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Process for removing acid gas with low-temperature methanol solution

A technology of acidic gas and low-temperature methanol, applied in separation methods, chemical instruments and methods, air quality improvement, etc., can solve problems such as unqualified total sulfur content of purified gas, pollution of downstream equipment, blockage of pipeline valves, etc., to reduce external supply Effects of cooling capacity and power consumption, reduction of investment and consumption, and reduction of operating load

Active Publication Date: 2012-07-04
WUHUAN ENG
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Problems solved by technology

But the process still has the following problems: 1. In the actual production process, if the ammonia content in the raw gas is too high, it is easy to be enriched in the low-temperature methanol washing device, and it will react with carbon dioxide to form ammonium bicarbonate, which will cause pollution to downstream equipment and pipeline valves Blockage, or react with hydrogen sulfide to form ammonium sulfide, which will cause the total sulfur content of the purified gas to be unqualified after being decomposed at the top of the washing tower at high temperature; 2. The lean methanol at the bottom of the regeneration tower is used as the absorption liquid of the absorption tower after pressurization and cooling, and the circulation volume is large 3. The recovery rate of carbon dioxide is not high, only 50%-70mol%. The concentration of hydrogen sulfide in the acid gas after thermal regeneration is low, and the concentration of hydrogen sulfide is completely dependent on the CO in the raw gas. 2 / H 2 S ratio

Method used

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  • Process for removing acid gas with low-temperature methanol solution
  • Process for removing acid gas with low-temperature methanol solution
  • Process for removing acid gas with low-temperature methanol solution

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Embodiment

[0021] Taking the raw material gas of coal gas as an example, if the attached figure 2 , the processing capacity is 106310Nm 3 / h Raw material gas (1) is in countercurrent contact with boiler feed water (37) in the ammonia washing tower (36), and after ammonia washing, the tower top gas (39) enters the raw material gas cooler (2), and the waste water at the bottom of the tower (38) is removed for sewage treatment . Before the feed gas enters the feed gas cooler (2), a small amount of lean methanol (24) is sprayed into it. After heat exchange and cooling, the water-containing methanol separated by the feed-liquid separator (3) enters the bottom of the absorption tower (4) and contains water. Methanol goes to the methanol / water separation tower (26). The lean methanol (5) from the heat regeneration tower (22) and the methanol semi-poor liquid (40) from the desorption tower (14) are sent successively from the top of the absorption tower (4), and are contacted and washed with t...

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Abstract

The invention relates to a process for removing an acid gas with a low-temperature methanol solution, solving the problem that a low-temperature rectisol plant enriches ammonia and has lower recovery rate of CO2, lower concentration of H2S in acid gases and large solution circulating volume in the traditional process. The process comprises feed gas preprocessing, desulfuration and decarbonizationby an absorption tower, CO2 analysis and gas stripping and hydrogen sulfide concentration by a desorber, regeneration by a heat regenerator and deficient methanol separation by a methanol / water separation tower, wherein the feed gas is conveyed into an ammonia scrubber for deamination and preprocessing. The process can reduce the ammonia enrichment in the low-temperature rectisol plant, increase the recovery rate of CO2, improve the concentration of H2S in acid gases, reduce the circulating volume of the solution and ensure the quality of purified gas products.

Description

technical field [0001] The invention relates to a gas purification process, in particular to a process for removing acid gas by using a low-temperature methanol solution. Background technique [0002] The low-temperature methanol washing method belongs to the physical absorption method. This technology utilizes the physical characteristics of methanol's great solubility to acid gas at low temperature, uses cold methanol as the acid gas absorption liquid, and selectively absorbs H in the raw gas in stages. 2 S and CO 2 And various organic sulfur and other impurities, it is widely used in the production of synthetic ammonia, city gas, natural gas desulfurization, industrial hydrogen production, hydroxyl synthesis, synthetic methanol or some other one-carbon chemicals. This process is an effective gas purification technology jointly developed by Linde and Lurgi in Germany in the 1950s, usually including raw gas pretreatment, absorption tower desulfurization and decarbonization...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/14
CPCY02C10/06Y02A50/20Y02C20/40
Inventor 李繁荣胡四斌徐建民夏吴
Owner WUHUAN ENG
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