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Thermoelectricity combined production method and apparatus for preparing alkene and by coal and natural gas

A technology of natural gas and olefins, which is applied in the field of combined heat and power generation and devices for producing olefins and ammonia from coal and natural gas, which can solve the problems of low energy utilization efficiency of the system, achieve comprehensive utilization, reduce energy waste, and reduce production costs

Inactive Publication Date: 2013-07-24
PETROCHINA CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] In the method of producing ethylene from coal, since the hydrogen-to-carbon ratio in the synthesized gas is low, generally less than 1, gas shifting is often required when synthesizing downstream products to combine CO and H 2 O reacts to form H 2 and CO 2 Raise H 2 / CO, CO added during transformation 2 emissions to the environment, and in recovering CO 2 , CO removal 2 In the process of converting CO and CO, additional energy is consumed, which makes the energy utilization efficiency of the system lower

Method used

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  • Thermoelectricity combined production method and apparatus for preparing alkene and by coal and natural gas
  • Thermoelectricity combined production method and apparatus for preparing alkene and by coal and natural gas
  • Thermoelectricity combined production method and apparatus for preparing alkene and by coal and natural gas

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Embodiment 1

[0059] figure 1 It is a process flow chart of Embodiment 1 of the cogeneration process for producing olefins and ammonia from coal and natural gas in the present invention. In this embodiment, coal and natural gas are used as raw materials, and the existing mature technology is used to prepare synthesis gas. Among them, when coal is used as raw material to produce syngas, American Texaco entrained flow bed coal-water slurry gasification technology and Holland Shell pulverized coal gas pressurized gasification technology can be used. The hydrogen-to-carbon ratio in coal-to-synthesis gas is 0.4-0.7; Methane carbon dioxide reforming technology is used when natural gas is used as raw material to produce synthesis gas. The hydrogen-to-carbon ratio of the synthesis gas produced by methane carbon dioxide reforming technology is 1. Usually, the synthesis gas needs to undergo gas shift to adjust the hydrogen-to-carbon ratio to achieve the optimal hydrogen-to-carbon ratio of 2:1 for me...

Embodiment 2

[0070] figure 2 It is the process flow chart of the second embodiment of the cogeneration process for producing olefins and ammonia from coal and natural gas of the present invention. In this embodiment, coal is used as raw material to produce synthesis gas, which can be gasified by American Texaco entrained flow bed coal water slurry Technology, Holland Shell pulverized coal gas pressurized gasification technology; natural gas steam reforming process is used when natural gas is used as raw material to produce synthesis gas. The hydrogen-carbon ratio in the synthesis gas produced by the steam reforming process of natural gas is high, generally 2.5 to 3.0. By adjusting the mass ratio of raw coal and natural gas, the coal-to-synthesis gas and natural gas-to-synthesis gas can be combined according to the preset ratio To make it meet the optimal hydrogen-carbon ratio of methanol synthesis, the mixed synthesis gas is directly sent to the synthesis of methanol, and the unreacted ga...

Embodiment 3

[0079] In order to make the technical scheme and advantages of the present invention clearer, the process of the present invention is analyzed below in conjunction with specific example 3, and the described process adopts the above-mentioned method of the present invention. figure 2 Part of the process, this embodiment is only a part of the present invention. This embodiment uses coal and natural gas as raw materials to produce olefins cogeneration process, and does not include ammonia synthesis process. The main steps are: primary purification and desulfurization treatment after coal gasification, natural gas is reformed and mixed with coal-based synthesis gas in a certain proportion, and then methanol synthesis and olefin synthesis are carried out. The unreacted gas from methanol synthesis is divided into three parts, one part Carry out circular synthesis of methanol, one part is used as fuel for the natural gas reforming unit, and the other part is sent to the gas turbine ...

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Abstract

The invention relates to a thermoelectricity combined production method and apparatus for preparing alkene and by coal and natural gas, and the method comprises the following steps: (1) separating coal, steam and air for obtaining oxygen, gasifying oxygen for obtaining water gas by reaction, and purifying for obtaining coal-based synthetic gas; carrying out a reforming reaction from natural gas and carbon dioxide and obtaining a natural gas-based synthetic gas; (2) synthesizing methanol using the coal-based synthetic gas in the step (1) or using the coal-based synthetic gas and the natural gas-based synthetic gas; (3) separating the unreacted gas in the step (2) into three parts, and the first part is used for synthesizing methanol in the step (2), and the second part is used as fuel for providing heat for the natural gas reforming reaction, and the third part is used for power generation and heat supply for the gas turbine; (4) separating the methanol in the step (2) into two parts, and one part is used for preparing alkene and generating water; and the other part is used for the reforming reaction with the generated water for preparing hydrogen and carbon dioxide, and separating hydrogen and carbon dioxide, and synthesizing ammonia from the obtained hydrogen and nitrogen separated from air, wherein, the obtained carbon dioxide by separation is used for the natural gas reforming reaction.

Description

technical field [0001] The invention relates to a cogeneration method and device for producing olefins and ammonia from coal and natural gas. Background technique [0002] Ethylene and propylene are the most basic raw materials in the petrochemical industry. The output of ethylene is considered to be a sign of the level of national economic development. With the development of my country's economy and society, there will still be a relatively high rigid demand in the future. Traditional ethylene production methods mainly use ethane, propane, naphtha, and light diesel as raw materials to produce ethylene through steam cracking in tube furnaces. However, China's light hydrocarbon and petroleum resources are very limited and cannot meet the requirements of ethylene light raw materials. Moreover, the continuous rise of crude oil prices and the aggravation of the inferior quality of crude oil make the product cost of traditional ethylene production methods relatively high. In re...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C11/04C07C11/06C07C1/20C01B3/36C01C1/04F01K23/10
CPCY02P30/20Y02P30/40
Inventor 李云杨莉程光旭张早校
Owner PETROCHINA CO LTD
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