly used inhibitor is dichromate. Dichromates are undesirable due to the toxicity of various chromium compounds. For another example, an acid with a first pKa of 8 to 12 is sometimes used, for example to buffer the aqueous medium at a pH of 8 to 12. A commonly used organic acid with a first pKa of 8 to 12 is boric acid. Boric acid is undesirable due to the toxicity of various boron compounds. For a third example, gelatin is sometimes used, for example as a dispersion stabilizer...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F12/08C08F212/08C08F212/36C08F2/00C08F8/30
CPCC08F8/30C08F12/08C08F212/08C08F2/001C08F212/36B01J39/20C08L25/04C08L33/06C08F2/42C08F112/08
Inventor J·D·芬奇A·M·萨沃
Owner ROHM & HAAS CO