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System and process for preparing olefin by taking coal and coke-oven gas as raw materials

A technology of coke oven gas and raw materials, which is applied in the field of olefin production system, can solve problems such as waste of resources, and achieve the effects of simplified process, optimized resource allocation, and high operational stability

Active Publication Date: 2014-04-02
SOUTH CHINA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] There are two main problems in the existing coal-to-olefins process: first, the energy consumption of the coal-to-olefins process is twice that of the traditional petroleum cracking route; second, the CO 2 Emissions are 5-6 times higher than conventional petroleum routes
China's annual output of coke oven gas is about 35 billion standard cubic meters. However, except for 20% being directly burned as fuel, most of the coke oven gas is directly discharged into the atmosphere, wasting a lot of resources

Method used

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  • System and process for preparing olefin by taking coal and coke-oven gas as raw materials
  • System and process for preparing olefin by taking coal and coke-oven gas as raw materials
  • System and process for preparing olefin by taking coal and coke-oven gas as raw materials

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Experimental program
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Effect test

Embodiment 1

[0037] A system for producing olefins from coal and coke oven gas, comprising a coal water slurry preparation unit 1, a coal gasification unit 2, a synthesis gas purification unit 4, a methanol synthesis unit 5 and an olefin synthesis unit 6 connected in sequence, the water The coal slurry preparation unit 1 is provided with a raw material inlet that can be fed into pulverized coal. The coal water slurry outlet of the coal water slurry preparation unit 1 is directly connected with the coal water slurry raw material inlet of the coal gasification unit 2. The coal gasification of the coal gasification unit 2 is roughly synthesized The gas outlet is directly connected to the crude synthesis gas inlet of the synthesis gas purification unit 4 through a pipeline, the synthesis gas purification unit 4 is provided with a net synthesis gas outlet, the methanol synthesis unit 5 is provided with a synthesis gas inlet for methanol synthesis and a methanol outlet, and the methanol outlet is ...

Embodiment 2

[0059] Utilize the system described in embodiment 1 to carry out olefin preparation, concrete implementation is as follows:

[0060] The raw coal pulverized flow that enters the system of the present invention is 125.85t / h. The raw coke oven gas flow rate is 201.4t / h, and the feed ratio of coke oven gas to pulverized coal is 1.6. The composition of coke oven gas is shown in Table 1. The general flow chart of coal and coke oven gas combined production of olefins can be found in figure 2 .

[0061] Table 1 Composition of coke oven gas

[0062] Element

H 2

CH 4

CO

CO 2

N 2

O 2

C m h n

Volume fraction%

59.5

24.8

6.5

5.5

3.2

0.3

0.2

[0063] Coke oven gas separation process:

[0064] See the detailed process image 3 , the raw material coke oven gas 21 entering the process is subjected to a three-stage compression heat exchange process through the first compression heat exchanger 39, and...

Embodiment 3

[0072] Utilize the system described in embodiment 1 to carry out olefin preparation, concrete implementation is as follows:

[0073] The flow rate of raw coal powder entering the system of the present invention is 109.75t / h, the flow rate of raw coke oven gas is 142.67t / h, and the feed ratio of coke oven gas and coal powder is 1.3. The composition of coke oven gas is shown in Table 1. The general flow chart of coal and coke oven gas combined supply to olefins process is shown in the appendix figure 2 .

[0074] Table 1 Composition of coke oven gas

[0075] Element

H 2

CH 4

CO

CO 2

N 2

O 2

C m h n

Volume fraction%

61.7

21.8

4.1

6.4

3.2

0.3

2.5

[0076] Coke oven gas separation process:

[0077] See the detailed process image 3 , the raw material coke oven gas 21 entering the process is subjected to a three-stage compression heat exchange process through the first compression heat exc...

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Abstract

The invention belongs to the technical fields of energies and chemical industry, and discloses a system and a process for preparing olefin by taking coal and coke-oven gas as raw materials. The system for preparing olefin by taking coal and coke-oven gas as raw materials comprises a water-coal-slurry preparation unit, a coal gasification unit, a synthesis gas purification unit, a methanol synthesis unit, an olefin synthesis unit, a coke-oven gas separation unit, a methane dry-reforming unit, a methane vapour reforming unit and a gas mixer. By using the system for preparing olefin, hydrogen separated by the coke-oven gas separation unit, methane dry reforming synthesis gas, methane vapour reforming synthesis gas and the clean synthesis gas generated by the coal gasification unit can be mixed, the hydrogen-carbon ratio of the synthesis gas is adjusted to meet the requirements of methanol synthesis so as to synthesize methanol, and then olefin is synthesized. By adopting the device and the process disclosed by the invention, the emission amount of CO2 during the existing coal-to-olefin process can be decreased, the energy utilization ratio can be increased, and the exhaust emission of the industrial coal coking industry can be reduced.

Description

technical field [0001] The invention belongs to the technical field of energy and chemical industry, and specifically relates to a system and process for producing olefins by using coal and coke oven gas as raw materials. Background technique [0002] Alkenes are important platform chemicals. In recent years, the world's olefin production capacity and demand have grown rapidly, especially in China. However, China's ethylene self-sufficiency rate is only about 50%, and the supply of olefins is seriously insufficient. The olefin production process is mainly the cracking or pyrolysis of alkanes, naphtha and gasoline, so olefin production is heavily dependent on petroleum, and the proportion of olefin production from naphtha accounts for 85% of the world's olefin production. Petroleum accounts for 16.2% of China's energy structure, while coal accounts for 74.7%. Therefore, the development of coal to replace petroleum to olefins technology is the main development trend in the f...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C11/02C07C1/20
CPCY02P20/10
Inventor 杨思宇满奕钱宇
Owner SOUTH CHINA UNIV OF TECH
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