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Coal-to-olefin process tail gas internal recycling system and working method thereof

A coal-to-olefins and working method technology, applied in the field of coal chemical industry, can solve the problems of greenhouse gas emissions, waste of resources, high energy consumption, etc., and achieve the effects of low tail gas emissions, reduced production and operation costs, and reduced emissions

Pending Publication Date: 2021-01-01
CHINA HUANENG GRP CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, in large-scale coal-to-synthetic ammonia and coal-to-methanol projects, a large amount of CO in tail gas 2 Due to the low concentration, it is directly vented, which not only causes a large amount of greenhouse gas emissions, but also causes CO 2 waste of resources
In order to recover the CO emitted from the exhaust gas 2 , can be recovered by PSA or MEA, MDEA, etc., and can even be directly compressed and returned to the raw gas, but this requires additional capture equipment and consumes a lot of energy

Method used

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  • Coal-to-olefin process tail gas internal recycling system and working method thereof

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Embodiment Construction

[0029] The present invention will be described in further detail below in conjunction with accompanying drawing and specific embodiment, and its content is explanation of the present invention rather than limitation:

[0030] Such as figure 1 , the tail gas internal recycling system of the coal-to-olefins process of the present invention includes a coal-to-olefins unit 1, a tail gas collection unit 2, a fly ash collection unit 3, a fly ash pretreatment unit 4, an exhaust steam recovery unit 5, and a tail gas treatment unit Unit 6 and product collection unit 7.

[0031] The fly ash outlet of the coal-to-olefins unit 1 is connected to the inlet of the fly ash collection unit 3, the outlet of the fly ash collection unit 3 is connected to the inlet of the fly ash pretreatment unit 4, and the outlet of the fly ash pretreatment unit 4 It is connected to the solid inlet of the tail gas treatment unit 6; the steam outlet of the coal-to-olefins unit 1 is connected to the inlet of the ...

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Abstract

The invention discloses an internal recycling system for tail gas in a coal-to-olefin process and a working method thereof, and belongs to the technical field of coal chemical industry. A coal ash outlet of a coal-to-olefin unit is connected with an inlet of a coal ash collection unit, an outlet of the coal ash collection unit is connected with an inlet of a coal ash pretreatment unit, and an outlet of the coal ash pretreatment unit is connected with a solid inlet of a tail gas treatment unit; a steam outlet of the coal-to-olefin unit is connected with an inlet of a discharged steam recovery unit, and an outlet of the discharged steam recovery unit is connected with a steam inlet of the tail gas treatment unit; a tail gas outlet of the coal-to-olefin unit is connected with an inlet of thetail gas collection unit; an outlet of the tail gas collection unit is connected with a tail gas inlet of the tail gas treatment unit; an outlet of the tail gas treatment unit is connected with an inlet of a product collection unit. The system is low in tail gas emission, equipment investment is reduced, energy in the process is effectively utilized, products with economic value are produced, andthe system has a good application prospect.

Description

technical field [0001] The invention belongs to the technical field of coal chemical industry, and in particular relates to an internal circulation utilization system of tail gas in the coal-to-olefins process and a working method thereof. Background technique [0002] With the rapid development of the coal-to-olefins industry, CO in the production of coal-to-olefins 2 Emissions are also increasing. In the coal-to-olefins process, the unit product CO 2 Emissions are 10 tons of CO 2 / ton of olefins. Carbon emissions from coal-to-olefins production process accounted for 53.38%, carbon emissions from fuel combustion in thermoelectric boilers accounted for 36.25%, and carbon emissions from net purchased electricity consumption accounted for 10.36%. It can be seen that direct carbon emissions are the main CO 2 Emission source, CO 2 There is a lot of room for emission reduction utilization. Therefore, the research on carbon capture and utilization in coal-to-olefins proces...

Claims

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Application Information

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IPC IPC(8): C10G1/00B01D53/72
CPCC10G1/002B01D53/72B01D2257/702B01D2258/02
Inventor 刘蓉王琪刘练波郜时旺李旭
Owner CHINA HUANENG GRP CO LTD
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