A process for producing gasoline from synthetic gas

A synthesis gas and gasoline technology, applied in the petroleum industry, the preparation of liquid hydrocarbon mixtures, etc., can solve the problems of catalyst sintering deactivation, catalyst deactivation, catalyst life shortening, etc., to improve energy utilization, reduce energy consumption and Effect of cost and equipment investment increase

Active Publication Date: 2015-12-30
SHANXI LUAN MINING GRP +1
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

In this patent, a fixed bed is used to produce methanol from syngas, but since the methanol synthesis reaction (1) is a strong exothermic reaction, the catalyst is easily deactivated under high temperature conditions during the reaction process, requiring a large amount of circulating cooling medium, and must Limit the conversion rate of synthesis gas, so that the catalyst cannot be sintered and deactivated due to too much heat generated due to too high conversion rate. Therefore, the process has high energy consumption and low product yield
Methanol dehydration includes two-step reactions (2) and (3), both of which are strongly exothermic reactions. During the reaction process, the catalyst is easily coked and deactivated at high temperature, which shortens the life of the catalyst and does not meet the requirements of industrial production.

Method used

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  • A process for producing gasoline from synthetic gas

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Step (1) Synthesis gas 1 is mainly produced by coal gasification or natural gas cracking, with a hydrogen-to-carbon volume ratio of 2, pressurized to 2.5MPa, and heat-exchanges with the tail gas 8 of the preheated synthesis gas through the heat exchanger 2, and the preheated After heating, it enters the slurry bed reactor 4.

[0033] Step (2) Slurry bed reactor 2 adopts air flow bubbling suspension slurry bed reactor, uses liquid paraffin as inert liquid phase heat carrier, reaction temperature is 240°C, reaction pressure is 2.5MPa, and space velocity is 6000ml·g -1 h -1, the syngas is dehydrated into dimethyl ether by a bifunctional catalyst (a bifunctional catalyst LP201+TH16 developed by Tsinghua University (LP201 mass content 67%, TH16 mass content 33%)) in the reactor, in which the single-pass conversion rate of CO is 65% .

[0034] Step (3) The tail gas 5 after the slurry bed reaction directly enters the fixed bed reactor 6, and the fixed bed reactor 6 is equipp...

Embodiment 2

[0039] Step (1) Synthesis gas 1 is mainly produced by coal gasification or natural gas cracking, with a hydrogen-to-carbon volume ratio of 3, pressurized to 2.0 MPa, and exchanges heat with the tail gas 8 of the preheated synthesis gas through the heat exchanger 2. After heating, it enters the slurry bed reactor 4.

[0040] Steps (3), (4), (5) are the same as in Example 1

[0041] Step (2) Slurry bed reactor 4 adopts air flow bubbling to suspend slurry bed reactor, uses liquid paraffin as inert liquid phase heat carrier, and uses n-hexane as supercritical medium, reaction temperature 250°C, reaction pressure 3MPa, space velocity 5000ml·g -1 h -1 , the syngas is dehydrated into dimethyl ether by a bifunctional catalyst (a bifunctional catalyst LP201+TH16 developed by Tsinghua University (LP201 mass content 67%, TH16 mass content 33%)) in the reactor, in which the single-pass conversion rate of CO is 65% , H 2 The single-pass conversion rate is 62%.

[0042] The obtained ga...

Embodiment 3

[0044] Step (1) Synthesis gas 1 is mainly produced by coal gasification or natural gas cracking, with a hydrogen-to-carbon volume ratio of 2.5, pressurized to 4.0 MPa, and exchanges heat with the tail gas 8 of the preheated synthesis gas through the heat exchanger 2. After heating, it enters the slurry bed reactor 4.

[0045] Steps (3), (4), (5) are the same as in Example 1

[0046] Step (2) The slurry bed reactor 4 adopts a mechanically stirred tank type slurry bed, uses liquid paraffin as an inert liquid phase heat carrier, and uses n-hexane as a supercritical medium, the reaction temperature is 230°C, the reaction pressure is 4MPa, and the space velocity is 3000ml· g -1 h -1 , the synthesis gas passes through the bifunctional catalyst in the reactor (the bifunctional catalyst CN1176742C developed by Nanhua Group, the composition of the catalyst mainly includes metal oxides and acidic components, and the suitable weight content of metal oxides: CuO is 30% , ZnO is 20%, an...

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Abstract

A process for preparing gasoline through synthesis gas is characterized in that pressurized synthesis gas is sent into a slurry bed reactor loaded with a catalyzer for synthesizing dimethyl ether to synthesize dimethyl ether, gas coming from the slurry bed reactor directly enters into a fixed bed reactor loaded with a catalyzer for synthesizing gasoline to synthesize gasoline, one part of mixed gas coming from the fixed bed reactor enters into a gas-liquid separator after being preheated for synthesizing gas through a heat exchanger, the rest part of the mixed gas enters into the gas-liquid separator after the heat of the rest part is recycled through an exhaust boiler, then liquid phase and gas are obtained after separation, the liquid phase comprises gasoline and water, one part of gas is discharged or used for other purposes, and the other part of gas circulates and returns to the slurry bed reactor through a compressor. The process provided by the invention has the advantages that the conversion per pass of the synthesis gas is high, energy consumption is low, the cost is low, and the service life of the catalyzer is long.

Description

technical field [0001] The invention belongs to a synthetic gas gasoline production process, in particular to a slurry bed-fixed bed combined gasoline production process. Background technique [0002] my country is rich in coal and lacks oil. It is estimated that by 2020, my country's dependence on foreign oil may be close to 65%. Therefore, the development of alternative energy sources for oil is imminent, and coal-to-oil has become an important trend in my country's energy strategy. [0003] At present, the coal-to-liquids process mainly includes the direct liquefaction process and the indirect liquefaction process of coal. The process conditions of direct coal liquefaction are very harsh, and the products are complex and difficult to separate; the indirect coal liquefaction technology is to first gasify coal into synthesis gas, and then use coal-based synthesis gas (carbon monoxide and hydrogen) as raw materials, at a certain temperature and pressure, It is a process for...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G2/00
Inventor 王东飞冯永发章清李忠孟凡会邹佩良张洪建
Owner SHANXI LUAN MINING GRP
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