CN112940795A - Iron-based desulfurizer for blast furnace gas and preparation method thereof - Google Patents

Iron-based desulfurizer for blast furnace gas and preparation method thereof Download PDF

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Publication number
CN112940795A
CN112940795A CN202110200350.2A CN202110200350A CN112940795A CN 112940795 A CN112940795 A CN 112940795A CN 202110200350 A CN202110200350 A CN 202110200350A CN 112940795 A CN112940795 A CN 112940795A
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CN
China
Prior art keywords
desulfurizer
solid
blast furnace
furnace gas
iron
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202110200350.2A
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Chinese (zh)
Inventor
李咸伟
刘道清
贺玉成
黄刚
华建明
胡子国
俞勇梅
陈健
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hubei Huatel Purifying Technology Co ltd
Baoshan Iron and Steel Co Ltd
Original Assignee
Hubei Huatel Purifying Technology Co ltd
Baoshan Iron and Steel Co Ltd
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Application filed by Hubei Huatel Purifying Technology Co ltd, Baoshan Iron and Steel Co Ltd filed Critical Hubei Huatel Purifying Technology Co ltd
Priority to CN202110200350.2A priority Critical patent/CN112940795A/en
Publication of CN112940795A publication Critical patent/CN112940795A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00Purifying combustible gases containing carbon monoxide
    • C10K1/002Removal of contaminants
    • C10K1/003Removal of contaminants of acid contaminants, e.g. acid gas removal
    • C10K1/004Sulfur containing contaminants, e.g. hydrogen sulfide
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00Purifying combustible gases containing carbon monoxide
    • C10K1/32Purifying combustible gases containing carbon monoxide with selectively adsorptive solids, e.g. active carbon

Abstract

The invention discloses an iron-based desulfurizer for blast furnace gas, which comprises the following main raw materials: 30-50wt% of ferrous sulfate, 20-30wt% of calcium hydroxide, 10-40wt% of carbide slag, 5-15wt% of fly ash and 5-15wt% of sawdust. The solid reacts in the kneading and forming process to generate a desulfurizer precursor, and then the desulfurizer precursor is naturally oxidized into a finished desulfurizer product. The desulfurizer prepared by the method has high sulfur capacity, working sulfur capacity of 35-45wt%, saturated sulfur capacity of 60-70wt%, simple preparation process, no waste water and waste residue in the production process, low production cost and suitability for large-scale production.

