Method and device for lye extraction desulfurization

A lye extraction and lye technology, applied in the direction of refining with alkaline aqueous solution, etc., can solve the problems of difficult release, inability to achieve, and the desulfurization effect is not obvious, and achieve the effect of promoting separation

Active Publication Date: 2007-07-04
CHINA PETROLEUM & CHEM CORP +1
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AI Technical Summary

Problems solved by technology

However, it must be noted that in the prior art, especially in practical applications, the content of mercaptans absorbed into the lye changes accordingly due to changes in the content of mercaptans in the hydrocarbon stream. Alkali regeneration is complete, and it is usually necessary to inject an oxidizing gas much higher than the theoretical meter into the oxidation system, and the excess oxidizing gas usually flows into the phase separation system together with the alkali solution, and it is difficult to completely release it in the phase separation system
[0007] This leads to two defects: one is that the oxidizing gas flowing into the phase separation system is easy to form bubbles in the lye, which affects the settlement and separation of the regenerated lye and the disulfide phase or the solvent phase containing disulfide, making the regenerated lye Disulfides or disulfide-containing solvents ar...

Method used

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  • Method and device for lye extraction desulfurization
  • Method and device for lye extraction desulfurization

Examples

Experimental program
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Embodiment 1

[0041] The hydrocarbon stream to be desulfurized is FCC gasoline fraction, and its basic properties are shown in Table 1. Among them, the determination of sulfur content adopts microcoulomb method, and the determination of thiol adopts potentiometric titration method.

[0042]

raw material

Distillation range (℃)

Sulfur content (ppm)

Mercaptan sulfur content

(ppm)

FCCG1

33~98

139

71

FCCG2

34~114

73

20

[0043] The hydrocarbon streams FCCG1 and FCCG2 in Table 1 were desulfurized using the flow chart shown in FIG. 1 . A NaOH solution with a concentration of 15% (weight) is used, and the content of sulfonated cobalt phthalocyanine in the alkali solution is 100 ppm. In the extraction system, the volume ratio of alkali liquor to hydrocarbon stream is 1:9, the temperature is normal temperature, and the pressure is 0.50MPa. In the oxidation system, the injection volume of ai...

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Abstract

The invention provides a method and device for desulfurization from hydrocarbon flow thorough alkaline liquid suction. It is to add a gas- removal system between oxidation system and phase separation system, and introduce inert gas into gas- removal system to exchange oxidative gas and then effectivelyt promote the separation of sulfur dioxide or sulfur dioxide- containing solvent from regenerative alkaline liquid in phase separation system, and the thiol in hydrocarbon flow can be inhibited from oxidation by oxidative gas in suction system, which enables thorough desulfurization by alkaline liquid suction.

Description

technical field [0001] The invention belongs to the refining field of hydrocarbon materials. Specifically, the present invention relates to a method and equipment for desulfurizing hydrocarbon material fluids, ie hydrocarbon streams, through alkaline extraction. Background technique [0002] Alkaline extraction is a traditional method for refining hydrocarbon materials, widely used in the sweetening and refining of hydrocarbon materials such as liquefied petroleum gas, gasoline, diesel oil, naphtha, alkanes, and olefins. The method is to contact the fluid of the hydrocarbon material, that is, the hydrocarbon stream with the lye, and the mercaptan in the hydrocarbon stream is removed from the oil by reacting with the lye to form mercaptide. [0003] If the lye containing mercaptide is discharged directly, it is neither economical nor environmentally friendly. Oxidation is usually used to oxidize mercaptides into disulfides so that the lye containing mercaptides is regenerat...

Claims

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Application Information

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IPC IPC(8): C10G19/02
Inventor 潘光成陶志平吴明清李涛董伟张红霞张小云
Owner CHINA PETROLEUM & CHEM CORP
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