IP Library Granted Patent US 8,877,989
Granted Patent B2
US 8,877,989 · App. 13/188,884 · Granted Nov 4, 2014

Dehydration process of hydrofluorocarbon or hydrochlorofluorocarbon and production method of 1,3,3,3-tetrafluoropropene using the dehydration process

Inventors: Yoshio Nishiguchi (Iruma-gun, JP); Yasuo Hibino (Shiki, JP)
Assignee: Central Glass Company, Limited
C07C17/38C07C17/25C07C17/383C07C17/206C07C17/21
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,877,989
App. No.
13/188,884
Granted
Nov 4, 2014
Kind
B2
Abstract

A process for dehydrating a hydrofluorocarbon or hydrochlorofluorocarbon, which can be done by simple equipment, and a continuous process of producing 1,3,3,3-tetrafluoropropene using the dehydration process. The dehydration process includes cooling the hydrofluorocarbon or hydrochlorofluorocarbon in gaseous form containing water with a heat exchanger, thereby condensing and liquefying the hydrofluorocarbon or hydrochlorofluorocarbon while freezing and solidifying the water. The 1,3,3,3-tetrafluoropropene production method includes a first step for fluorinating 1-chloro-3,3,3-trifluoropropene with hydrogen fluoride to obtain a mixture of 1,3,3,3-tetrafluoropropene, unreacted 1-chloro-3,3,3-trifluoropropene, hydrogen fluoride, hydrogen chloride and by-products, or dehydrofluorinating 1,1,1,3,3-pentafluoropropane to obtain a mixture of 1,3,3,3-tetrafluoropropene, unreacted 1,1,1,3,3-pentafluoropropane and by-products, a second step for removing acidic components, a third step for dehydrating the 1,3,3,3-tetrafluoropropene by the above dehydration process, and a fourth step for purifying the 1,3,3,3-tetrafluoropropene by distillation.

Claims (18)

1. A dehydration process of 1,3,3,3-tetrafluoropropene, comprising:

cooling the 1,3,3,3-tetrafluoropropene in gaseous form containing at least water by an indirect heat exchanger of either double-tube type, multi-cylinder type, cylindrical coil type or cylindrical jacketed type, thereby condensing and liquefying the 1,3,3,3-tetrafluoropropene while freezing and solidifying the water onto a heat transfer surface of the indirect heat exchanger.

2. The dehydration process according to claim 1 , further comprising forming the 1,3,3,3-tetrafluoropropene in gaseous form containing at least water by fluorination of 1-chloro-3,3,3-trifluoropropene with hydrogen fluoride and then subjecting the 1,3,3,3-tetrafluoropropene to washing.

3. The dehydration process according to claim 2 , wherein the 1,3,3,3-tetrafluoropropene contains at least a cis-isomer or a trans-isomer, or a mixture of cis- and trans-isomers, of the 1-chloro-3,3,3-trifluoropropene.

4. The dehydration process according to claim 1 , further comprising forming the 1,3,3,3-tetrafluoropropene in gaseous form containing at least water by dehydrofluorination of 1,1,1,3,3-pentafluoropropane and then subjecting the 1,3,3,3-tetrafluoropropene to washing to remove impurities contained in the 1,3,3,3-tetrafluoropropene.

5. The dehydration process according to claim 4 , wherein the 1,3,3,3-tetrafluoropropene contains at least the 1,1,1,3,3-pentafluoropropane as an impurity.

6. The dehydration process according to claim 1 , wherein the 1,3,3,3-tetrafluoropropene is in the form of a cis-isomer or a trans-isomer or a mixture of cis- and trans-isomers thereof.

7. A production method of 1,3,3,3-tetrafluoropropene, comprising:

a dehydration step of dehydrating 1,3,3,3-tetrafluoropropene by the dehydration process according to claim 1 ; and

a distillation purification step of distillating and purifying the dehydrated 1,3,3,3-tetrafluoropropene containing impurities.

8. The production method according to claim 7 , further comprising:

a synthesis step for fluorinating 1-chloro-3,3,3-trifluoropropene with hydrogen fluoride to obtain a mixture of the 1,3,3,3-tetrafluoropropene, unreacted 1-chloro-3,3,3-trifluoropropene, hydrogen fluoride, hydrogen chloride and by-products; and

an acid removal step for removing the hydrogen fluoride and hydrogen chloride from the mixture.

9. The production method according to claim 8 , wherein, in the acid removal step, the hydrogen fluoride is removed by contact of the mixture obtained in the synthesis step with sulfuric acid, water or aqueous basic solution.

10. The production method according to claim 7 , further comprising:

a synthesis step for dehydrofluorinating 1,1,1,3,3-pentafluoropropane to obtain a mixture of the 1,3,3,3-tetrafluoropropene, unreacted 1,1,1,3,3-pentafluoropropane and by-products; and

an acid removal step for removing hydrogen fluoride from the mixture.

11. The production method according to claim 10 , wherein, in the acid removal step, the hydrogen fluoride is removed by contact of the mixture obtained in the synthesis step with sulfuric acid, water or aqueous basic solution.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 29, 2011
From: NISHIGUCHI, YOSHIO; HIBINO, YASUO
To: CENTRAL GLASS COMPANY, LIMITED
Reel/Frame 026823/0087 →
Priority Claims (2)
JP 2010-205473 · Sep 14, 2010 · national
JP 2011-145451 · Jun 30, 2011 · national
Continuity (1)
Related Publication 20120065435A1 · Mar 15, 2012