IP Library Granted Patent US 10,329,229
Granted Patent B2
US 10,329,229 · App. 15/473,732 · Granted Jun 25, 2019

Method for producing high-concentration alcohol

Inventors: Kazuhide Maeda (Tokyo, JP); Koichi Yamazaki (Mie, JP); Hiroyuki Kakiuchi (Tokyo, JP); Takeshi Tahara (Tokyo, JP); Takahiko Takewaki (Kanagawa, JP)
Assignees: MITSUBISHI CHEMICAL CORPORATION; Mitsubishi Chemical Engineering Corporation
C07C29/76B01D3/005B01D3/145B01D17/0202B01D61/362B01D67/0051B01D71/028B01D2311/04B01D2323/12
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Quick Facts
Patent No.
US 10,329,229
App. No.
15/473,732
Granted
Jun 25, 2019
Kind
B2
Abstract

The present invention aims at providing a method for producing a high-concentration alcohol from a water-alcohol mixture, in which the overall process is efficient and the present invention relates to a production method of a high-concentration alcohol, including a water adsorption step of adsorbing water of a water-alcohol mixture on an adsorption column to obtain a first concentrated alcohol, a water desorption step of introducing an alcohol to obtain a hydrous alcohol, and a membrane separation step of introducing the hydrous alcohol into a membrane separation unit provided with a membrane composite containing zeolite having an SiO 2 /Al 2 O 3 molar ratio of 5 to 15 to obtain a second concentrated alcohol.

Claims (14)

1. A method of producing a high-concentration alcohol which is methanol or ethanol, with an adsorption column and a membrane separation unit,

the method comprising:

(A) introducing a water-alcohol mixture into the adsorption column to adsorb water on the adsorption column and obtain a first concentrated alcohol,

(B) introducing the first concentrated alcohol obtained in (A) into the adsorption column to desorb the water adsorbed and obtain a hydrous alcohol, and

(C) after (B), introducing the hydrous alcohol into a membrane separation unit provided with a zeolite membrane composite containing zeolite having an SiO 2 /Al 2 O 3 molar ratio of 5 to 15 to obtain a second concentrated alcohol.

2. The method according to claim 1 , wherein the zeolite is zeolite having a framework density of 10.0 to 18.0 T/1000 Å.

3. The method according to claim 1 , wherein the zeolite is CHA-type zeolite.

4. The method according to claim 1 , wherein the water-alcohol mixture is a distillate obtained at the top of a rectification column before (A) and (B).

5. The method according to claim 1 , wherein a plurality of adsorption columns are present.

6. The method according to claim 1 , wherein the second concentrated alcohol obtained is reintroduced in an adsorption column in (A).

7. The method according to claim 1 , wherein the alcohol is ethanol and the water-alcohol mixture is obtained by alcohol fermentation with fermentative bacteria.

8. The method according to claim 1 , wherein the water-alcohol mixture further comprises an acid.

9. The method according to claim 1 , wherein the-membrane separation is performed by pervaporation.

10. The method according to claim 1 , wherein the membrane separation is performed by vapor permeation.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 12, 2021
From: MITSUBISHI CHEMICAL ENGINEERING CORPORATION
To: MITSUBISHI CHEMICAL CORPORATION
Reel/Frame 055247/0456 →
CHANGE OF NAME Recorded Sep 5, 2017
From: MITSUBISHI RAYON CO., LTD.
To: MITSUBISHI CHEMICAL CORPORATION
Reel/Frame 043750/0834 →
MERGER Recorded Sep 4, 2017
From: MITSUBISHI CHEMICAL CORPORATION
To: MITSUBISHI RAYON CO., LTD.
Reel/Frame 043750/0207 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 30, 2017
From: MAEDA, KAZUHIDE; YAMAZAKI, KOICHI; KAKIUCHI, HIROYUKI; TAHARA, TAKESHI; TAKEWAKI, TAKAHIKO
To: MITSUBISHI CHEMICAL CORPORATION; MITSUBISHI CHEMICAL ENGINEERING CORPORATION
Reel/Frame 041793/0340 →
Priority Claims (1)
JP 2014-221970 · Oct 30, 2014 · national
Continuity (2)
Continuation PCTJP2015068739 · Jun 29, 2015
Related Publication 20170204030A1 · Jul 20, 2017