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Method for producing high-octane gasoline

A high-octane gasoline and catalyst technology, applied in the catalytic reforming of naphtha, etc., can solve the problems of high cost and high reaction temperature, and achieve the effects of increasing octane, reducing olefin content, and increasing aromatic content

Active Publication Date: 2012-08-08
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] BP and UOP have jointly developed a very representative light hydrocarbon aromatization process: Cyclar process (USP4642402), which uses mixed hydrocarbons as raw materials for aromatization to generate aromatics. The structuring product liquid yield is low (60%), and the cost of the catalyst is relatively high because it contains gallium

Method used

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  • Method for producing high-octane gasoline
  • Method for producing high-octane gasoline
  • Method for producing high-octane gasoline

Examples

Experimental program
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Effect test

Embodiment 1

[0025] The aromatization catalyst is ZSM-35 / MCM-22 eutectic molecular sieve, after being treated with water vapor at 550° C., the molecular sieve is impregnated with praseodymium nitrate solution so that the weight content of praseodymium is 1.5%. The aromatization reaction conditions are: reaction temperature 340°C, weight hourly space velocity 1.0h -1 , the reaction pressure is 1.5 MPa, and the ratio of C4 olefins to FCC gasoline is 16:84.

Embodiment 2

[0027] The aromatization catalyst is ZSM-5 / MCM-22 composite molecular sieve. After being treated with water vapor at 500°C, the molecular sieve is dipped in tungstic acid solution so that the weight content of tungsten is 2%. The aromatization reaction conditions are: reaction temperature 360°C, weight hourly space velocity 2.0h -1 , the reaction pressure is 1.5MPa, and the ratio of C4 olefins to FCC gasoline is 10:90.

Embodiment 3

[0029] The aromatization catalyst is Y molecular sieve. After being treated with water vapor at 550° C., cerium nitrate solution is impregnated on the molecular sieve to introduce 4% cerium. The aromatization reaction conditions are: reaction temperature 350°C, weight hourly space velocity 4.5h -1 , the reaction pressure is 2.0MPa, and the ratio of C4 olefins to FCC gasoline is 80:20.

[0030] The aromatization reactor that embodiment 4-6 adopts and mode of operation are as follows:

[0031] A simulated moving bed with three fixed bed reactors connected in series is used as the aromatization reactor. figure 2 A schematic diagram of the reaction. Three fixed-bed reactors 1, 2, 3, and 4 are used as product separation equipment. Each reactor is equipped with raw material inlet valve and inlet pipeline, product outlet valve and outlet pipeline, and a communication valve and communication pipeline are provided between each reactor and the next reactor, that is, the material can...

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Abstract

The invention provides a method for producing high octane gasoline by aromatization reaction of a mixed raw material of catalytic gasoline and C4, and catalyst on an aromatization reactor after the mixed raw material contacts the catalyst. The method is as follows: the catalytic gasoline is mixed with the C4 olefin, and the mixed raw material enters into a fixed bed aromatization reactor or a simulated moving bed aromatization reactor which is filled with the molecular sieve catalyst, contacts the aromatizing catalyst, and undergoes olefin aromatization reaction, wherein the reaction conditions are as follows: the reaction temperature is between 250 and 340 DEG C; the pressure is between 0.5 and 3.0 MPa; the weight space velocity is between 0.5 and 10h<-1>; the mass ratio of the C4 olefin to the catalytic gasoline is between 90 to 10 and 2 to 98; and active ingredients of a molecular sieve carrier of the catalyst are one or more than one among rare earth element, No. 4B element and No. 8 element, and the weight of the active ingredients is 0.01 to 10 percent of that of the carrier. The method can obviously reduce the olefin content of the raw gasoline, effectively improve the octane number, and achieve the aim of production of the clean high-octane gasoline.

Description

technical field [0001] The invention provides a method for producing high-octane gasoline by contacting the mixed raw materials of catalytic cracking gasoline and C4 olefins with a catalyst on an aromatization reactor for aromatization reaction. Background technique [0002] With the increasing awareness of environmental protection and the approaching of the "Green Olympics" in 2008, my country's requirements for gasoline standards are becoming more and more stringent, and the olefin content in gasoline has also been clearly limited. More than 80% of the catalytic cracking gasoline in my country has an olefin content of over 40% and an aromatic content of only about 10%, mainly using high-octane gasoline such as alkylated gasoline (iso-octane) or reformed gasoline (rich in aromatics fractions) However, the production capacity of olefin-free high-octane gasoline blending components in my country is very limited (catalytic reforming + isomerization + alkylation + etherification...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G35/04
Inventor 兰玲吴冠京付兴国马安吴培鞠雅娜
Owner PETROCHINA CO LTD
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