Gas production apparatus, gas production system, steel production system, chemical manufacturing system, and gas production method with reduced carbon dioxide emission

Patent metadata

Field	Value
Publication number	US-12582941-B2
Application number	US-202017277962-A
Country	US
Kind code	B2
Filing date	Aug 4, 2020
Priority date	Aug 4, 2020
Publication date	Mar 24, 2026
Grant date	Mar 24, 2026

Abstract

A gas production apparatus includes: a separator configured to separate and capture a separated gas including carbon dioxide as a main component from an exhaust gas of exhaust gas equipment; reactors which are downstream of the separator, each of the reactors: (i) containing a reductant configured to contact the separated gas to produce carbon monoxide through a reduction reaction of carbon dioxide; (ii) being configured to separate at least some oxygen atoms split off from carbon dioxide in the reduction reaction; and (iii) having a reducing agent containing a metal oxide configured to reduce carbon dioxide as the reductant; a reducer configured to supply a reducing gas containing a reducing substance configured to reduce the reducing agent oxidized by contact with carbon dioxide; a pressure regulator configured to regulate a pressure of the separated gas; and a flow regulator configured to regulate a flow rate of the separated gas.

First claim

The invention claimed is:

1 . A gas production apparatus, comprising:
a separation and capture section configured to separate and capture a separated gas including carbon dioxide as a main component from an exhaust gas of exhaust gas equipment; a reaction section including reactors which are downstream of the separation and capture section, each of the reactors: (i) containing a reductant configured to contact the separated gas to produce carbon monoxide through a reduction reaction of carbon dioxide; (ii) being configured to separate at least some oxygen atoms split off from carbon dioxide in the reduction reaction; and (iii) having a reducing agent containing a metal oxide configured to reduce carbon dioxide as the reductant; a reducing gas supply section configured to supply a reducing gas containing a reducing substance configured to reduce the reducing agent oxidized by contact with carbon dioxide; a pressure regulating section which is downstream of the reactors and configured to regulate a pressure of the separated gas supplied to each of the reactors; and a flow regulating section which is upstream of the separation and capture section and configured to regulate a flow rate of the separated gas supplied to each of the reactors, wherein: the separation and capture section and the flow regulating section are arranged on only a single line connected to the reaction section; each of the reactors is connected to at least one of the separation and capture section or the reducing gas supply section; and each of the reactors is configured to: (i) switch between the separated gas and the reducing gas to be supplied to each of the reactors; or (ii) transfer the reducing agent between the reactors.

2 . The gas production apparatus according to claim 1 , wherein the separation and capture section is configured to regulate a concentration of the carbon dioxide in the separated gas to be 70% or more by volume of a total of the separated gas.

3 . The gas production apparatus according to claim 1 , wherein the pressure regulating section is configured to regulate the pressure of the separated gas supplied to each of the reactors to be 0 MPaG to 2 MPaG.

4 . The gas production apparatus according to claim 1 , wherein each of the reactors is connected to the separation and capture section and the reducing gas supply section.

5 . A gas production system, comprising:
the gas production apparatus according to claim 1 ; and the exhaust gas equipment, wherein: the exhaust gas equipment includes a furnace, a smokestack configured to release the exhaust gas which contains the carbon dioxide and is emitted from the furnace, and the single line connecting the smokestack to the furnace; and the separation and capture section is connected to the single line and configured to extract the exhaust gas from the exhaust gas equipment.

6 . The gas production system according to claim 5 , wherein:
the exhaust gas equipment further comprises a treater arranged on the single line and configured to treat the exhaust gas; and the gas production apparatus is configured to take the exhaust gas from the single line between the smokestack and the treater.

7 . The gas production system according to claim 6 , wherein the treater includes at least one of a fan, a combustion furnace, a denitrator, or a desulfurizer.

8 . The gas production system according to claim 6 , wherein the treater includes a fan, a combustion furnace, a denitrator, and a desulfurizer.

9 . A steel production system, comprising:
the gas production apparatus according to claim 1 ; and a melting furnace which is downstream of the reactors, wherein: each of the reactors is configured to bring the separated gas into contact with the reductant to convert carbon dioxide into carbon monoxide as a product gas; and the steel production system is configured to supply the product gas containing carbon monoxide to the melting furnace to produce steel.

10 . The steel production system according to claim 9 , wherein a concentration of the carbon monoxide in the product gas is 70% or more by volume of a total of the product gas.

11 . The steel production system according to claim 9 , further comprising a product gas heater configured to heat the product gas before the product gas is supplied to the melting furnace.

12 . The steel production system according to claim 11 , wherein a temperature of the product gas after heating by the product gas heater is between 500° C. and 1300° C.

13 . A chemical manufacturing system, comprising:
the gas production apparatus according to claim 1 ; and a reaction facility which is downstream of the reactors, wherein: each of the reactors is configured to bring the separated gas into contact with the reductant to convert carbon dioxide into carbon monoxide as a product gas; and the chemical manufacturing system is configured to supply the product gas containing carbon monoxide to the reaction facility to produce chemicals.

Assignees

• Sekisui Chemical Co Ltd

Inventors

• Nakama Yuki
• Dasanayake Aluthge Rasika
• Nakamura Masaki

Classifications

• F27D17/20

  Arrangements for treatment or cleaning of waste gases · CPC title

• C10K3/026

  Increasing the carbon monoxide content, e.g. reverse water-gas shift [RWGS] · CPC title

• C21B5/06 Primary

  using top gas in the blast furnace process · CPC title

• B01D2258/025

  from metallurgy plants · CPC title

• B01D53/76

  Gas phase processes, e.g. by using aerosols · CPC title