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Cyclic process for the production of taurine from alkali isethionate

a technology of cyclic process and alkali isethionate, which is applied in the field of cyclic process for the production of taurine from alkali isethionate and alkali vinyl sulfonate, can solve the problems of large waste stream, low overall yield, and inability to meet the requirements of the process,

Active Publication Date: 2021-01-12
VITAWORKS IP LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the ethylene oxide process is well established and widely practiced in commercial production, the overall yield is not very high, less than 80%.
Moreover, the process generates a large amount of waste stream that is increasingly difficult to dispose of.
Therefore, the problems encountered in the production of taurine from the ethylene oxide process arise from the ammonolysis of sodium isethionate and from the separation of taurine from sodium sulfate.
This process is complicated and requires the use of large quantity of acid and base to regenerate the ion exchange resins in each production cycle.
However, the waste mother liquor still contains taurine, sodium sulfate, and other unspecified organic impurities.

Method used

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  • Cyclic process for the production of taurine from alkali isethionate
  • Cyclic process for the production of taurine from alkali isethionate
  • Cyclic process for the production of taurine from alkali isethionate

Examples

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example 1

[0048]This example relates to the preparation of sodium ditaurinate and its reaction with aqueous ammonia under ammonolysis reaction conditions.

[0049]Into a 1 L flask, equipped a refluxing condenser, is added 31.5 g (0.30 mole) of diethanolamine and 300 mL of dichloroethane, then 51.0 mL of thionyl chloride. Solid suspension formed immediately after the addition of thionyl chloride and then dissolved upon warming to 50° C. During refluxing, the solid suspension is dissolved and then the crystalline solid appears. The crystalline suspension is refluxed while being stirred for 3 hrs. The reaction is quenched by adding 20 mL of methanol and the solvents are removed under vacuum. A white crystalline material, bis(2-chloroethyl)amine hydrochloride, weighted 53.0 g, is obtained in a quantitative yield.

[0050]To the flask is added 500 mL of deionized water, 100 g of sodium sulfite. The solution is stirred at a temperature first at 50-60° C. for 3 hrs, then at 95° C. for 4 hrs. HPLC and LC-M...

example 2

[0055]This example relates to the preparation of sodium tritaurinate and its reaction with aqueous ammonia under ammonolysis reaction conditions.

[0056]Into a 1 L flask, equipped with a refluxing condenser, is added 29.8 g (0.20 mole) of triethanolamine, 300 mL of dichloroethane, then 51.0 mL of thionyl chloride. The mixture is heated to reflux for 4 hrs. The reaction is quenched by adding 20 mL of methanol. Removal of solvent gives a white crystalline mass of tris(2-chloroethylamine) hydrochloride in quantitative yield.

[0057]To the flask is added 500 mL of deionized water, 100 g of sodium sulfite. An oil phase is separated first. After heating at 60° C. for 2 hrs and 98° C. for 5 hrs, the oil phase disappears and a clear solution is obtained. HPLC and LC-MS shows complete conversion of the starting material to the desired sodium tritaurinate.

[0058]The crude reaction solution is transferred to a 2 L autoclave, to which 26 g of sodium hydroxide and 600 mL of 25% aqueous ammonia are ad...

example 3

[0060]This example demonstrates the conversion of sodium ditaurinate and sodium tritaurinate in the recrystallization mother liquor to sodium taurinate.

[0061]To 200 mL of the mother liquor from 2nd cooling crystallization stage, composed of sodium ditaurinate (25% by wt), sodium tritaurinate (3% by wt), taurine (5% by wt), and sodium sulfate (6% by wt), is added 15 g of sodium hydroxide, 500 mL of 25% aqueous ammonia. The solution is heated in a 2 L autoclave at 220° C. for 2 hrs to carry out the ammonolysis reaction.

[0062]HPLC and LC-MS analysis shows that the reaction solution is comprised of the following taurinates: sodium taurinate (76%), sodium ditaurinate (21%), and sodium tritaurinate (3%) on the molar basis.

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Abstract

A cyclic process is disclosed for the production of taurine from alkali isethionate in a high overall yield by continuously converting the byproducts of the ammonolysis reaction, sodium ditaurinate and sodium tritaurinate, to sodium taurinate. Sodium sulfate and residual taurine in the crystallization mother liquor are efficiently separated by converting taurine into a highly soluble form of sodium taurinate or ammonium taurinate while selectively crystallizing sodium sulfate.

Description

CROSS REFERENCE TO RELATED APPLICATIONS[0001]This application is a continuation-in-part of co-pending applicationU.S. Ser. No. 14 / 120,046, filed on Apr. 18, 2014, now U.S. Pat. No. 9,428,450, issued on Aug. 30, 2016.TECHNICAL FIELD[0002]The present invention relates to a cyclic process for the production of taurine from alkali isethionate and from alkali vinyl sulfonate in a high overall yield, i.e., greater than 90%, in particular, greater than 95%, by continuously converting the byproducts of the ammonolysis reaction, alkali ditaurinate and alkali tritaurinate, to alkali taurinate.BACKGROUND OF THE INVENTION[0003]Taurine can be referred to as 2-aminoethanesulfonic acid and is one of the amino sulfonic acids found in the tissues of many animals. Taurine is an extremely useful compound because it has such pharmacological effects as detoxification effect, fatigue-relieving effect and nourishing and tonifying effect. As a result, taurine finds wide applications as an essential ingredi...

Claims

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Application Information

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Patent Type & Authority Patents(United States)
IPC IPC(8): C07C303/32C07C303/02C07C303/44
CPCC07C303/32C07C303/02C07C303/44C07C309/14
Inventor HU, SONGZHOU
Owner VITAWORKS IP LLC
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