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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 reactors need to be connected in series and operated at variable temperatures. At the same time, it will cause frequent switching regeneration or shutdown regeneration of the device, cumbersome operation, and there are products The quality is not stable, especially the dry gas yield increases greatly in the later stage of the product

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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