System and method for co-producing low carbon olefin and ammonia by low carbon alkane

A technology of low-carbon olefins and low-carbon alkanes, applied in chemical instruments and methods, preparation/separation of ammonia, hydrocarbons, etc., can solve problems such as large investment, high energy consumption, waste gas, waste residue and wastewater pollution, and shorten The effect of high flow and process integration and less waste discharge

Inactive Publication Date: 2017-10-17
SHANGHAI JIAO TONG UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, my country's ammonia synthesis route mainly adopts the coal gasification route with coal as raw material, which requires large investment, high energy consumption, and pollution of waste gas, waste residue and waste water.

Method used

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  • System and method for co-producing low carbon olefin and ammonia by low carbon alkane
  • System and method for co-producing low carbon olefin and ammonia by low carbon alkane

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] A factory uses propane as raw material, the application such as figure 1 The shown system co-produces propylene and ammonia, and the system includes an alkane dehydrogenation unit 100, an air separation unit 200 and an ammonia synthesis unit 300, wherein the alkane dehydrogenation unit 100 is connected to the ammonia synthesis unit 300 through a hydrogen delivery pipeline 12, and the air separation unit 200 is connected with ammonia synthesis device 300 through nitrogen delivery pipeline 22.

[0025] Specifically:

[0026] The alkane dehydrogenation unit 100 comprises an alkane dehydrogenation reaction device 110, a hydrogen hydrocarbon separation device 120 and an alkane separation device 130, and the alkane dehydrogenation reaction device 110 is connected with the hydrogen hydrocarbon separation device 120, and the alkane separation device 130 is connected with the alkane circulation pipeline 13 The alkane dehydrogenation reaction equipment 110 is connected, the hydr...

Embodiment 2

[0036] A factory uses isobutane as raw material, the application such as figure 1 The shown system co-produces isobutene and ammonia, and the system includes an alkane dehydrogenation unit 100, an air separation unit 200 and an ammonia synthesis unit 300, wherein the alkane dehydrogenation unit 100 is connected to the ammonia synthesis unit 300 through a hydrogen delivery pipeline 12, and the air separation unit 200 is connected with ammonia synthesis device 300 through nitrogen delivery pipeline 22.

[0037] Wherein, the alkane dehydrogenation unit 100 includes alkane dehydrogenation reaction equipment 110, hydrogen hydrocarbon separation equipment 120 and alkane separation equipment 130, alkane dehydrogenation reaction equipment 110 is connected with hydrogen hydrocarbon separation equipment 120, and alkane separation equipment 130 passes through the alkane circulation pipeline 13 is connected to the alkane dehydrogenation reaction equipment 110, the hydrogen delivery pipeli...

Embodiment 3

[0047] A factory uses propane as raw material, the application such as figure 2 The system shown co-produces propylene and ammonia. The difference from Example 1 is that in this example, in order to reduce equipment investment, a hydrogen-nitrogen mixed gas compressor 310' is used to replace the hydrogen compressor 310 and nitrogen compressor 320 in Example 1. The alkane dehydrogenation device 100 The high-purity hydrogen and high-purity nitrogen from the air separation unit 200 are boosted by the hydrogen-nitrogen mixture compressor 310 ′, and then enter the ammonia synthesis reaction device 330 to generate ammonia.

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Abstract

The invention relates to a system and method for co-producing low carbon olefin and ammonia by low carbon alkane. The system comprises an alkane dehydrogenation device (100), an air separation unit (200) and an ammonia synthesis device (300). The alkane dehydrogenation device (100) is connected with the ammonia synthesis device (300) by a hydrogen conveying pipeline (12). The air separation unit (200) is connected with the ammonia synthesis device (300) by a nitrogen conveying pipeline (22). The low carbon alkane is reacted in the alkane dehydrogenation device so as to obtain the corresponding low carbon olefin and hydrogen, a low carbon olefin product with high purity and the hydrogen are obtained by the separation, the hydrogen is conveyed into the ammonia synthesis device, and reacts with the high-purity nitrogen obtained by the air separation unit, so the ammonia is generated. Compared with the current olefin uni-yield alkane dehydrogenation technology or coal-based synthesis ammonia technology, the method is capable of adequately using the byproduct hydrogen in the alkane dehydrogenation process to generate the ammonia, and has the advantages of short technological process, less waste discharge, and high economic and social benefit.

Description

technical field [0001] The invention belongs to the field of chemical industry, and in particular relates to a system and method for co-producing low-carbon olefins and ammonia from low-carbon alkanes. Background technique [0002] Olefins, especially low-carbon olefins, ethylene, propylene and butene (including n-butene, 2-butene and isobutene) are the basis of the entire petrochemical industry, and their output and technical level represent the country's economic and technological development level. At present, low-carbon olefins mainly come from petroleum cracking (including steam cracking and catalytic cracking). The emerging coal chemical route, that is, methanol to olefins (MTO, MTP) is mainly suitable for countries and regions rich in coal resources, because methanol can be produced with cheap coal, and it is currently developing rapidly in my country. In addition, with the exploitation of natural gas in the United States and the Middle East, especially shale gas, a ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C5/327C07C11/04C07C11/06C07C11/08C07C11/09C01C1/04
CPCC01C1/04C07C5/327C07C11/04C07C11/06C07C11/08C07C11/09
Inventor 肖文德李学刚
Owner SHANGHAI JIAO TONG UNIV
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