US2009220410A1PendingUtilityA1
Method for Producing Hydrogen and/or Other Gases from Steel Plant Wastes and Waste Heat
Est. expirySep 30, 2025(expired)· nominal 20-yr term from priority
C01B 3/34Y02P20/129C04B 5/00C21B 2400/024C21B 3/08C10J 3/57C10J 2300/0943Y02P10/20C21B 2400/072C10J 2300/093C22B 7/04C10J 2300/16C10J 2300/0976Y02E60/32C10J 2300/1807C01B 3/06C01B 3/042C01B 32/40Y02P10/25C10J 2300/0946C10J 3/82C21B 2400/08C10J 2300/12C10J 2300/0973C21B 2400/02C01B 3/02Y02E60/36
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Claims
Abstract
A method for producing hydrogen and/or other gases from steel plant wastes and waste heat is disclosed. The method comprises the steps of providing molten waste from steel plant like molten slag in a reactor. The molten slag is contacted with water and/or steam in the presence of a reducing agent to form a stream of hydrogen and/or other gases. The hydrogen and/or other gases can then be extracted from the stream of gases from the reactor.
Claims
exact text as granted — not AI-modified1 - 19 . (canceled)
20 . A method for producing hydrogen and/or other gases from steel plant wastes and waste heat, comprising the steps of:
providing molten slag in a reactor; contacting the molten slag with water and/or steam in the presence of a reducing agent to form a stream of hydrogen and/or other gases; and extracting hydrogen and/or other gases from said stream.
21 . The method of claim 20 , wherein the molten slag is waste from a steel plant.
22 . The method of claim 20 , wherein the molten slag comprises blast furnace slag, desulphurization slag of steelmaking, converter slag of steelmaking, ferrochrome or ferromanganese slag in submerged arc furnace (SAP), or a mixture thereof.
23 . The method of claim 20 , wherein contacting the molten slag with water and/or steam comprises spraying water into the molten slag using a water line with a spray nozzle.
24 . The method of claim 20 , wherein the temperature of the molten slag when contacted with water and/or steam is greater than 1250° C.
25 . The method of claim 20 , wherein contacting the molten slag with water and/or steam comprises injecting steam into the molten slag using a lance.
26 . The method of claim 20 , wherein contacting the molten slag with water and/or steam comprises injecting the reducing agent along with the water and/or steam into the molten slag.
27 . A method for production of a stream of hydrogen and/or carbon monoxide, comprising the steps of:
providing molten slag in a reactor; contacting the molten slag with water and/or steam in the presence of a carbonaceous material to form a stream of hydrogen and/or other gases; and extracting the stream of hydrogen and/or other gases from the reactor.
28 . The method of claim 27 , wherein the molten slag is waste from a steel plant.
29 . The method of claim 27 , wherein the molten slag comprises blast furnace slag, desulphurization slag of steelmaking, converter slag of steelmaking, ferrochrome or ferromanganese slag in submerged arc furnace (SAF), or a mixture thereof.
30 . The method of claim 27 , wherein contacting the molten slag with water and/or steam comprises spraying water into the molten slag using a spray nozzle.
31 . The method of claim 27 , wherein the temperature of the molten slag when contacted with water and/or steam is greater than 1250° C.
32 . The method of claim 27 , wherein contacting the molten slag with water and/or steam comprises injecting steam into the molten slag using a lance.
33 . The method of claim 27 , wherein contacting the molten slag with water and/or steam comprises injecting the carbonaceous material along with water and/or steam into the molten slag.
34 . The method of claim 27 , wherein the carbonaceous material comprises coal coke, steel plant waste, municipal waste and coal mine waste.
35 . The method of claim 27 , wherein the ratio of water to carbonaceous material is between 1:0.1 to 1:1.
36 . The method of claim 27 , wherein a flux is added to the molten slag and carbonaceous material for promoting the formation of hydrogen.
37 . The method of claim 27 , wherein the volume ratio of hydrogen and carbon monoxide produced is from 1:0.2 to 1:1.
38 . The method of claim 27 , wherein the gas stream extracted from the reactor comprises at least 10 volume percent of hydrogen.
39 . The method of claim 27 , wherein the gas stream produced in the reactor comprises not greater than 15 volume percent carbon dioxide.
40 . The method of claim 27 , wherein the gas stream comprises a ratio of hydrogen to carbon monoxide of about 1:1 to 8:1.Join the waitlist — get patent alerts
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