IP Library Granted Patent US 7,067,695
Granted Patent B2
US 7,067,695 · App. 11/064,020 · Granted Jun 27, 2006

Method of vapor phase catalytic oxidation using multitubular reactor

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Quick Facts
Patent No.
US 7,067,695
App. No.
11/064,020
Granted
Jun 27, 2006
Kind
B2
Abstract

An object of the present invention is to provide a method of vapor phase catalytic oxidation which is capable of: efficiently removing heat of reaction; preventing the formation of hot spots; and efficiently providing a desired product. The invention provides a method of vapor phase catalytic oxidation of a substance to be oxidized with a gas containing molecular oxygen by means of a multitubular reactor, wherein the method comprises: performing a reaction of vapor phase catalytic oxidation under such conditions that a heat transfer coefficient of the heat medium is 1,000 W/(m 2 ·K) or higher.

Claims (4)

1. A method of a vapor phase catalytic oxidation of a substance to be oxidized with a gas containing molecular oxygen by means of a multitubular reactor, the multitubular reactor comprising: a cylindrical reactor shell fitted with a raw material supply port and a product outlet; multiple circular conduits disposed around the cylindrical reactor shell and used to introduce a heat medium into the cylindrical reactor shell or to lead the heat medium out therefrom; a circulation device for connecting the multiple circular conduits to each other; multiple reaction tubes restrained by means of multiple tube plates of the reactor and having a catalyst accommodated therein; and multiple baffles arranged in a longitudinal direction of the reaction tube and used to change a direction of the heat medium introduced into the reactor shell, wherein the method comprises:

performing a reaction of vapor phase catalytic oxidation under such conditions that a heat transfer coefficient of the heat medium is 1,000 W/(m 2 ·K) or higher, and preventing the reaction of vapor phase catalytic oxidation in an area of the reactor having a heat transfer coefficient of the heat medium less than 1,000 W/(m 2 ·K).

2. The method of vapor phase catalytic oxidation according to claim 1 , wherein the method comprises:

oxidizing propylene, propane, or isobutylene with molecular oxygen to produce (meth)acrolein; and/or oxidizing (meth)acrolein with molecular oxygen to produce (meth)acrylic acid.

Assignments (2)
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 →