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Non-hydrogenation aromatization upgrading method for naphtha

An aromatization and non-hydrogenation technology, which is applied in the catalytic reforming of naphtha, naphtha treatment, petroleum industry, etc., can solve the problems of reducing the dry point and high end boiling point of aromatized modified gasoline, and achieves Effects of reducing dry point, improving quality and reducing pollution

Active Publication Date: 2012-12-12
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0013] The method of the present invention takes naphtha or naphtha and mixed carbon four as raw materials, carries out aromatization modification, and then adsorbs the modified gasoline with the adsorbent described in the present invention to remove the carbon dioxide in the modified gasoline. High boiling point products, thereby greatly reducing the dry point of aromatized gasoline, especially after the naphtha is mixed with mixed carbon four for aromatization, it can effectively solve the problem of heavy components in the obtained modified gasoline. The problem of excessively high final boiling point caused by the excessive use of carbon four fractions can not only improve the quality of modified gasoline, but also obtain gasoline products that meet national standards, thereby reducing the pollution caused by automobile exhaust. Naphthalene series compounds used in the production of chemical products such as phthalic anhydride, synthetic resin, and plant growth hormone can be obtained

Method used

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  • Non-hydrogenation aromatization upgrading method for naphtha
  • Non-hydrogenation aromatization upgrading method for naphtha
  • Non-hydrogenation aromatization upgrading method for naphtha

Examples

Experimental program
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Effect test

example 1

[0034] Prepare the adsorbent of the present invention.

[0035] (1) Preparation of LiY molecular sieve: Take 100 grams of Y-type zeolite (produced by Zhoucun Catalyst Factory of Qilu Petrochemical Company), ion-exchange with a LiCl solution with a concentration of 0.1mol / L for 5 hours, and then wash with deionized water until there is no Cl in the washing liquid - , Dry at 110°C for 6 hours, and bake at 500°C for 3 hours. The above ion exchange was repeated three times to obtain LiY zeolite.

[0036] (2) Prepare adsorbent: mix LiY zeolite and aluminum hydroxide powder (produced by German Condea company, brand SB) at a mass ratio of 69:31, add deionized water and 1% nitric acid accounting for about 45% of solid mass, and knead After extrusion, it was dried at 110°C for 10 hours and calcined at 500°C for 4 hours to obtain Adsorbent A, which contained 75% by mass of LiY zeolite and 25% by mass of γ-alumina.

example 2

[0038] Prepare adsorbent B by the method for example 1, difference is that (1) step is the NaCl solution ion-exchange X type zeolite (Qilu Petrochemical Company Zhoucun Catalyst Factory production) of 0.1mol / L with concentration; (2) step prepares adsorption The mass ratio of NaX zeolite and aluminum hydroxide powder added to the agent was 60:40, and the prepared adsorbent B contained 67% by mass of NaX zeolite and 33% by mass of γ-alumina.

example 3

[0040] The adsorbent was prepared according to the method of Example 1, except that in the step (1), the mixed solution of LiCl and NaCl with a mass ratio of lithium oxide and sodium oxide of 75:25 was used to perform ion exchange on X-type zeolite to obtain LiNaX zeolite. Get LiNaX zeolite and aluminum hydroxide powder and mix by the mass ratio of 65: 35, press the method for example 1 (2) step to knead then extrude, dry, roast, contain LiNaX zeolite 72 mass %, 28% by mass of γ-alumina.

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PUM

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Abstract

The invention relates to a method for reforming naphtha non-hydrogasification aromatization, which comprises the following steps: naphtha contacts with reforming catalyst to perform the aromatization reforming reaction under the condition of non-hydrogasification, the obtained reforming product contacts with sorbent and adsorbs naphthaline series compound therein, and then strippant is used for desorbing the naphthaline series compound adsorbed in the sorbent, the strippant is separated from the naphthaline series compound by fractionation separation, and the sorbent comprises 55-80 percent of lithium by mass and / or sodium modified faujasite and 20-45 percent of caking agent by mass. The method can effectively remove heavy components in the aromatization reforming liquid product, lowers the end point of distillation and can obtain the naphthaline series compound with higher purity.

Description

technical field [0001] The invention relates to a method for non-hydroaromatization modification of naphtha, in particular to a method for improving the properties of a liquid product of non-hydroaromatization modification of naphtha. Background technique [0002] At present, FCC gasoline accounts for about 80% of my country's finished gasoline, and the olefin content of conventional FCC gasoline is as high as 50-55%. Content ≯35% standard. Therefore, the production of clean gasoline blending components with high octane number and low olefin content has become an urgent need for refineries. At present, the method of producing high-octane clean gasoline blending components in my country is mainly catalytic reforming. Due to the shortage of raw materials, many catalytic reforming units cannot operate at full capacity. [0003] In recent years, due to the discovery of ZSM-5 shape-selective zeolite, naphtha and / or low-carbon hydrocarbons can be converted into gasoline blending ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G61/06C10G35/06
Inventor 赵雅郡任坚强于中伟孟宪波陈春芳
Owner CHINA PETROLEUM & CHEM CORP
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