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Improved solventless sulfonation of exchange resins

A sulfonation and resin technology, applied in the field of improved solvent-free sulfonation of exchange resins, can solve the problems of increasing the time of the total production cycle, increasing expenditure, etc.

Inactive Publication Date: 2006-11-01
DOW GLOBAL TECH LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, chlorinated solvents are not as safe as once thought
Currently, there are two problems with the continued use of 1,2-dichloroethane: residual solvent in gelled cation exchange resin products, and increased expenditure on disposing of the solvent in an environmentally friendly manner
The acid concentration used to wash the sulfonated beads is gradually reduced, which increases the overall production cycle time

Method used

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  • Improved solventless sulfonation of exchange resins
  • Improved solventless sulfonation of exchange resins
  • Improved solventless sulfonation of exchange resins

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1-10

[0047] The laboratory sulfonator is a glass vessel with a capacity of 1.7 liters. It has a fill port, a fluoropolymer paddle agitator, and a foot valve. The stirrer was driven by a variable speed motor at 200 rpm. The temperature gradient is controlled by an automatic process control computer. The acid concentration is determined by first taking a small sample and titrating it with caustic. Microscopic observation was used to determine when sulfonation was complete, ie, there was no visible polymer core surrounded by a shell of sulfonated polymer.

Embodiment 1

[0049] Experiments were performed at low hydration rates using high initial sulfuric acid concentrations. The copolymers were seeded in situ (semi-batch, Harris, in U.S. Patent 4,564,644 and U.S. Patent 5,068,255) and used 5 wt% active divinylbenzene from 55% DVB and 45% A monomer mixture of ethylvinylbenzene is polymerized. The measured toluene swell crosslinking corresponds to 8% DVB. The copolymer beads were 20 / 45 US mesh in size (that is, the beads were between 354 and 841 microns in size). The copolymer itself has a gel structure. T of copolymer / monomer mixture g Estimated to be 117°C. The copolymer was sulfonated by adding 97% sulfuric acid and heating at 1.0°C / minute to 140°C and maintaining at this temperature for two hours. The resin was hydrated as follows: Acid was pumped into the top of the resin bed so that the acid concentration was reduced and the resin was hydrated at a rate of 1.2 to 1.75% per minute. Acid was removed from the bottom of the column at the...

Embodiment 2

[0051] Experiments were performed on a second polymer to show the effect of reducing the acid concentration at a given temperature. Copolymerization of 8% active divinylbenzene with a particle size of 20 / 45 US mesh (that is, the particle size of the beads is between 354 and 381 microns) at three different starting acid concentrations For sulfonation, the copolymer and acid slurry was heated to 140°C at 1°C / min and maintained at 140°C for the time listed in the table to achieve complete sulfonation. T of copolymer / monomer mixture g Estimated to be 113°C. figure 1 Results are shown for WUBs at each concentration after hydration at a rate of 12% / min. Higher concentrations have shorter sulfonation times, but a lower percentage of intact, unbroken beads.

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Abstract

A process for the preparation of styrene-divinylbenzene gel cationic exchange resins by sulfonation in sulfuric acid, without the addition of a swelling agent or acrylic co-monomers, with relatively fast hydration rate. The use of temperature and acid concentration to increase the rate of sulfonation while controlling the side reaction of sulfone bridging minimizes reaction time while maximizing bead quality.

Description

[0001] This application claims the benefit of US Provisional Patent Application 60 / 485,166, filed July 7,2003. Background of the invention [0002] Commercially available cation exchangers are well known in the art. In US 2,366,007, D'Alelio first described cation exchange resins based on sulfonated styrene-divinylbenzene copolymers. Boyer in US 2,500,149 describes the use of swelling agents during sulfonation. The use of solvents, especially chlorinated solvents, in the gel cation exchange resin process has become the preferred process and produces mechanically and osmotically stable cation exchange resins with low bead breakage. The most commonly used solvent in the gel cation exchange resin method is 1,2-dichloroethane. US Patent 5,248,435 discloses the sulfonation of porous styrene-divinylbenzene copolymers by adding a chlorine-containing swelling agent containing sulfuric acid at a concentration of 95% at 85°C. However, chlorinated solvents have become less safe than o...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F8/36B01J39/20C08F212/08C08F212/36C08F257/02C08J5/20
CPCB01J39/20C08F8/36C08F2800/20C08F2810/20C08F212/08C08F257/02
Inventor M·H·蒂根R·S·特施W·I·哈里斯
Owner DOW GLOBAL TECH LLC