Method for preparing synthesis gas from coke oven gas

A technology for coke oven gas and synthesis gas, which is applied in chemical instruments and methods, bulk chemical production, inorganic chemistry, etc., can solve the problem of unsuitable methanol production and F-T synthesis, increase equipment investment and operating costs, and syngas H/C Advanced problems, to achieve the effect of less impurities, comprehensive utilization, and efficient utilization

Inactive Publication Date: 2010-06-02
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The disadvantage is that the H / C of the raw material gas itself is high, and carbon dioxide is not used as a carbon source, so the H / C of the obtained synthesis gas is relatively high, with an average of 2.7, which is not suitable for the production of methanol and F-T synthesis in industry
Its shortcoming is that the coke oven gas and the gas conversion agent carry out a non-catalytic conversion reaction in the reformer. To make the conversion rate of the reactant high, the reaction temperature must be increased, and the consumption of oxygen must be increased. The reaction temperature When the temperature is too high, it is easy to deposit carbon. In order to reduce carbon deposition, it is necessary to increase the amount of water vapor added, which increases equipment investment and operating costs.

Method used

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  • Method for preparing synthesis gas from coke oven gas
  • Method for preparing synthesis gas from coke oven gas
  • Method for preparing synthesis gas from coke oven gas

Examples

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Effect test

Embodiment 1

[0026] Firstly, the coke oven gas produced by high-temperature dry distillation of coal as raw material gas is desulfurized and purified, and the sulfur content after treatment is less than 5ppm.

[0027] Secondly, at normal temperature and under a pressure of 1-4MPa, mix some carbon dioxide and water vapor with a purity of 93% and coke oven gas after desulfurization and purification, and send it to the waste heat boiler 4 to preheat to 400-700°C; at the same time, the Some carbon dioxide and water vapor with a purity of 93% and oxygen with a purity of 92% are mixed and sent to the preheater 3 to be preheated to 400-700°C.

[0028] The amounts of oxygen, carbon dioxide and water vapor used per mole of desulfurized and purified coke oven gas are: oxygen ≤ 0.28 mol; carbon dioxide ≤ 0.3 mol; water vapor ≤ 0.3 mol.

[0029] Then, the preheated raw gas is heated at 2500~5000h -1 Under the condition of space velocity, they are fed into the reactor 1 and reacted while mixing. At 10...

Embodiment 2

[0046] Firstly, the coke oven gas produced by high-temperature dry distillation of coal as raw material gas is desulfurized and purified, and the sulfur content after treatment is less than 5ppm.

[0047] Secondly, at normal temperature and under a pressure of 1-4MPa, mix some carbon dioxide and water vapor with a purity of 99% and coke oven gas after desulfurization and purification, and send it to the waste heat boiler 4 to preheat to 400-700°C; at the same time, the Part of the carbon dioxide and water vapor with a purity of 99% and oxygen with a purity of 98% are mixed and sent to the preheater 3 to be preheated to 400-700°C.

[0048] The amounts of oxygen, carbon dioxide and water vapor used per mole of desulfurized and purified coke oven gas are: oxygen ≤ 0.28 mol; carbon dioxide ≤ 0.3 mol; water vapor ≤ 0.3 mol.

[0049] Then, the preheated raw gas is heated at 2500~5000h -1 Under the condition of space velocity, they are fed into the reactor 1 and reacted while mixing...

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Abstract

The invention discloses a method for preparing synthesis gas from coke oven gas. Desulfurized and purified high-temperature carbonization gas is taken as a raw material gas, and oxygen, carbon dioxide and vapor are taken as gas transforming agents; and the method comprises the following steps: preheating the raw material gas and the gas transforming agents, introducing into a reactor for mixing, and simultaneously generating autothermal non-catalytic conversion reaction; and then introducing mixed gas after the non-catalytic conversion reaction into a catalyst bed layer for catalytic reforming reaction to prepare the synthesis gas. In the method, the consumption of the catalyst is low, the conversion rate is high, the ratio of hydrogen to carbon of the synthesis gas has strong controllability, the comprehensive utilization of energy is realized, the coke oven gas and the carbon dioxide are utilized as raw material gases, and the method for preparing the synthesis gas from the coke oven gas is economic, environment-friendly and low-carbon.

Description

technical field [0001] The invention relates to a method for producing synthesis gas from coke oven gas, in particular to a method for producing synthesis gas by reacting coke oven gas, oxygen, carbon dioxide and water vapor. Background technique [0002] Coke oven gas is a by-product produced during the coking process. It usually contains 40-70% hydrogen, 10-30% methane, and a small amount of other gases. Except for a small amount used for furnace combustion and power generation, a large amount of it is directly vented and burned to waste resources. It also pollutes the environment. At the same time, my country's carbon dioxide emissions rank second in the world, which poses a great threat to our living environment. Therefore, rational use of coke oven gas and carbon dioxide has important economic and environmental significance, and meets the requirements of low-carbon economy and sustainable development. [0003] Coke oven gas, oxygen, carbon dioxide, and water vapor are u...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B3/34C01B3/36C01B3/38
CPCY02P20/52
Inventor 申曙光张翠
Owner TAIYUAN UNIV OF TECH
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