IP Library Patent Application 18571837
Patent Application
App. No. 18/571,837

METHOD FOR PRODUCING ALCOHOLS

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Quick Facts
Patent No.
US None
App. No.
18/571,837
Abstract

Provided is a method for producing alcohols by an olefin hydration reaction using a heteropolyacid catalyst, wherein the catalyst can be stably used on a long-term basis. The temperature difference within the catalyst layer in the olefin hydration reaction using a heteropolyacid catalyst is made less than or equal to a certain value. Specifically, in a method for producing alcohols in which a gas-phase hydration reaction is carried out using a solid acid catalyst that supports a heteropolyacid acid or salt thereof and supplying water and C2-C5 olefin to a reactor, the temperature difference within the catalyst layer in the reactor is established at less than or equal to 6° C.

Claims (10)

1 . A method for producing an alcohol comprising continuously supplying a raw material gas containing water and an olefin having 2 to 5 carbon atoms to a reactor having a catalyst layer filled with a solid acid catalyst in which a heteropolyacid or a salt thereof is supported on a carrier, and subjecting them to a hydration reaction in a gas phase using the solid acid catalyst to obtain an alcohol,

wherein the hydration reaction is carried out with the temperature difference in the catalyst layer of 6° C. or less.

2 . The method for producing an alcohol according to claim 1 , wherein the reactor is a multi-tubular reactor.

3 . The method for producing an alcohol according to claim 2 , wherein the solid acid catalyst is filled in tubes of the multi-tubular reactor.

4 . The method for producing an alcohol according to claim 3 , wherein the tubes of the multi-tubular reactor have an inner diameter of 40 mm or less.

5 . The method for producing an alcohol according to claim 1 , wherein liquid phase water is used in the reactor as a coolant.

6 . The method for producing an alcohol according to claim 1 , wherein the superficial linear velocity of the raw material gas in the reactor is 0.1 to 1.0 m/s.

7 . The method for producing an alcohol according to claim 1 , wherein the conversion rate of the olefin having 2 to 5 carbon atoms is 2 to 6%.

8 . The method for producing an alcohol according to claim 1 , wherein the reactor is an adiabatic reactor.

9 . The method for producing an alcohol according to claim 1 , wherein the olefin having 2 to 5 carbon atoms is ethylene and the alcohol is ethanol.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 18, 2025
From: RESONAC CORPORATION
To: CRASUS CHEMICAL INC.
Reel/Frame 072044/0367 →
CHANGE OF ADDRESS Recorded Feb 9, 2024
From: RESONAC CORPORATION
To: RESONAC CORPORATION
Reel/Frame 066547/0677 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 19, 2023
From: INOUE, GEN; KIMURA, TOSHIHIRO; KOYANO, MASAFUMI
To: RESONAC CORPORATION
Reel/Frame 065908/0730 →