Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Method for desulfuration by recombination alkylate catalytic distillation

A catalytic distillation and alkylation technology, used in hydrocarbon distillation, petroleum industry, refined hydrocarbon oil, etc., can solve the problems of insufficient boiling point of alkylthiophene derivatives, poor sulfur transfer effect, and separation of low-carbon olefins, etc. Mild operating conditions, small construction investment, and the effect of increasing the boiling point

Active Publication Date: 2009-12-09
PETROCHINA CO LTD
View PDF7 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

None of the existing technologies separate low-carbon olefins from low-boiling point thiophene sulfides. In this case, low-carbon olefins can easily react with low-boiling point thiophene sulfides to occupy the substitution position, and the resulting alkylthiophene derivatives The boiling point of the substance is not high enough, so the sulfur transfer effect is not good

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
  • Method for desulfuration by recombination alkylate catalytic distillation
  • Method for desulfuration by recombination alkylate catalytic distillation
  • Method for desulfuration by recombination alkylate catalytic distillation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] combined with figure 1 , the process of the present invention is further described.

[0030] The catalytic distillation tower is divided into four parts: an upper reaction section 31 , a lower reaction section 32 , a rectification section 33 and a stripping section 34 . The FCC gasoline raw material is connected to the preprocessor 10 through the pipeline 101 , and then connected to the flash tank 20 through the pipeline 102 . The top of the flash tank is connected to the bottom of the reaction section of the catalytic distillation tower 30 through a pipeline 103 , and the C3-C5 olefin raw material is connected to the bottom of the reaction section through a pipeline 106 . The bottom of the flash tank is connected with the upper reaction section 31 and the lower reaction section 32 of the catalytic distillation column 30 through the pipeline 104 . The top of the tower is connected to the total condenser through the pipeline 201, and the pipeline 202 is connected to th...

Embodiment 2

[0034] Knot and attach figure 2 , the process of the present invention is further described.

[0035] The catalytic distillation tower 30 is divided into four parts: an upper reaction section 31 , a lower reaction section 32 , a rectification section 33 and a stripping section 34 . The FCC gasoline raw material is connected to the preprocessor 10 through the pipeline 101 , and then connected to the flash tank 20 through the pipeline 102 . The flash tank is connected to the bottom of the reaction section of the catalytic distillation tower through a pipeline 103 , and the C3-C5 olefin raw material is connected to the bottom of the reaction section through a pipeline 106 . The bottom of the flash tank is connected with the upper reaction section 31 and the lower reaction section 32 of the catalytic distillation column 30 through the pipeline 104 . The top of the tower is connected to the total condenser through the pipeline 201, and the pipeline 202 is connected to the outlet...

Embodiment 3

[0039] combined with image 3 , the process of the present invention is further described.

[0040] The catalytic distillation tower is divided into six parts: a rectification section 33 , a stripping section 34 , an upper reaction section 31 , an upper reaction section 2 35 , a lower reaction section 32 , and an intermediate fractionation section 36 . The FCC gasoline raw material is connected to the preprocessor 10 through the pipeline 101 , and then connected to the prefractionator 50 through the pipeline 102 . The top of the prefractionation tower is connected to the bottom of the reaction section of the catalytic distillation tower 30 through a pipeline 103 , and the C3-C5 olefin raw material is connected to the bottom of the reaction section through a pipeline 106 . The bottom of the pre-fractionation tower is connected with the upper reaction section 2 35 and the lower reaction section 32 of the catalytic distillation tower 30 through a pipeline 104 . The top of the t...

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 relates to a method for desulfuration by recombination alkylate catalytic distillation. Gasoline material to be desulfurized is separated into a light distillate and a heavy distillate, and the light distillate and the heavy distillate are respectively led to different positions of a catalytic distilling tower, wherein a feed inlet of the light distillate is lower than a feed inlet of the heavy distillate; solid acid catalyst is filled in the catalytic distilling tower, wherein the operation pressure of the catalyst distilling tower is 0.1MPa to 0.5 MPa, the temperature of a reaction area is 80-200 EDG C, and the airspeed of liquid is 0.1h-1 to 20h-1; olefin contained in the gasoline is fully utilized to react with the sulphocompound in the gasoline so as to remarkably improve the boiling point of the sulphocompound, enable the sulfur transfer degree to be higher, effectively remove the sulfur in the gasoline without losing the octane number and achieve the double purposes desulfuration and olefin reduction. The method also has the advantages of little constructing investment, mild operating condition and easy control of the process.

Description

technical field [0001] The invention relates to a desulfurization method using olefin contained in gasoline as an alkylating agent. Background technique [0002] At present, catalytic cracking (FCC) gasoline accounts for more than 75% of gasoline in my country, and brings more than 90% of sulfur impurities into finished gasoline. Therefore, the production of clean gasoline products requires a substantial reduction in the sulfur content of FCC gasoline. Among the sulfides contained in FCC gasoline, mercaptans and thioethers are less, and thiapanes account for more than 80% of the total sulfides. Hydrodesulfurization (HDS) is a widely used FCC gasoline desulfurization technology at present. It can remove many kinds of sulfides and high reaction conversion rate, but the olefins in the light fraction are easily saturated at the same time, which reduces the octane number of gasoline. Alkylation desulfurization refers to contacting gasoline with an acidic catalyst, so that the t...

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): C10G7/00C10G29/00
Inventor 李永红沈昕伟张铁珍刘文勇韩志波贾云刚石宏伟
Owner PETROCHINA CO LTD
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products