IP Library Granted Patent US 11,760,950
Granted Patent B2
US 11,760,950 · App. 16/979,335 · Granted Sep 19, 2023

Gas purification device

Inventors: Kaori Yoshida (Tokyo, JP); Rikio Kan (Hiroshima, JP); Seiji Kakesako (Hiroshima, JP)
Assignee: Mitsubishi Heavy Industries Engineering, Ltd.
C10K1/34B01J19/0013C10K1/004C10K1/006C10K1/101B01J2219/00058B01J2219/00164
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Quick Facts
Patent No.
US 11,760,950
App. No.
16/979,335
Granted
Sep 19, 2023
Kind
B2
Abstract

A gas purification device includes: a converter packed with a catalyst for hydrolyzing both carbonyl sulfide and hydrogen cyanide; an upstream heat exchanger for heat exchange between a gas to be introduced into the converter and a cooling fluid for cooling the gas; a reaction-temperature estimation member for estimating a reaction temperature inside the converter; and a flow-rate adjustment member for adjusting a flow rate of the cooling fluid flowing into the upstream heat exchanger based on an estimated value of the reaction-temperature estimation member to control the reaction temperature.

Claims (22)

1. A gas purification device comprising:

a converter packed with a catalyst for hydrolyzing both carbonyl sulfide and hydrogen cyanide;

an upstream heat exchanger for heat exchange between a gas to be introduced into the converter and a cooling fluid for cooling the gas;

a reaction-temperature estimation member for estimating a reaction temperature inside the converter; and

a flow-rate adjustment member for adjusting a flow rate of the cooling fluid flowing into the upstream heat exchanger based on an estimated value of the reaction-temperature estimation member to control the reaction temperature,

wherein, if a concentration of one of carbonyl sulfide or hydrogen cyanide in the gas increases, the flow-rate adjustment member controls the reaction temperature so as to accelerate hydrolysis reaction of the one of carbonyl sulfide or hydrogen cyanide in the gas having the increased concentration.

2. The gas purification device according to claim 1 ,

wherein the reaction-temperature estimation member is a temperature sensor disposed between the upstream heat exchanger and the converter and configured to detect a temperature of the gas flowing into the converter.

3. The gas purification device according to claim 1 , further comprising:

an analysis device disposed upstream of the converter and configured to analyze a concentration of carbonyl sulfide and a concentration of hydrogen cyanide in the gas; and

a setting-temperature-range determination unit configured to determine a setting temperature range of the reaction temperature based on an analysis result of the analysis device,

wherein the flow-rate adjustment member is configured to adjust the flow rate of the cooling fluid flowing into the upstream heat exchanger such that the estimated value of the reaction-temperature estimation member is within the setting temperature range.

4. The gas purification device according to claim 1 , further comprising:

a hydrogen-sulfide removal device configured to remove hydrogen sulfide produced by hydrolysis of carbonyl sulfide from the gas flowing out of the converter to produce a purified gas; and

a downstream heat exchanger for heat exchange between the gas flowing out of the converter and the purified gas flowing out of the hydrogen-sulfide removal device,

wherein the cooling fluid is the purified gas that has exchanged heat with the gas flowing out of the converter in the downstream heat exchanger.

5. The gas purification device according to claim 1 , further comprising a supply source of steam having a lower temperature than the gas to be introduced into the converter,

wherein the cooling fluid is the steam supplied from the supply source.

6. The gas purification device according to claim 5 ,

wherein the supply source is a steam turbine.

7. The gas purification device according to claim 1 ,

wherein the gas to be introduced into the converter is a syngas obtained by gasification of coal.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 17, 2023
From: MHI ENGINEERING, LTD.
To: MITSUBISHI HEAVY INDUSTRIES, LTD.
Reel/Frame 065245/0620 →
CHANGE OF NAME Recorded Oct 17, 2023
From: MITSUBISHI HEAVY INDUSTRIES ENGINEERING, LTD.
To: MHI ENGINEERING, LTD.
Reel/Frame 065245/0643 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 10, 2020
From: YOSHIDA, KAORI; KAN, RIKIO; KAKESAKO, SEIJI
To: MITSUBISHI HEAVY INDUSTRIES ENGINEERING, LTD.
Reel/Frame 053732/0463 →
Priority Claims (1)
JP 2018-046161 · Mar 14, 2018 · national
Continuity (1)
Related Publication 20210002569A1 · Jan 7, 2021