CN1151063C - Purification process of CO2 gas material for carbonation process of preparing strontium carbonate - Google Patents
Purification process of CO2 gas material for carbonation process of preparing strontium carbonate Download PDFInfo
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- CN1151063C CN1151063C CNB021029679A CN02102967A CN1151063C CN 1151063 C CN1151063 C CN 1151063C CN B021029679 A CNB021029679 A CN B021029679A CN 02102967 A CN02102967 A CN 02102967A CN 1151063 C CN1151063 C CN 1151063C
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- gas
- strontium carbonate
- catalyst
- organic sulfur
- raw material
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2
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Abstract
The present invention relates to a method for purifying raw CO2 in the preparation of strontium carbonate by using a carbonizing method, which comprises the steps: after raw CO2 is absorbed by active carbon at normal temperature and normal pressure to remove H2S, an organic sulfur catalyst and iron oxide are utilized to remove organic sulfur, and then a copper catalyst is utilized for deoxidization at 130 to 200 DEG C. Due to the treatment of harmful gases in CO2, the product quality of strontium carbonate can be improved.
Description
The present invention is a divisional application entitled "method for producing strontium carbonate by continuous carbonization", filed on 19/3/1999, with application number 99102632.2.
Technical Field
The invention relates to CO for preparing strontium carbonate by a carbonization method2A gas purification treatment method.
Background
At present, the industrial carbonization method for producing strontium carbonate generally adopts CO such as lime kiln2Gas source as CO2Raw material gas due to CO2The raw material gas contains harmful gases such as sulfur and oxygen, and the total sulfur content is 0.01-0.1g/m3In between, the volume ratio of oxygen is generally between 1.0-0.01%, and untreated sulfur enters the product, thus reducing the product quality. During the carbonization process, due to O2The presence of (a) entails the following side reactions:
thereby generating sulfite to degrade the quality of the product.
Disclosure of Invention
The invention aims to improve the quality of strontium carbonate products by treating harmful gases in raw material gases, and comprises the following steps.
1. Decarbonizing gas or CO from lime kiln gas or synthetic ammonia2CO of gas field gas2Adsorbing and removing H by active carbon at normal temperature and pressure2S;
2. Removing H from the above2Gas after SHydrolyzing and removing organic sulfur by using an organic sulfur catalyst and an iron oxide catalyst as catalysts at normal temperature and under the pressure of 0.6 mPa;
3. deoxidizing the gas obtained in the step 2 at the temperature of 130-200 ℃ by using copper as a catalyst.
The invention is through the reaction of CO2The harmful gas in the raw material gas is treated, so that the treatment caused by the harmful gas can be avoidedThe product quality is reduced due to the existence of harmful gases such as oxygen, sulfur and the like, can stably reach the national high-quality standard, and can also reach the electronic grade standard after adjustment operation.
Drawings
FIG. 1 is a CO of the present invention2A flow chart of a raw material gas desulfurization and deoxidation process.
Detailed Description
The invention is described in detail below with reference to theattached drawing figures:
as shown in FIG. 1, from lime kiln gas or synthetic ammonia decarbonation gas or CO2CO of gas field gas2The raw material gas is sent to a desulfurizing tower 2 by a fan 1, and the active carbon is used for physical adsorption of H2S, the sulfur is pressurized to 0.6mpa by a compressor 3, cooled to normal temperature by a water cooler 4 and then sent to a second desulfurizing tower 5, and organic sulfur is removed by hydrolysis by taking an organic sulfur catalyst and an iron oxide catalyst as catalysts, and the reaction principle is as follows:
the total sulfur content in the gas is less than or equal to 5ppm, and the desulfurization process is carried out at normal temperature. Then the gas is heated to 130-:
In synthetic ammonia decarbonization gas, there is H2In the presence of the catalyst, the oxidation and reduction regeneration of the Cu catalyst are carried out simultaneously, so that the catalyst can be kept from aging. Such as in CO2Absence of H in the gas2When the catalyst activity is reduced, H can be introduced2The gas makes it reduce and regenerate. O can be reduced by the above-mentioned deoxidation2The content is reduced to below 10ppm by volume ratio. And (3) sending the deoxidized gas to a heat exchanger 6, cooling to about 80-100 ℃, and then sending to a carbonization working section of the following strontium carbonate.
Claims (2)
1. CO for preparing strontium carbonate by carbonization method2The raw material gas purification treatment method comprises the following steps:
(1) decarbonizing gas or CO from lime kiln gas or synthetic ammonia2CO of gas field gas2Adsorbing and removing H by active carbon at normal temperature and pressure2S;
(2) Removing H from the above2Hydrolyzing the gas after S at normal temperature and 0.6mpa pressure by using an organic sulfur catalyst and an iron oxide catalyst as catalysts to remove organic sulfur;
(3) deoxidizing the gas obtained in the step 2 at the temperature of 130-200 ℃ by using copper as a catalyst.
2. The method according to claim 1, characterized in that the CO is2The raw material gas is synthetic ammonia decarbonization gas or CO2Gas field gas.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB021029679A CN1151063C (en) | 2002-02-09 | 2002-02-09 | Purification process of CO2 gas material for carbonation process of preparing strontium carbonate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB021029679A CN1151063C (en) | 2002-02-09 | 2002-02-09 | Purification process of CO2 gas material for carbonation process of preparing strontium carbonate |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN99102632A Division CN1106346C (en) | 1999-03-19 | 1999-03-19 | Process for preparing strontium carbonate by continuous carbonifying method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1389396A CN1389396A (en) | 2003-01-08 |
CN1151063C true CN1151063C (en) | 2004-05-26 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB021029679A Expired - Fee Related CN1151063C (en) | 2002-02-09 | 2002-02-09 | Purification process of CO2 gas material for carbonation process of preparing strontium carbonate |
Country Status (1)
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CN (1) | CN1151063C (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN107058861B (en) * | 2017-03-29 | 2019-07-26 | 江苏吉鑫风能科技股份有限公司 | A kind of preparation method of ductile cast iron material, the composition comprising it and wind power casting and wind power casting |
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2002
- 2002-02-09 CN CNB021029679A patent/CN1151063C/en not_active Expired - Fee Related
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Publication number | Publication date |
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CN1389396A (en) | 2003-01-08 |
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