Gas hydrogenation catalyst sulfurization and sulfurization waste gas treatment and emission process

A hydrogenation catalyst and waste gas treatment technology, applied in the field of coal chemical industry, can solve the problem of being reduced before vulcanization, and achieve high utilization efficiency, short vulcanization time, and good vulcanization effect

Active Publication Date: 2020-11-03
WUHAN KELIN FINE CHEM
View PDF4 Cites 2 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0015] Aiming at the deficiencies in the prior art, the present invention provides a gas hydrogenation catalyst sulfidation and sulfidation waste gas treatment and discharge process, which adopts intermediary installation between the catalyst and the pre-sulfurization catalyst outside the device to solve the problem of centralized heat release and sulfur release when the pre-sulfurization catalyst outside the device is activated And avoid the problem of the catalyst being reduced before sulfidation; the sulfidation process contains H 2 The S waste gas enters the heating furnace for combustion, and the heat is used for heating, and the flue gas is converted to SO by the dry flue gas desulfurization device. 2 Removal to 30mg / m 3 The following and discharged after bleaching treatment

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Gas hydrogenation catalyst sulfurization and sulfurization waste gas treatment and emission process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0041] Sulfurization of 50 m in a coke oven gas to synthetic natural gas plant in Xinjiang 3 Primary hydrogenation. The volume ratio of the catalyst to the external presulfurized catalyst is 8:7, respectively 26.7 m 3 and 23.3 m 3 , the total number of layers in the room is 15 layers, and each layer is filled with 3.3 m 3 . The external presulfided catalyst is prepared by dry method, and the degree of sulfidation is 70%. Vulcanizing agent is CS 2 , prepare 2.02 tons. Replace flue gas desulfurizer 7.31 m 3 , The sulfur capacity of the flue gas desulfurizer is 31%. SO in exhaust flue gas 2 less than 30mg / m 3 , no white smoke is generated. The specific vulcanization process is as follows:

[0042] (1) Use a heating furnace to heat nitrogen to raise the temperature of the catalyst at a heating rate of 20°C / h, and control the temperature of each point of the bed to not exceed 200°C , Control the pressure at 0.1MPa, raise the temperature for 9 hours to 200°C in the upper...

Embodiment 2

[0048] Sulfurization of 18.7 m in a coke oven gas to methanol plant in Shaanxi 3 Prehydrogenation. The volume ratio of the catalyst to the external presulfurized catalyst is 3:2, respectively 11.2 m 3 and 7.5 m 3 , the total number of layers in the room is 5 layers, and each layer is filled with 3.7m 3 . The presulfurized catalyst outside the device is prepared by wet method, and the degree of sulfidation is 40%. The vulcanizing agent is dimethyl disulfide, and 0.94 tons are prepared. Replace flue gas desulfurizer 2.85 m 3 , Flue gas desulfurization agent sulfur capacity 30%. SO in exhaust flue gas 2 less than 30mg / m3 , no white smoke is generated. The specific vulcanization process is as follows:

[0049] (1) Use a heating furnace to heat nitrogen to raise the temperature of the catalyst at a heating rate of 30°C / h, and control the temperature of each point of the bed to not exceed 200°C , The pressure is controlled at 0.2MPa; after 6 hours, the temperature of the u...

Embodiment 3

[0055] Sulfurization of 29 m in a coke oven gas to synthetic natural gas plant in Hebei 3 Primary hydrogenation. The loading volume ratio of the catalyst to the external presulfurized catalyst is 5:4, respectively 16.1 m 3 and 12.9 m 3 , the total number of layers in the room is 9 layers, and each layer is filled with 3.2m 3 . The external presulfided catalyst is prepared by dry method, and the degree of sulfidation is 55%. Vulcanizing agent is CS 2 , prepare 1.31 tons. Replace flue gas desulfurizer 4.74 m 3 , The sulfur capacity of the flue gas desulfurizer is 32%. SO in exhaust flue gas 2 less than 30mg / m 3 , no white smoke is generated. The specific vulcanization process is as follows:

[0056] (1) Use a heating furnace to heat nitrogen to raise the temperature of the catalyst at a heating rate of 25°C / h, and control the temperature of each point of the bed to not exceed 200°C , The pressure is controlled at 0.15MPa; after 7.2 hours, the temperature of the upper...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention discloses a gas hydrogenation catalyst sulfurization and sulfurization waste gas treatment and emission process, wherein the problems of concentrated heat release and sulfur release during activation of the out-of-device pre-sulfurized catalyst and reduction of the catalyst before sulfurization are solved by adopting the catalyst and the out-of-device pre-sulfurized catalyst. The total interlayer number is an odd number of 5-15, wherein the uppermost layer and the lowermost layer are both catalysts, in the initial stage of sulfurization, the first layer of catalyst is supplied with sulfur and heat by a system, and the rest odd layers of catalysts are respectively supplied with sulfur and heat by an out-of-reactor pre-sulfurized catalyst on the upper layer; the sulfuration waste gas enters a heating furnace to be combusted, SO2 in the flue gas is removed to 30 mg/m3 or below through a dry flue gas desulfurization device, and the flue gas is discharged after being subjectedto white smoke removal treatment. The sulfurization process is simple in flow, free of pollution and corrosion of power, heat exchange, condensation, gas-liquid separation and other equipment, smallin sulfurization agent dosage, short in sulfurization time and good in sulfurization effect. The whole sulfurization and sulfurization waste gas treatment and discharge process is low in investment cost, solid waste after flue gas desulfurization can be recycled, and the process is green and economical.

Description

technical field [0001] The invention relates to a gas hydrogenation catalyst sulfidation and sulfidation waste gas treatment and discharge process, which belongs to the field of coal chemical industry. Background technique [0002] my country is a big country of coke production, and a large amount of coke oven gas is produced as a by-product. The production of methanol / LNG from coke oven gas has a good application prospect. Methanol synthesis catalysts and methanation catalysts are used in the production of methanol and LNG. The active components are Cu and Ni respectively, which are easily deactivated by reaction with sulfide. Therefore, it is of great significance to remove various sulfides in coke oven gas. [0003] The sulfur content in coke oven gas is related to the total sulfur content of the coal charge. Generally, dry coal contains 0.5-1.2% (weight) of total sulfur, of which 20-45% is transferred to coke oven gas, and hydrogen sulfide accounts for the total sulfur...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): C10K1/00C10K1/34B01D53/50B01D53/81B01D46/00
CPCB01D46/00B01D53/508B01D53/81B01D2251/404B01D2251/604B01D2258/0283C10K1/004C10K1/34
Inventor 王天元王泽王国兴张先茂金建涛李兴建赵志杰夏克勤张晓平
Owner WUHAN KELIN FINE CHEM
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products