IP Library Granted Patent US 7,811,524
Granted Patent B2
US 7,811,524 · App. 11/597,822 · Granted Oct 12, 2010

Reactor, reactor control system, and catalytic gas phase oxidation reaction method

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,811,524
App. No.
11/597,822
Granted
Oct 12, 2010
Kind
B2
Abstract

A multi-tubular reaction apparatus, a control system, and a method are provided for controlling temperature change of a heat medium in the reaction apparatus, and quickly adjusting fluctuation in temperature, to thereby properly control a reaction. In particular, the apparatus and system apply to a catalytic gas-phase oxidation reaction such as in producing (meth)acrylic acid or the like. The reaction apparatus includes a multi-tubular reactor having a plurality of reaction tubes in a shell in which a heat medium circulates, and a heat medium cooling apparatus outside the reactor. The reaction apparatus includes a process for primarily cooling the heat medium taken out outside the shell, a process for secondarily cooling a part of the primarily cooled heat medium, and a line for enabling the secondarily cooled heat medium and the primarily cooled heat medium, which is not secondarily cooled, to circulate in the shell.

Claims (21)

1. A multi-tubular reaction apparatus comprising:

a shell,

a plurality of reaction tubes provided in the shell and filled with a catalyst;

a heat medium that circulates in the shell; and

a cooling apparatus provided outside the shell, the cooling apparatus comprising,

a primary cooler to cool at least a part of the heat medium taken outside the shell;

a secondary cooler to cool at least a part of the primarily cooled heat medium;

a flow control mechanism to divert a first fraction of the heat medium taken outside the shell into the secondary cooler and to by pass a second fraction of the heat medium taken outside the shell around the secondary cooler; and

a return line connected to an output of the primary cooler and an output of the secondary cooler for enabling the secondarily cooled heat medium and a residual part of the primarily cooled heat medium, which is not secondarily cooled, to circulate in the shell.

2. The multi-tubular reaction apparatus according to claim 1 , further comprising:

a reaction apparatus control system to adjust a temperature of the heat medium circulating in the shell by adjusting the flow in the heat medium return line of the secondarily cooled heat medium and the residual part of the primarily cooled heat medium, which is not secondarily cooled, on the basis of a temperature of at least one point selected from a heat medium temperature in the shell and a catalyst temperature.

3. The multi-tubular reaction apparatus according to claim 2 , wherein the flow control mechanism comprises:

a flow control valve provided in a supply line connected from the primary cooler to the secondary cooler for supplying at least a part of the primarily cooled heat medium to the secondary cooler; and

a flow control valve provided in a bypass line connected from the output of the primary cooler to bypass the secondary cooler, wherein the control valves are adjusted in opposite directions in adjusting a temperature of the heat medium circulating in the shell.

4. A catalytic gas-phase oxidation reaction method using the multi-tubular reaction apparatus according to claim 3 , the method comprising:

performing a catalytic gas-phase oxidation reaction by controlling a temperature using the reaction apparatus control system in the multi-tubular reaction apparatus.

5. A system for controlling a reaction apparatus comprising:

a multi-tubular reactor, which further comprises a shell, a plurality of reaction tubes provided in the shell and filled with a catalyst, and a heat medium that circulates in the shell;

at least one cooling apparatus to cool the heat medium, the cooling apparatus provided outside the reactor;

a flow control valve provided in a line for supplying at least a part of the heat medium having been taken out outside the shell to the at least one cooling apparatus to cool the heat medium; and

a flow control valve provided in a line of the heat medium, to bypass the cooling apparatus for the heat medium, wherein the flow control valves are used for adjusting a temperature of the heat medium circulating in the shell.

Assignments (3)
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, 2007
From: KANAMARU, TAKASHI; YADA, SHUHEI; JINNO, KIMIKATSU
To: MITSUBISHI CHEMICAL CORPORATION
Reel/Frame 019096/0390 →