Description

Iron-based desulfurizer for blast furnace gas and preparation method thereof
Technical Field
The invention relates to the technical field of gas purification, in particular to an iron-based desulfurizer for blast furnace gas and a preparation method thereof.
Background
The blast furnace gas generally contains a large amount of COS and H2And (4) S gas. The blast furnace gas is directly combusted or used as chemical raw material gas, sulfide in the blast furnace gas can poison subsequent catalysts, and simultaneously, a large amount of SO can be generated by combustion2The subsequent treatment cost is very high for the standard discharge.
Before the blast furnace gas is combusted or used as a chemical raw material gas, a desulfurization process is additionally arranged, so that the purification cost can be obviously reduced, and equipment and subsequent catalysts are protected. At present, the desulfurization of blast furnace gas generally adopts organic sulfur hydrolytic agent to convert COS into H2S, then using a desulfurizing agent to react H2And (4) S absorption. Blast furnace gas de-H2S generally adopts an active carbon desulfurizer or an iron oxide desulfurizer, and the active carbon desulfurizer has higher price and is not suitable for a production process with large gas quantity of blast furnace gas and huge desulfurizer consumption; the common ferric oxide desulfurizer has low sulfur capacity, generates waste water and waste residue in the production process, and is not suitable for large-scale production and use. Currently, the production and use of iron oxide desulfurizers are severely limited.
Disclosure of Invention
Aiming at the problems in the related art, the invention provides an iron-based desulfurizer for blast furnace gas and a preparation method thereof, which solve the problems of low sulfur capacity, high production cost and waste water and waste residue discharge in the production process of the existing desulfurizer.
In order to achieve the technical purpose, the technical scheme of the invention is as follows:
an iron-based desulfurizer for blast furnace gas comprises the following main raw materials: 30-50wt% of ferrous sulfate, 20-30wt% of calcium hydroxide, 10-40wt% of carbide slag, 5-15wt% of fly ash and 5-15wt% of sawdust.
Further, the raw material of the desulfurizing agent also comprises ammonium bicarbonate solid.
A preparation method of an iron-based desulfurizer for blast furnace gas comprises the following steps:
s1, mixing ferrous sulfate solid, calcium hydroxide powder, carbide slag, fly ash and sawdust according to the mass ratio: (25-50): (20-30): (10-40): (5-15): (5-15), adding the mixture into a reaction tank, and uniformly mixing to obtain a solid mixture a;
s2, dissolving ammonium bicarbonate solid in water to prepare an ammonium bicarbonate solution b with the concentration of 1-5%;
s3, injecting a ammonium bicarbonate solution b into a reaction tank of the solid mixture a, mixing and stirring the solid while injecting the ammonium bicarbonate solution until the solid matter becomes a mud state, continuously mixing and stirring for 2-3 hours, then stopping stirring, and aging for 12-24 hours to obtain a solid mud state matter c;
s4, extruding the aged solid mud-like object c into strips by using a hydraulic press to form a desulfurizer precursor d;
s5, directly drying the desulfurizer precursor d in the sun, and naturally oxidizing for 24-36 hours to obtain a finished desulfurizer product e.
The invention has the beneficial effects that: the main raw material of the iron-based desulfurizer is solid waste, waste is changed into valuable, no waste water and waste residue are discharged in the production process, and the prepared desulfurizer has high working sulfur capacity, low price and simple production process and is suitable for large-scale production.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings needed in the embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art to obtain other drawings without creative efforts.
FIG. 1 is a diagram of a sulfur capacity detecting apparatus for an iron-based desulfurizing agent for blast furnace gas according to the present invention.
In the figure:
1、H2s, storing a gas cylinder; 2. a flow meter; 3. water vapourA saturator; 4. a reactor; 5. a first constant-temperature water bath device; 6. a second constant-temperature water bath device; 7. and a buffer tank.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments that can be derived by one of ordinary skill in the art from the embodiments given herein are intended to be within the scope of the present invention.
An iron-based desulfurizer for blast furnace gas comprises the following main raw materials: 45wt% of ferrous sulfate, 20wt% of calcium hydroxide, 20wt% of carbide slag, 10wt% of fly ash and 5wt% of sawdust.
In this example, the desulfurizing agent feedstock also included 1kg of ammonium bicarbonate solids.
In this example, the ferrous sulfate is derived from titanium dioxide byproduct waste.
In the embodiment, the carbide slag is derived from waste slag generated by hydrolysis of carbide.
The preparation method of the iron-based desulfurizer for blast furnace gas is characterized by comprising the following steps:
s1, mixing ferrous sulfate solid, calcium hydroxide powder, carbide slag, fly ash and sawdust according to a mass ratio of 45: 20: 20: 10: 5, adding the mixture into a reaction tank, and uniformly mixing to obtain a solid mixture a;
s2, dissolving 1kg of ammonium bicarbonate solid in 20kg of water to prepare an ammonium bicarbonate solution b with the concentration of 5%;
s3, injecting a ammonium bicarbonate solution b into a reaction tank of the solid mixture a, mixing and stirring the solid while injecting the ammonium bicarbonate solution until the solid matter becomes a mud state, adding 6kg of the solution b in total, continuing mixing and stirring for 3 hours, stopping stirring, and aging for 24 hours to obtain a solid mud-like substance c;
s4, extruding the aged solid mud-like object c into strips by using a hydraulic press to form a desulfurizer precursor d;
s5, directly drying the desulfurizer precursor d in the sun, and naturally oxidizing for 36 hours to obtain a finished desulfurizer product e.
In this example, the obtained desulfurization agent product e was charged into the fixed bed reactor 4, and its sulfur capacity was measured. Wherein the sulfur capacity is detected according to the sulfur capacity test method of HG/T4354-2012 normal-temperature iron oxide, the detection temperature is 30 ℃, and the airspeed is 500-1000h-1,H2S concentration 3000-2The concentration is 0.2-0.3%.
In this embodiment, the working sulfur capacity of the obtained desulfurizer product e can reach 35-45wt%, and the saturated sulfur capacity can reach 60-70 wt%.
In summary, the invention combines the current blast furnace gas desulfurization process flow in the steel industry to develop a high-efficiency iron-based desulfurizer, which is suitable for the desulfurization of blast furnace gas and other gas components in complex environments, has low production cost and no waste water and waste residue, and is suitable for large-scale production and use.
The present invention is not limited to the above preferred embodiments, and any modifications, equivalent substitutions, improvements, etc. within the spirit and principle of the present invention should be included in the protection scope of the present invention.

