IP Library Patent Application 18571875
Patent Application
App. No. 18/571,875

METHOD FOR PRODUCING ALCOHOL

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Quick Facts
Patent No.
US None
App. No.
18/571,875
Abstract

Provided is a method for producing an alcohol through an olefin hydration reaction using a heteropolyacid catalyst, the method enabling the catalyst to be stably used over a long period. In the olefin hydration reaction, in which the heteropolyacid catalyst is used, the pressure loss during the period of passing a feed-material gas through a catalyst layer is regulated to a certain value or less. Specifically, the method for producing an alcohol comprises using a solid-acid catalyst including a supported heteropolyacid or salt thereof, supplying water and a 2C-5C olefin to a reactor, and hydrating the olefin in a gas phase, wherein the pressure loss during the period of passing the feed-material gas through a layer of the catalyst is regulated to 350 kPa or less.

Claims (11)

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 pressure loss when the raw material gas passes through the catalyst layer is 350 kPa 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 the superficial linear velocity of the raw material gas in the reactor is 0.1 to 1.0 m/s, and the gas space velocity of the raw material gas in the reactor is 500 to 15,000/hr.

6 . 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%.

7 . The method for producing an alcohol according to claim 1 , wherein the partial pressure of water in the raw material gas is 0.4 to 0.6 MPa.

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

9 . The method for producing an alcohol according to claim 1 , wherein the heteropolyacid is at least one selected from the group consisting of silicotungstic acid, phosphotungstic acid, phosphomolybdic acid, silicomolybdic acid, silicovanadotungstic acid, phosphovanadotungstic acid, and phosphovanadomolybdic acid.

10 . 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: KOYANO, MASAFUMI; INOUE, GEN; KIMURA, TOSHIHIRO
To: RESONAC CORPORATION
Reel/Frame 065911/0192 →