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Oxidative desulfurization process with continuously regenerated desulfurizer

A technology of oxidative desulfurization and desulfurization agent, applied in the direction of chemical instruments and methods, separation of dispersed particles, separation methods, etc., can solve problems such as air, water environment and water source pollution, difficulty in waste solvent treatment, human and environmental hazards, etc., to avoid Large fluctuations, improved service life, and no secondary pollution

Active Publication Date: 2016-08-17
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] Although the waste desulfurizers treated by the above methods can be put into use again, these methods have a large workload and cumbersome operations. The organic solvents used have serious harm to the human body and the environment, and can cause pollution to the air, water environment and water sources. It is also difficult to deal with

Method used

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Examples

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Effect test

Embodiment 1

[0039] Properties of desulfurizer: commercially available W701 type iron oxide desulfurizer, Φ3~5×(3~15)mm round bar shape, bulk density 0.8~0.9g / ml, average radial crushing strength / N cm -1 ≥50.

[0040] The distillation range of catalytic cracking diesel oil is 240~260°C; in the solid-liquid separator: the temperature for cooling and separating sulfur is 10°C.

Embodiment 2

[0044] Properties of desulfurizer: Prepare amorphous iron oxyhydroxide desulfurizer according to CN101898108A, containing 97wt% amorphous iron oxyhydroxide, spherical shape of Φ8~10mm, bulk density of 0.9~1.0g / ml, average crush resistance of particle points / N· Pieces ≥ 30.

[0045] The distillation range of catalytic cracking diesel oil is 260~280°C; in the solid-liquid separator: the temperature for cooling and separating sulfur is 8°C.

Embodiment 3

[0049] Desulfurizer properties: commercially available TC-22 zinc oxide desulfurizer, Φ4×(4~10)mm round bar shape, bulk density 0.9~1.1g / ml, average radial crushing strength / N cm -1 ≥40. The distillation range of catalytic cracking diesel oil is 300~330°C; in the solid-liquid separator: the temperature for cooling and separating sulfur is 10°C.

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Abstract

The invention discloses an oxidative desulfurization process in which the desulfurizer can be continuously regenerated, which is characterized in that it comprises the following content: in a fixed bed reactor, hydrogen sulfide-containing gas, oxygen-containing gas and the desulfurizer are in contact with the desulfurizer bed to perform oxidative desulfurization And the desulfurization agent regeneration reaction, the purified gas is discharged from the top of the reactor, and the catalytic cracking diesel oil is introduced during the reaction process to dissolve the elemental sulfur generated by the regeneration reaction, and the catalytic cracking diesel oil dissolved in the elemental sulfur flows out of the reactor, and after solid-liquid separation recycle. The process has high desulfurization precision, long service life of desulfurizer, simple operation and low cost.

Description

technical field [0001] The invention relates to an oxidation desulfurization process in which a desulfurizer can be continuously regenerated. Background technique [0002] With the increasing development of the chemical synthesis industry, the consumption of industrial raw gas, various coal gases, natural gas, and synthetic raw material gas has increased significantly, and the environmental protection standards have become increasingly stringent. More stringent requirements have been put forward for various industrial and civil gas sources. Requirements, that is, the process gas must be effectively purified before industrial and civil applications, especially the removal of sulfur-containing gases, among which the removal of hydrogen sulfide is particularly important. [0003] At present, there are many methods for removing hydrogen sulfide at home and abroad, mainly including wet method and dry method. Wet desulfurization is generally suitable for raw materials with high s...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/96B01D53/82B01D53/52
Inventor 刘淑鹤方向晨韩建华程明珠
Owner CHINA PETROLEUM & CHEM CORP
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