Method and system for preparing propylene by oxidative dehydrogenation of chemical chain propane

A chemical chain propane, oxidative dehydrogenation technology, applied in the field of chemical chain propane oxidative dehydrogenation to prepare propylene, can solve the problems that are not conducive to the safe operation of equipment, complicated production process, lower propylene yield, etc., and achieve the elimination of the limitation of thermodynamic equilibrium , good product quality, and the effect of reducing energy consumption

Active Publication Date: 2019-07-30
NORTHEASTERN UNIV LIAONING
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, these emerging technologies also have some problems. As emerging coal chemical technologies, MTO and MTP need to experience coal / CH 4 -Synthesis gas-methanol-propylene multi-step process, resulting in a more complicated production process, lower product purity and higher equipment investment. In addition, if coal is used as raw material, it will consume a lot of water resources and emit a lot of CO 2 and NOx
DHP is a strong endothermic process, so the process needs to consume a lot of energy, and it needs to be carried out under high temperature and low pressure reaction conditions. Under such conditions, the catalyst is easily deactivated and needs to be regenerated repeatedly, and due to the limitation of thermodynamic equilibrium , the one-way propylene yield is not high (generally less than 30%)
ODHP is to feed oxygen and propane into the reactor at the same time in the presence of a catalyst to make propane react with oxygen to generate propylene and water. Although this technology can be carried out under milder conditions, it can also overcome the thermodynamics in the dehydrogenation process. Balance limit, but propane is prone to over-oxidation reaction in the presence of oxygen to generate COx gas (carbon monoxide and carbon dioxide), which will reduce the yield of propylene, and the use of oxygen will also increase the operating cost, which is not conducive to the safe operation of the equipment. In addition, the The technology also requires expensive air separation plants to ensure a constant supply of oxygen

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  • Method and system for preparing propylene by oxidative dehydrogenation of chemical chain propane

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Embodiment 1

[0030] refer to figure 1 , this embodiment provides a system for preparing propylene by oxidative dehydrogenation of chemical chain propane, the system includes a dehydrogenation reactor 3, a mixed gas purification device, a mixed gas separation device 13, an oxidation reactor 1, a mixed gas heat exchanger 9, Mixed gas waste heat boiler 10 , oxygen-lean gas heat exchanger 5 , oxygen-lean gas waste heat boiler 6 , oxygen-lean gas dust collector 7 , separation equipment 2 , hopper 8 , COx gas storage 15 and propylene storage 14 .

[0031] The dehydrogenation reactor 3 can receive propane and oxygen carrier particles, and provide propane and oxygen carrier particles to react therein at high temperature to generate propylene, water vapor, COx gas and oxygen carrier particles after oxygen loss, COx gas As a by-product of the reaction of propane with oxygen carrier particles. The propylene and water vapor generated by the oxidative dehydrogenation reaction and the water vapor and C...

Embodiment 2

[0081] This embodiment provides a method for preparing propylene by oxidative dehydrogenation of chemically chained propane. The method uses the system of the above-mentioned embodiment 1 and includes the following steps:

[0082] S1. Pass propane into the dehydrogenation reactor 3, and a part of propane and oxygen carrier particles undergo oxidative dehydrogenation reaction at high temperature (preferably 300-700°C) to generate propylene, water vapor and oxygen carrier after deoxygenation Granules, another part of propane in the dehydrogenation reactor 3 undergoes a deep oxidation reaction at high temperature to generate water vapor and COx gas. The mixed gas containing propylene and water vapor generated by the oxidative dehydrogenation reaction, water vapor and COx gas generated by the deep oxidation reaction, and incompletely reacted propane, and the oxygen carrier particles after deoxygenation are output from the dehydrogenation reactor 3 respectively To the mixed gas hea...

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Abstract

The invention relates to a method and system for preparing propylene through chemical-looping oxidative dehydrogenation of propane. The method comprises the following steps: reacting propane with oxygen carrier particles in a dehydrogenation reactor to produce propylene, water vapor and Cox gas, wherein the oxygen carrier particles lose oxygen; separating propylene from a gas mixture obtained in the previous step; and subjecting the oxygen carrier particles having lost oxygen and oxygen-containing gas to an oxidation reaction to produce oxygen-poor gas and regenerated oxygen carrier particles,and circulating the regenerated oxygen carrier particles for participation in dehydrogenation. The system comprises a dehydrogenation reactor, a gas mixture purifying device, a gas mixture separatingdevice and an oxidation reactor, wherein the dehydrogenation reactor can receive oxygen carrier particles produced in the oxidation reactor. The method and system for preparing propylene through chemical-looping oxidative dehydrogenation of propane are efficient, energy-saving, environment-friendly, economic and safe.

Description

technical field [0001] The invention relates to a method and system for preparing propylene by oxidative dehydrogenation of chemical chain propane. Background technique [0002] Propylene is an important basic raw material for chemical synthesis and plays an important role in the petrochemical industry. It is mainly used to synthesize other important chemical products such as polypropylene, acrylonitrile and acrylic acid. At present, 80% of the world's propylene comes from steam cracking or catalytic cracking (FCC) of naphtha and heavy crude oil, but these two processes mainly produce ethylene and refined oil, and propylene is only a by-product. form, so the production of propylene is severely limited. In recent years, with the rapid increase in the consumption of downstream derivatives of propylene, the demand for propylene has continued to rise, and the contradiction between supply and demand has become increasingly obvious. [0003] In order to increase the production o...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C5/48C07C11/06
CPCC07C5/48C07C11/06Y02P20/10Y02P20/50
Inventor 于庆波吴天威王坤秦勤
Owner NORTHEASTERN UNIV LIAONING
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