CN86102646A - Catalysts for the production of carbon dioxide - Google Patents
Catalysts for the production of carbon dioxide Download PDFInfo
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- CN86102646A CN86102646A CN 86102646 CN86102646A CN86102646A CN 86102646 A CN86102646 A CN 86102646A CN 86102646 CN86102646 CN 86102646 CN 86102646 A CN86102646 A CN 86102646A CN 86102646 A CN86102646 A CN 86102646A
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- sodium carbonate
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- carbonate solution
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Abstract
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本发明是一种活化碳酸钠溶液富集和生产Co2的复合催化剂。The invention is a composite catalyst for enriching and producing Co2 by activating sodium carbonate solution.
国外生产Co2的方法是用碳酸钾溶液吸收原料气体中的Co2气体,碳酸钾价格高,且需要高压(27kg/cm2G)下进行,此生产方法设备复杂,成本高。国内生产Co2的方法是用碳酸钠溶液吸收原料气体中的Co2,虽然碳酸钠价格较碳酸钾低廉,但因碳酸钠活性不够,吸收Co2效果不理想。The method of producing Co 2 in foreign countries is to use potassium carbonate solution to absorb Co 2 gas in the raw gas. The price of potassium carbonate is high, and it needs to be carried out under high pressure (27kg/cm 2 G). This production method has complicated equipment and high cost. The method of domestic production of Co 2 is to use sodium carbonate solution to absorb Co 2 in the raw gas. Although the price of sodium carbonate is lower than that of potassium carbonate, the effect of absorbing Co 2 is not ideal due to the insufficient activity of sodium carbonate.
本发明之复合催化剂可以活化碳酸钠溶液,以达到更好地吸收Co2气体的目的。The composite catalyst of the present invention can activate the sodium carbonate solution to achieve the purpose of better absorbing Co2 gas.
本发明的详细内容如下:The details of the present invention are as follows:
复合催化剂的配方为乙醇胺类:即35-45%的一乙醇胺+25-28.5%二乙醇胺+15.9-18%三乙醇胺,另加2.5-3.5%的硼砂及3-7%的氨基乙酸。将0.5-2%复合催化剂加在浓度7-12%的碳酸钠溶液中。用这种溶液处理净化原料气体(Co2在7-30%之间均可),就可以把原料气体中的Co2脱至1%以下。The formula of the composite catalyst is ethanolamine: 35-45% monoethanolamine + 25-28.5% diethanolamine + 15.9-18% triethanolamine, plus 2.5-3.5% borax and 3-7% glycine. Add 0.5-2% composite catalyst to 7-12% sodium carbonate solution. Use this solution to treat and purify the raw gas (Co 2 can be between 7-30%), and the Co 2 in the raw gas can be removed to less than 1%.
在同样的负荷条件,所需的填料面积比单纯用碳酸钠水溶液吸收Co2少一倍以上,而解析速度可提高二倍以上,节能达70%与国外生产Co2方法相比,可简化设备。根据我国传统生产Co2的具体情况,不需要更换新设备,只需在价格低廉的碳酸钠溶液中加入本发明之复合催化剂即可达到生产成本低,质量高的Co2。使用该复合催化剂还可以根据市场对Co2的需求量调节Co2的生产量,如需求大量Co2时,可以在碳酸钠溶液中加该催化剂可使Co2生产速度加快,在市场对Co2需求量少时,可不加催化剂维持少量生产即可。Under the same load conditions, the required packing area is more than twice that of simply using sodium carbonate aqueous solution to absorb Co2 , while the resolution speed can be increased by more than two times, and the energy saving can reach 70%. Compared with foreign methods of producing Co2 , the equipment can be simplified . According to the specific situation of traditional production of Co 2 in our country, there is no need to replace new equipment, just add the composite catalyst of the present invention to the cheap sodium carbonate solution to achieve low production cost and high quality Co 2 . The use of this composite catalyst can also adjust the production capacity of Co according to the demand of the market for Co 2 . When a large amount of Co is required, the catalyst can be added to the sodium carbonate solution to speed up the production of Co 2 . When the demand is small, a small amount of production can be maintained without adding a catalyst.
复合催化剂效果实验。Composite catalyst effect experiment.
试验条件:将钢瓶Co2气体经净化后进入带搅拌的槽式反应器,以80转/分转速在55-70℃之间吸收,所得吸收速度及解析速度比较如下:Test conditions: Purify the Co2 gas in the steel cylinder and enter it into the tank reactor with stirring, and absorb it at 55-70°C at a speed of 80 rpm. The comparison of the obtained absorption speed and resolution speed is as follows:
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 86102646 CN86102646A (en) | 1986-04-11 | 1986-04-11 | Catalysts for the production of carbon dioxide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 86102646 CN86102646A (en) | 1986-04-11 | 1986-04-11 | Catalysts for the production of carbon dioxide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN86102646A true CN86102646A (en) | 1987-10-21 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 86102646 Pending CN86102646A (en) | 1986-04-11 | 1986-04-11 | Catalysts for the production of carbon dioxide |
Country Status (1)
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| CN (1) | CN86102646A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1069222C (en) * | 1994-12-15 | 2001-08-08 | 关西电力株式会社 | Process for removing carbon dioxide and nitrogen oxides from combustion gases |
| CN102000486A (en) * | 2010-10-18 | 2011-04-06 | 武汉凯迪电力股份有限公司 | Method for catching carbon dioxide in flue gas by active sodium carbonate and apparatus thereof |
-
1986
- 1986-04-11 CN CN 86102646 patent/CN86102646A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1069222C (en) * | 1994-12-15 | 2001-08-08 | 关西电力株式会社 | Process for removing carbon dioxide and nitrogen oxides from combustion gases |
| CN102000486A (en) * | 2010-10-18 | 2011-04-06 | 武汉凯迪电力股份有限公司 | Method for catching carbon dioxide in flue gas by active sodium carbonate and apparatus thereof |
| CN102000486B (en) * | 2010-10-18 | 2012-11-21 | 武汉凯迪电力股份有限公司 | Method for catching carbon dioxide in flue gas by active sodium carbonate and apparatus thereof |
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