Improved low-temperature rectisol and improved low-temperature rectisol device
A low-temperature methanol washing and improved technology, which is applied in the process of purifying water gas and water gas purification process, can solve the problems of high production operation cost, large amount of circulating methanol, and large investment in equipment, so as to reduce production operation cost and reduce Pipeline and equipment size, the effect of reducing equipment investment
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2012-06-27
- Estimated Expiration
- Not applicable · inactive patent
Smart Images
Figure 1 Figure 2
Abstract
Description
technical field
[0001] The invention relates to the technical field of water gas purification, in particular to a water gas purification process flow, which is a novel water gas purification process flow. Background technique
[0002] The low-temperature methanol washing purification technology is a process suitable for the treatment of sulfide-containing water gas purification developed by Linde Company and Lurgi Company in the early 1950s. Low-temperature methanol washing uses methanol as an absorbent for physical absorption.
[0003] Due to the sharp rise in oil prices, the cost of petrochemicals has increased significantly, and low-cost coal has become a new raw material for the production of petrochemical products. Low-temperature methanol washing has good selectivity, and can selectively remove carbon dioxide and hydrogen sulfide. The high degree of gas purification can make the total sulfur content in the purified process gas less than 0.1ppm, which can well protect...
Examples
Embodiment Construction
[0020] The device structure of the present invention is as figure 1 Shown: a device for low-temperature methanol washing, including a sulfide absorption tower 1, the sulfide absorption tower 1 is connected to a process gas quencher 2, and the process gas quencher 2 is connected to a carbon dioxide quencher 3. A carbon dioxide separation tank 4 is arranged between the chiller 3 and the carbon dioxide absorption tower 5. The carbon dioxide separation tank 4 communicates with the carbon dioxide chiller 3 through pipelines, and the carbon dioxide absorption tower 5 communicates with the sulfide absorption tower 1 through pipelines.
[0021] The principle of the present invention is as follows: firstly, the sulfide is removed, and the process gas after the sulfide removal is cooled to liquefy part of the carbon dioxide, and then the liquid carbon dioxide is separated by a separation device. Part of the carbon dioxide remaining in the process gas is removed by using methanol. Due t...