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A kind of regeneration method of TSA tower in coke oven gas making lng device

A coke oven gas and tail gas technology, which is applied in the removal of gas pollutants, gas fuel, combustible gas purification, etc., can solve the problems of shortened life of adsorption packing, high power cost, accelerated deterioration, etc., and achieve efficient and harmless treatment , Improve the regeneration effect and prolong the service life

Active Publication Date: 2022-02-18
SD STEEL RIZHAO CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] There are generally three TSA naphthalene removal towers in each set of coke oven gas to LNG plant, one for adsorption, one for regeneration, and one for standby after cold blowing. The regeneration process of the adsorption tower includes hot blowing regeneration and cold blowing. Blowing and cooling, the coke oven gas after adsorption and removal of naphthalene is now used as the hot blowing regeneration gas of the adsorption tower and the cold blowing gas for the adsorption and adsorption packing in the tower after regeneration, and the coke oven gas after adsorption and removal of naphthalene is used as the hot blowing regeneration gas and There are several problems in cold blowing: 1) The coke oven gas after adsorption and removal of naphthalene also contains impurities such as hydrogen sulfide and organic sulfur. During regeneration, elemental sulfur will be generated on the adsorption packing, which will block the micropores of the adsorption packing and make the adsorption packing The performance is irreversibly deteriorated, which shortens the life of the adsorption packing; 2) The temperature of coke oven gas after adsorption and removal of naphthalene is 35-40°C. Due to the high temperature, the cooling efficiency of cold blowing is poor, and a large amount of cold blowing gas is required, and the power cost is high; 3 ) When the adsorption performance of the adsorption filler deteriorates to a certain extent, it will cause naphthalene through the tower, resulting in an increase in the naphthalene content of the outlet gas. At this time, the gas is used for regeneration and cold blowing, and the adsorption performance of the adsorption filler will show a trend of accelerated deterioration. Tower switching operations will also be more frequent

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  • A kind of regeneration method of TSA tower in coke oven gas making lng device
  • A kind of regeneration method of TSA tower in coke oven gas making lng device

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Embodiment Construction

[0018] The present invention is described in further detail now in conjunction with accompanying drawing.

[0019] Such as Figure 1-2 , a regeneration method of a TSA tower in a coke oven gas LNG plant, comprising the following steps:

[0020] 1) Transport the coke oven gas to the gas holder for homogenization;

[0021] 2) Compressing the homogenized coke oven gas for the first time, and entering the pre-purification device for pretreatment, the pre-purification device includes a hydrogen sulfide removal unit and a temperature swing adsorption unit;

[0022] 3) The pretreated coke oven gas is compressed for the second time, and then enters the fine desulfurization device for fine desulfurization, in order to convert organic sulfur into hydrogen sulfide, and then desulfurize the hydrogen sulfide through a zinc oxide desulfurizer;

[0023] 4) transporting the finely stripped coke oven gas to a methanation unit, so that the coke oven gas is converted into a synthetic methane m...

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Abstract

The invention discloses a method for regenerating a TSA tower in a coke oven gas-to-LNG device, which comprises the following steps: transporting the coke oven gas to a gas cabinet for homogenization; compressing the homogenized coke oven gas for the first time, and entering into the The pre-purification device performs pretreatment; the pretreated coke oven gas is compressed for the second time and enters the fine desulfurization device for fine desulfurization; the coke oven gas after fine desulfurization is sent to the methanation device; the synthetic methane mixed gas enters the drying After the mercury removal device removes water and mercury, it is transported to the liquefaction device to separate the LNG product and nitrogen and hydrogen tail gas. Part of the nitrogen and hydrogen tail gas is decompressed and returned to the gas cabinet, and part of the nitrogen and hydrogen tail gas enters the first TSA naphthalene removal tower; The gas in a TSA denaphthalene removal tower is heated to 200°C through a heater, and the heated gas enters the second TSA denaphthalene removal tower for thermal blowing regeneration of the second TSA denaphthalene removal tower; it will enter the first TSA denaphthalene removal tower and The nitrogen and hydrogen tail gas after the second TSA denaphthalene removal tower is transported to the pipeline of the primary cooler of the coke oven gas purification system for recovery and repurification.

Description

technical field [0001] The invention belongs to the technical field of deep processing and utilization of coke oven gas, and in particular relates to a regeneration method of a TSA tower in a coke oven gas LNG device. Background technique [0002] There are generally three TSA naphthalene removal towers in each set of coke oven gas to LNG plant, one for adsorption, one for regeneration, and one for standby after cold blowing. The regeneration process of the adsorption tower includes hot blowing regeneration and cold blowing. Blowing and cooling, the coke oven gas after adsorption and removal of naphthalene is now used as the hot blowing regeneration gas of the adsorption tower and the cold blowing gas for the adsorption and adsorption packing in the tower after regeneration, and the coke oven gas after adsorption and removal of naphthalene is used as the hot blowing regeneration gas and There are several problems in cold blowing: 1) The coke oven gas after adsorption and rem...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10L3/08C10L3/10C10K1/00C10K1/20C10K1/32C10K1/34
CPCC10L3/08C10L3/106C10L3/101C10K1/004C10K1/20C10K1/32C10K1/002C10K1/34
Inventor 杨鹏朱圣华张满孙业新张帆许保明赵秀秀蒋家良张守强栾树龙倪维龙
Owner SD STEEL RIZHAO CO LTD
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