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Large-Scale Reactor for Partial Oxidation of Hydrocarbons to Acetylene and Syngas

A synthesis gas and reactor technology, applied in hydrogen/syngas production, fluid mixers, chemical instruments and methods, etc., can solve problems such as large water consumption and pollution, and achieve the effect of reducing the range of quenching nozzles

Active Publication Date: 2018-01-19
BEIJING CHEM REACTION ENG SCI & TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The acetylene industry in my country is still dominated by the calcium carbide method, which has problems such as large water consumption and serious pollution

Method used

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  • Large-Scale Reactor for Partial Oxidation of Hydrocarbons to Acetylene and Syngas
  • Large-Scale Reactor for Partial Oxidation of Hydrocarbons to Acetylene and Syngas
  • Large-Scale Reactor for Partial Oxidation of Hydrocarbons to Acetylene and Syngas

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Embodiment Construction

[0040] Embodiments according to the present invention will be described in detail with reference to the accompanying drawings. Here, it is to be noted that, in the drawings, the same reference numerals are assigned to components having substantially the same or similar structures and functions, and repeated descriptions about them will be omitted.

[0041] figure 1 A structural block diagram of a large-scale reactor for preparing acetylene and syngas by partial oxidation of hydrocarbons according to an embodiment of the present invention is shown.

[0042] Such as figure 1 As shown, the large-scale reactor for preparing acetylene and syngas by partial oxidation of hydrocarbons according to an embodiment of the present invention includes: a mixing zone 100 , a reaction zone 200 , and a quenching zone 300 .

[0043] The mixing zone 100 has a hydrocarbon inlet and an oxygen inlet, which are used to feed in hydrocarbon and oxygen respectively. The hydrocarbon and oxygen are unif...

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Abstract

Large reactors for the partial oxidation of hydrocarbons to acetylene and synthesis gas, including mixing, reaction and quenching zones. In the mixing zone, there is a swirler and a side air inlet grid. One of the hydrocarbons and oxygen passes through the swirler, and the other passes through the side air inlet grid. Then the two streams are fully and uniformly mixed in the mixing area, and the hydrocarbon The mixing degree with oxygen reaches 99.9%. In the reaction zone, a burner plate and burners arranged on the burner plate are arranged, and the mixed gas is sprayed into the reaction zone through the burner for partial oxidation reaction. In the quenching area, built-in components are set to realize cold wall operation, and quenching nozzles are set on the outer wall of the built-in components to shorten the spraying range of the quenching medium required for cracking gas quenching, ensure the quenching effect of cracking gas, and realize the production capacity of the reactor. More than 30,000 tons / year.

Description

technical field [0001] The invention relates to an acetylene reactor device, in particular to a large-scale reactor device for producing acetylene by partial oxidation of hydrocarbons, which belongs to the field of chemical industry, especially the field of natural gas chemical industry. Background technique [0002] Acetylene is the simplest alkyne and is an important chemical raw material used to produce a series of chemical products such as acetic acid, vinyl acetate, vinyl acetylene, acrylic acid, butadiene, 1,4-butanediol, etc. Monomers of materials such as synthetic rubber, synthetic fibers, and plastics. As a representative of partial oxidation of hydrocarbons to acetylene, partial oxidation of natural gas to acetylene co-production of synthesis gas can efficiently utilize resources such as natural gas, shale gas and coalbed methane, and is a natural gas chemical technology with good economics. In recent years, with the efficient exploitation of resources such as sha...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J19/00B01F5/06C07C2/82C07C11/24C01B3/36
CPCB01J19/00C01B3/36C07C2/82C01B2203/025C01B2203/1235C01B2203/1241C01B2203/1276C01B2203/062B01J2219/00006B01F25/421C07C11/24
Inventor 王金福唐强靳辉
Owner BEIJING CHEM REACTION ENG SCI & TECH CO LTD