Method for supplying hydrogen-containing reducing gas to shaft part of blast furnace
US-10961596-B2 · Mar 30, 2021 · US
US10106863B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10106863-B2 |
| Application number | US-201515110073-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 6, 2015 |
| Priority date | Jan 7, 2014 |
| Publication date | Oct 23, 2018 |
| Grant date | Oct 23, 2018 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
A method for operation of a blast furnace able to greatly reduce the CO 2 emission and enabling stable production of pig iron over a long period of time in a commercial blast furnace, that is, a method for operation of a blast furnace in which iron ore and coke are charged from a furnace top and is blown in pulverized coal from a usual tuyere, comprising blowing in a gas containing at least one of hydrogen and hydrocarbon from the usual tuyere together with the pulverized coal and blowing a gas comprised of a top gas of the blast furnace from which carbon dioxide and steam is removed from a shaft tuyere into the blast furnace.
Opening claim text (preview).
The invention claimed is: 1. A method for operation of a blast furnace in which iron ore and coke are charged from a furnace top and pulverized coal is injected from a usual tuyere provided at a lower stage of the furnace at the side below a shaft tuyere, comprising blowing a blast containing at least one of hydrogen and hydrocarbon from said usual tuyere together with said pulverized coal, blowing a gas comprised of a first part of a top gas of the blast furnace from which carbon dioxide and steam are removed from the shaft tuyere into the blast furnace, blowing a second part of said top gas from the usual tuyere without heating the second part thereof, and raising an oxygen enrichment of gas blown from the usual tuyere, wherein said blast from the usual tuyere is enriched with oxygen by an oxygen enrichment of 10% not less than and not more than by a Y % shown in the following formula: Y= 0.079×CH 4 +32 wherein CH 4 indicates a vol % of methane in the blast blown in from the usual tuyere, and the vol % of the blast blown in from the usual tuyere is in a range from 0 to 100. 2. The method for operation of a blast furnace according to claim 1 , further comprising blowing a gas comprised of the second part of the top gas of the blast furnace from which carbon dioxide and steam are removed from the usual tuyere into the blast furnace. 3. The method for operation of a blast furnace according to claim 1 , wherein a blowing rate of the blast containing at least one of hydrogen and hydrocarbon is 30 Nm 3 /tHM or more. 4. The method for operation of a blast furnace according to claim 1 , wherein said top gas blown from the shaft tuyere is blown from said shaft tuyere by a blowing rate of 400 Nm 3 /tHM or less at a temperature of 600° C. to 1000° C. 5. The method for operation of a blast furnace according to claim 1 , wherein the blowing rate of the top gas blown from said shaft tuyere is 100 Nm 3 /tHM or more. 6. The method for operation of a blast furnace according to claim 1 , wherein the blast containing at least one of hydrogen and hydrocarbon blown from said usual tuyere contains methane. 7. The method for operation of a blast furnace according to claim 6 , wherein the blast containing methane includes at least one of coke oven gas and natural gas. 8. The method for operation of a blast furnace according to claim 2 , wherein a blowing rate of the blast containing at least one of hydrogen and hydrocarbon is 30 Nm 3 /tHM or more. 9. The method for operation of a blast furnace according to claim 2 , wherein said top gas blown from the shaft tuyere is blown from said shaft tuyere by a blowing rate of 400 Nm 3 /tHM or less at a temperature of 600° C. to 1000° C. 10. The method for operation of a blast furnace according to claim 3 , wherein said top gas blown from the shaft tuyere is blown from said shaft tuyere by a blowing rate of 400 Nm 3 /tHM or less at a temperature of 600° C. to 1000° C. 11. The method for operation of a blast furnace according to claim 2 , wherein the blowing rate of the top gas blown from said shaft tuyere is 100 Nm 3 /tHM or more. 12. The method for operation of a blast furnace according to claim 3 , wherein the blowing rate of the top gas blown from said shaft tuyere is 100 Nm 3 /tHM or more. 13. The method for operation of a blast furnace according to claim 4 , wherein the blowing rate of the top gas blown from said shaft tuyere is 100 Nm 3 /tHM or more. 14. The method for operation of a blast furnace according to claim 2 , wherein the blast containing at least one of hydrogen and hydrocarbon blown from said usual tuyere contains methane.
Chemistry & Metallurgy · mapped topic
Injecting additional fuel or reducing agents · CPC title
using top gas in the blast furnace process · CPC title
by capturing or storing CO2 · CPC title
Details, accessories or equipment specially adapted for furnaces of these types · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.