Preparation method and uses of condensate oil aromatization catalyst

A catalyst and aromatization technology, applied in physical/chemical process catalysts, isomerization hydrocarbon production, molecular sieve catalysts, etc., can solve the problems of unstable product quality, large increase in dry gas yield, and low liquid yield , to achieve long-term operation, improve the reaction and regeneration state, and reduce the effect of deep reaction

Inactive Publication Date: 2009-02-18
CHINA NAT OFFSHORE OIL CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Its shortcoming is that the raw material oil obtains 45-65% (accounting for the raw material oil weight) liquid after the first-stage reaction, the liquid yield is not high, and there are too many cracked products
However, if a fixed bed reactor is used, the aromatization catalyst is easily deactivated due to coke, and multiple rea

Method used

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  • Preparation method and uses of condensate oil aromatization catalyst
  • Preparation method and uses of condensate oil aromatization catalyst
  • Preparation method and uses of condensate oil aromatization catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Preparation of the catalyst of the present invention.

[0025] (1) Get 1500 grams of commercially available nanometer HZSM-5 molecular sieves with a silicon-aluminum ratio of 38, impregnate with 1000 milliliters of a solution containing 11.2 grams of chloroplatinic acid, then dry at 120° C. for 12 hours, and roast at 450° C. for 3 hours;

[0026] (2) Hydrothermal treatment: put the platinum-loaded molecular sieve in step (1) into a tubular reactor, raise the temperature to 520°C in air flow under normal pressure, then change to steam at this temperature for 8 hours, and then Dry air is introduced to purify and cool down, and the total water intake during the steam treatment process is 3000 grams;

[0027] (3) get 700 grams of aluminum sol (pH value is 3.0, containing aluminum oxide 21%), add 100 milliliters of deionized water, make binding agent, then (2) obtains the modified nanometer HZSM-5 molecular sieve, 250 grams of commercially available titanium dioxide and 200...

Embodiment 2

[0031] Prepare other several catalysts B, C by the method for embodiment 1, difference is to change the second metal type and content, be respectively B (nickel 5.0% by weight, use the solution 100 g that contains 26.5 grams of nickel nitrate in (4) step milliliter impregnation), C (5.0% by weight of cobalt, impregnated with 100 milliliters of solution containing 26.0 grams of cobalt nitrate in (4) step).

Embodiment 3

[0033] The catalyst was prepared according to the method of Example 1, except that the amount of pseudo-boehmite mixed with the nanometer HZSM-5 molecular sieve was 250 grams, and the rest of the carrier and metal content were unchanged, and catalyst D was obtained.

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Abstract

The invention discloses a preparation method and application of aromatization catalyst for gas condensate. The method is to load metal active components onto a nano molecular sieve, which comprises 0.1 to 10.0 weight percent of noble metal platinum, 1.0 to 10.0 weight percent of a second metal M, 89.0 to 98.9 weight percent of a carrier, wherein the carrier is composed of 60 to 90 weight percent of a nano HZSM-5 molecular sieve and titanium dioxide, the balance being aluminum oxide, the noble metal platinum is a fist active component. The catalyst is applicable to production of aromatic hydrocarbon through aromatization of gas condensate. With gas condensate as the raw material, benzene, toluene, xylene (BTX) together with a byproduct of 18 to 28 weight percent of high quality liquid gas are produced in a reactor of moving bed under the conditions of a total reaction pressure of between 0.5 and 2.0 Mpa, a temperature of between 400 and 580 DEG C, a weight space velocity of the raw material of between 0.5 and 4.0 h <-1>. The catalyst has high actively and selectivity anti-carbon capacity, reusability and high yield rate of aromatic hydrocarbon products.

Description

technical field [0001] The present invention relates to a preparation method and application of a condensate oil aromatization catalyst, more specifically, a condensate oil molecular sieve-loaded active metal aromatization catalyst and its preparation method, and using the catalyst to A method of aromatization of condensate. Background technique [0002] With the intensified development of petroleum and the large-scale exploitation of condensate oil and gas fields, a large amount of condensate oil products (C 3 —C 12 ), condensate is unfractionated liquid hydrocarbon recovered together with natural gas and oil field gas, it is a mixture of short-chain hydrocarbons and long-chain hydrocarbons, the yield of naphtha is usually 60~80% by weight, and the yield of diesel oil Usually 20~40m%. "West-to-East Gas Pipeline" is a major engineering project being carried out in China at the beginning of the 21st century. A large amount of natural gas condensate oil resources are obtain...

Claims

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Application Information

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IPC IPC(8): B01J29/44B01J29/46C07C5/31
CPCY02P20/584
Inventor 于海斌南军李孝国赵训志孙彦民姜雪丹
Owner CHINA NAT OFFSHORE OIL CORP
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