Method for preparing liquefied natural gas by converting raw materials of coke oven gas and blast furnace gas

A technology of liquefied natural gas and coke oven gas, which is applied in the direction of gas fuel, combustible gas purification, combustible gas purification/transformation, etc., which can solve the problems of increased investment and operating costs, short operating life of equipment, and high reaction temperature, and achieve investment and operation The effect of cost reduction, investment and operating cost reduction, and reaction temperature reduction

Inactive Publication Date: 2011-11-23
SHANGHAI HANXING ENERGY TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] So far, some people have tried the direct liquefaction of coke oven gas to produce LNG, which is involved in the patent 200820132075.5, but because coke oven gas contains a lot of H 2 S, naphthalene, tar, CO 2 、H 2 O, metal mercury and other components, so direct liquefaction is actually impossible, and it will block the LNG cold box, and the quality of natural gas cannot meet the national standard, and the output of liquefied natural gas is small and the benefit is low
In the patent 200810055168.7, a method for producing liquefied natural gas with coke oven gas as raw material is also mentioned, but the method has the following problems: 1) coke oven gas needs to be boosted and pretreated with a blower before compression, so This prolongs the process and increases investment and operating costs; 2) After the coke oven gas is compressed, a hydrolysis process needs to be set up. The hydrolysis process uses a chemical reaction method to convert organic sulfur into inorganic sulfur and then remove it. The investment is large and the energy consumption is high. , the service life of the hydrolytic desulfurizer is also short, and the process is complicated and there are many equipme

Method used

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  • Method for preparing liquefied natural gas by converting raw materials of coke oven gas and blast furnace gas
  • Method for preparing liquefied natural gas by converting raw materials of coke oven gas and blast furnace gas
  • Method for preparing liquefied natural gas by converting raw materials of coke oven gas and blast furnace gas

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Effect test

Embodiment 1

[0061] With coke oven gas 8500Nm 3 / h, the composition is as follows:

[0062]

[0063]

[0064] In order to produce more coke oven gas, add low-value 1700Nm 3 / h blast furnace gas, the composition is as follows:

[0065]

[0066]

[0067] After the two kinds of gas are mixed, they directly enter the desulfurization tower at a pressure close to normal pressure of 2KPa.G and a normal temperature of 40°C, and the H 2 S is removed below 10ppm, then enters the reciprocating gas compressor, compresses to 1.6MPa.G, and then enters the TSA+PSA adsorption purification process to remove naphthalene, tar, benzene, residual organic sulfur, inorganic sulfur, etc. in the gas All of them are removed by adsorption at one time to obtain a purified gas demethanization process with naphthalene<0.1ppm, tar<0.1ppm, benzene<1ppm, total sulfur<0.1ppm, pressure 1.5MPa.G, and temperature 40°C.

[0068]In the methanation process, through the isothermal-adiabatic series methanation react...

Embodiment 2

[0071] Also has coke oven gas 8500Nm 3 / h, the composition is as follows:

[0072]

[0073]

[0074] In the absence of blast furnace gas, only coke oven gas is used as raw material, and this technology can also be used.

[0075] At this time, the coke oven gas directly enters the desulfurization tower at a pressure of 2KPa.G and a normal temperature of 40°C, and the H 2 S is removed below 10ppm, then enters the reciprocating gas compressor, compresses to 1.6MPa.G, and then enters the TSA+PSA adsorption purification process to remove naphthalene, tar, benzene, residual organic sulfur, inorganic sulfur, etc. in the gas All of them are removed by adsorption at one time to obtain a purified gas demethanization process with naphthalene2 All converted to CH 4 , residual CO+CO 2 The content of 2 The content is 42.65 (v%), the pressure is 1.4MPa.G, the temperature is 40°C, and it enters the drying and demetallization process. After drying, the H2O content is less than 1ppm, a...

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Abstract

The invention discloses a method for preparing liquefied natural gas by converting raw materials of coke oven gas and blast furnace gas. In the technology, the coke oven gas and the blast furnace gas are taken as the raw materials, the raw materials are subjected to normal-temperature normal-pressure dry desulfurization, gas compression, gas adsorption purification, gas isothermal-adiabatic serial methanation, gas adsorption drying and demetalization, freezing liquefication separation and other technical processes, and high-quality liquefied natural gas with the purity of over 99 percent is produced. By the technology, harmful impurities such as sulfur, naphthalene, tar, benzene, mercury and the like in the gas can be efficiently and easily removed fully at low cost, and components with low value, such as H2, CO, CO2 and the like are completely converted into required CH4 component with high value, so the method has the characteristics of low requirement on quality of feed gas, high yield of liquefied natural gas product, high product purity, low production energy consumption, no environmental pollution, reliable flow, low investment, simple operation and good economic benefit.

Description

【Technical field】 [0001] The invention relates to a process flow method for comprehensively utilizing coke oven gas and blast furnace gas to produce a large amount of liquefied natural gas. 【Background technique】 [0002] my country is the largest coke producer in the world. During the coke production process, a large amount of coke oven gas (over 80 billion cubic meters per year) will be produced by-product. Except for about half of the coke oven gas being returned to the furnace as fuel, the remaining half needs to be used separately. , Such as gas, power generation, production of synthetic ammonia, methanol, dimethyl ether, etc. However, due to the common problem of large investment or low benefit in these utilization methods, many coke production enterprises still directly burn and discharge coke oven gas in large quantities, resulting in a large waste of resources and environmental pollution. At the same time, my country is the largest steel producing country in the wor...

Claims

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Application Information

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IPC IPC(8): C10L3/08C10L3/10C10K1/20C10K1/32
Inventor 尹冬梅
Owner SHANGHAI HANXING ENERGY TECH
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