IP Library Granted Patent US 9,598,357
Granted Patent B1
US 9,598,357 · App. 14/998,888 · Granted Mar 21, 2017

Process for producing taurine from alkali taurinates

Inventor: Songzhou Hu (Princeton, NJ)
Assignee: VITAWORKS IP, LLC
C07C303/22B01J27/02B01J27/053B01J27/055B01J27/08B01J27/10B01J27/1806B01J27/232B01J27/25B01J31/04C07C303/44B01J2231/005B01J2531/002
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Quick Facts
Patent No.
US 9,598,357
App. No.
14/998,888
Granted
Mar 21, 2017
Kind
B1
Abstract

The present invention discloses a process and catalysts for producing taurine by catalytic ammonolysis of alkali ditaurinate, alkali tritaurinate, and their mixture. Useful catalysts are the ammonium and alkali salts of sulfate, bisulfate, sulfite, bisulfite, carbonate, bicarbonate, nitrate, phosphate, and organic carboxylic acids.

Claims (14)

1. A process for producing taurine from alkali ditaurinate, alkali tritaurinate, or their mixture, comprising,

(a) adding one or a combination of two or more catalysts and an excess amount of ammonia to a solution of alkali ditaurinate, alkali tritaurinate, or their mixture;

(b) subjecting the solution of (a) to ammonolysis reaction;

(c) removing excess ammonia and neutralizing with an acid to obtain a crystalline suspension of taurine; and

(d) recovering taurine by solid-liquid separation.

2. The process according to claim 1 , wherein the catalysts are selected from the group consisting of the ammonium and alkali salts of hydroxide, sulfate, bisulfate, carbonate, bicarbonate, sulfite, bisulfate, phosphate, nitrate, and organic carboxylic acids.

3. The process according to claim 1 , wherein the amount of catalyst in molar ratio relative to ditaurine, tritaurine, or their mixture is from 0.01 to 10.

4. The process according to claim 2 , wherein the alkali are selected from the group consisting of lithium, sodium, potassium, and cesium.

5. The process according to claim 2 , wherein the organic carboxylic acids are selected from the group consisting of C 1 -C 12 monocarboxylic acid, dibasic carboxylic acid, aromatic acid, and hydroxy carboxylic acids.

6. The process according to claim 5 , wherein the organic carboxylic acids are selected from the group consisting of formic acid, acetic acid, propionic acid, butyric acid, glycolic acid, malic acid, tartaric acid, oxalic acid, succinic acid, adipic acid, citric acid, and benzoic acid.

7. The process according to claim 1 , wherein the acid is selected from the group consisting of hydrochloric acid, hydrobromic acid, sulfuric acid, nitric acid, and organic carboxylic acids.

8. The process according to claim 1 , wherein the ammonolysis reaction is carried out at a temperature from 160° C. to 260° C. under the pressure from autogenous to 260 bars.

9. The process of claim 1 further comprising after step (d):

(e) returning the mother liquor to (a) for further ammonolysis.

Assignments (3)
CORRECTIVE ASSIGNMENT TO CORRECT THE CORRESPONDENCE DATA PREVIOUSLY RECORDED ON REEL 72544 FRAME 405. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Oct 15, 2025
From: VITAWORKS IP, LLC
To: LIBRE HOLDINGS INC.
Reel/Frame 073067/0435 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 13, 2025
From: VITAWORKS IP, LLC
To: LIBRE HOLDINGS INC.
Reel/Frame 072544/0405 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 10, 2016
From: HU, SONGZHOU
To: VITAWORKS IP, LLC
Reel/Frame 040276/0272 →