IP Library Granted Patent US 8,394,999
Granted Patent B2
US 8,394,999 · App. 13/417,696 · Granted Mar 12, 2013

Process for converting glycerin into propylene glycol

Inventors: Zhongyi Ding (Katy, TX); Joseph Chiu (Katy, TX); Weihua Jin (Katy, TX)
Assignee: GTC Technology US LLC
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Quick Facts
Patent No.
US 8,394,999
App. No.
13/417,696
Granted
Mar 12, 2013
Kind
B2
Abstract

A process to convert glycerin into propylene glycol and purifying the produced propylene glycol is described. The glycerin-based propylene glycol production requires only one process step compared to petroleum/natural gas-based propylene glycol production requires multiple process steps, and thus represents a cost savings.

Claims (17)

1. A process for converting glycerin into propylene glycol comprising the steps of:

preheating a feed mixture comprising glycerin, hydrogen and methanol in a reactant heater;

passing the heated feed mixture to a reactor;

separating the reactor effluent into a vapor phase stream and a liquid phase stream;

condensing the vapor phase stream into a condensed liquid;

recycling the condensed liquid to the reactor; and

distilling the liquid phase stream to obtain purified propylene glycol.

2. The process according to claim 1 , wherein the reactor is a fixed bed reactor.

3. The process according to claim 1 , wherein the reactor is operated at a temperature of 150° C.-240° C.

4. The process according to claim 1 , wherein the reactor is operated at a pressure of 20-80 atmospheres.

5. The process according to claim 1 , further comprising hydrogenating the heated feed mixture in the reactor.

6. The process according to claim 5 , wherein the hydrogenating is carried out by a supported catalyst in the fixed bed reactor.

7. The process according to claim 6 , wherein the supported catalyst is a metal or metal oxide catalyst.

8. The process according to claim 7 , wherein the supported catalyst comprises copper.

9. The process according to claim 1 , further comprising mixing the condensed liquid with a glycerin feed.

10. The process according to claim 1 , wherein the liquid phase stream is depressurized and cooled prior to distilling.

11. The process according to claim 1 , wherein the liquid phase stream is distilled in multiple distillation columns.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 26, 2021
From: SULZER GTC TECHNOLOGY US INC.
To: SULZER MANAGEMENT AG
Reel/Frame 056046/0676 →
CHANGE OF NAME Recorded Mar 15, 2021
From: GTC TECHNOLOGY US, LLC
To: SULZER GTC TECHNOLOGY US INC.
Reel/Frame 055934/0098 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 23, 2012
From: DING, ZHONGYI; CHIU, JOSEPH; JIN, WEIHUA
To: GTC TECHNOLOGY US LLC
Reel/Frame 028259/0944 →
Continuity (2)
Provisional Application 61451246 · Mar 10, 2011
Related Publication 20120232312A1 · Sep 13, 2012