Claims (3)

1. An iron-based desulfurizer for blast furnace gas is characterized by comprising the following main raw materials: 30-50wt% of ferrous sulfate, 20-30wt% of calcium hydroxide, 10-40wt% of carbide slag, 5-15wt% of fly ash and 5-15wt% of sawdust.
2. The iron-based desulfurizing agent for blast furnace gas according to claim 1, wherein said desulfurizing agent raw material further comprises ammonium bicarbonate solids.
3. The preparation method of the iron-based desulfurizer for blast furnace gas is characterized by comprising the following steps:
s1, mixing ferrous sulfate solid, calcium hydroxide powder, carbide slag, fly ash and sawdust according to the mass ratio: (25-50): (20-30): (10-40): (5-15): (5-15), adding the mixture into a reaction tank, and uniformly mixing to obtain a solid mixture a;
s2, dissolving ammonium bicarbonate solid in water to prepare an ammonium bicarbonate solution b with the concentration of 1-5%;
s3, injecting a ammonium bicarbonate solution b into a reaction tank of the solid mixture a, mixing and stirring the solid while injecting the ammonium bicarbonate solution until the solid matter becomes a mud state, continuously mixing and stirring for 2-3 hours, then stopping stirring, and aging for 12-24 hours to obtain a solid mud state matter c;
s4, extruding the aged solid mud-like object c into strips by using a hydraulic press to form a desulfurizer precursor d;
s5, directly drying the desulfurizer precursor d in the sun, and naturally oxidizing for 24-36 hours to obtain a finished desulfurizer product e.
CN202110200350.2A 2021-02-23 2021-02-23 Iron-based desulfurizer for blast furnace gas and preparation method thereof Pending CN112940795A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115337896A (en) * 2022-07-22 2022-11-15 西南化工研究设计院有限公司 Dry desulfurizing agent for ultralow emission of sulfonated tail gas and preparation method thereof

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Publication number Priority date Publication date Assignee Title
CA1046734A (en) * 1973-10-05 1979-01-23 Abraham A. Dor Apparatus and method for removing sulfur from sulfur-bearing gases
CN101219320A (en) * 2007-09-20 2008-07-16 湖北蓝焰生态能源有限公司 Method for producing iron oxide desulphurizing agent in normal temperature
CN102010761A (en) * 2009-09-04 2011-04-13 南化集团研究院 Preparation method of normal-temperature ferric oxide desulfurizer
CA2423174C (en) * 2000-09-26 2012-10-23 Bayer Aktiengesellschaft Contact and adsorber granules
CN104058491A (en) * 2014-07-04 2014-09-24 岳阳海达环保科技有限公司 Ferric oxide desulfurizer and preparation method thereof
CN105664706A (en) * 2016-01-19 2016-06-15 北京三聚环保新材料股份有限公司 High-sulfur-capacity low-cost desulfurizing agent and preparation method thereof

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Publication number Priority date Publication date Assignee Title
CA1046734A (en) * 1973-10-05 1979-01-23 Abraham A. Dor Apparatus and method for removing sulfur from sulfur-bearing gases
CA2423174C (en) * 2000-09-26 2012-10-23 Bayer Aktiengesellschaft Contact and adsorber granules
CN101219320A (en) * 2007-09-20 2008-07-16 湖北蓝焰生态能源有限公司 Method for producing iron oxide desulphurizing agent in normal temperature
CN102010761A (en) * 2009-09-04 2011-04-13 南化集团研究院 Preparation method of normal-temperature ferric oxide desulfurizer
CN104058491A (en) * 2014-07-04 2014-09-24 岳阳海达环保科技有限公司 Ferric oxide desulfurizer and preparation method thereof
CN105664706A (en) * 2016-01-19 2016-06-15 北京三聚环保新材料股份有限公司 High-sulfur-capacity low-cost desulfurizing agent and preparation method thereof

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Title
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115337896A (en) * 2022-07-22 2022-11-15 西南化工研究设计院有限公司 Dry desulfurizing agent for ultralow emission of sulfonated tail gas and preparation method thereof
CN115337896B (en) * 2022-07-22 2023-12-01 西南化工研究设计院有限公司 Dry desulfurizing agent for ultralow emission of sulfonated tail gas and preparation method thereof

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