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Inferior gasoline non-hydrogen modification method

A non-hydrogen-modified, inferior gasoline technology, applied in the petroleum industry, processing hydrocarbon oil, reforming naphtha, etc., can solve the problems of high reaction temperature, high yield of cracked gas, low olefin conversion rate, etc. The effect of enhanced stability, low reaction temperature and high yield of product liquid

Active Publication Date: 2017-05-17
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In 2011, the total output of MTBE in my country has exceeded 4.5 million tons, while the average operating rate of domestic MTBE devices is only 60%. The insufficient supply of raw material isobutylene has become the bottleneck of the development of MTBE industry.
If the existing technical scheme is used in the non-hydrogenation reforming reaction of by-product gasoline in the process of n-butene skeletal isomerization, the required reaction temperature is relatively high, which will inevitably lead to an excessively high yield of cracked gas and reduce the yield of product gasoline
If the existing catalyst is used for the reaction at low temperature (below 300°C), due to the relatively low acid strength of the catalyst, the ideal conversion rate cannot be met, and there are disadvantages of low olefin conversion rate and small increase in octane number of the product

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] The specific preparation process of modified ZSM-5 molecular sieve F1 is as follows: (1) 5.7 g of zirconyl nitrate and 0.7 g of chloroiridic acid were dissolved in 22 ml of deionized water, and the obtained saline solution was added to 650 ml of n-hexane solvent, Stirring was continued for 1 hour to form a suspension A1. Add 114.5 g of Si / Al molar ratio 76, pore volume 0.19 cm to suspension A1 3 / g hydrogen ZSM-5 molecular sieve, stirred at room temperature (25°C) for 2 hours to obtain slurry B1. (2) Place the slurry B1 in a rotary evaporator, evaporate the n-hexane solvent to dryness, and obtain dry glue C1, dry it at room temperature (25°C) for 24 hours, dry it at 120°C for 12 hours, and then bake it at 550°C for 5 hours, ZSM-5 molecular sieve D1 containing zirconium and iridium was obtained. (3) Transfer D1 into 500 ml of 0.1 mol / L ammonium sulfate solution and soak for 5 hours. After the required soaking time is reached, filter out the ammonium sulfate solution an...

Embodiment 2

[0030] The specific preparation process of modified ZSM-5 molecular sieve F2 is as follows: (1) 7.7 g of zirconyl nitrate and 0.2 g of chloroiridic acid were dissolved in 26 ml of deionized water, and the resulting saline solution was added to 520 ml of cyclohexane solvent , stirring continuously for 1 hour to form suspension A2. Add 113.0 g of Si / Al molar ratio 54, pore volume 0.23 cm to suspension A2 3 / g hydrogen ZSM-5 molecular sieve, stirred at room temperature (25°C) for 2 hours to obtain slurry B2. (2) Place the slurry B2 in a rotary evaporator and evaporate the cyclohexane solvent to obtain dry glue C2, dry it at room temperature (25°C) for 24 hours, dry it at 120°C for 12 hours, and then bake it at 500°C After 10 hours, ZSM-5 molecular sieve D2 containing zirconium and iridium was obtained. (3) Transfer D2 into 500 ml of 0.5 mol / L ammonium sulfate solution and soak for 1 hour. After the required soaking time is reached, filter out the ammonium sulfate solution and r...

Embodiment 3

[0032] The specific preparation process of modified ZSM-5 molecular sieve F3 is as follows: (1) 9.3 g of zirconyl nitrate and 1.1 g of chloroiridic acid were dissolved in 23.7 ml of deionized water, and the resulting saline solution was added to 950 ml of cyclohexane solvent , stirring continuously for 1 hour to form suspension A3. Add 114.5 g of Si / Al molar ratio 93, pore volume 0.21 cm to suspension A3 3 / g hydrogen ZSM-5 molecular sieve, stirred at room temperature (25°C) for 2 hours to obtain slurry B3. (2) Place the slurry B3 in a rotary evaporator and evaporate the cyclohexane solvent to obtain dry glue C3, dry at room temperature (25°C) for 24 hours, dry at 120°C for 12 hours, and then bake at 530°C After 10 hours, ZSM-5 molecular sieve D3 containing zirconium and iridium was obtained. (3) Transfer D3 into 500 ml of 0.3 mol / L sulfuric acid solution and soak for 3 hours. After the required soaking time is reached, filter out the sulfuric acid solution and rinse the mol...

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Abstract

The invention discloses an inferior gasoline non-hydrogen modification method. Under the non-hydrogen modification condition, an inferior gasoline material successively passes through an ZSM-22 molecular sieve based catalyst bed and a modified ZSM-5 molecular sieve based catalyst bed, wherein filling mass ratio of a ZSM-22 molecular sieve based catalyst to a modified ZSM-5 molecular sieve based catalyst is 1:1-1:3. According to the non-hydrogen modification condition, reaction temperature is 200-400 DEG C, reaction total-pressure (absolute pressure) is 0-0.50 MPa and weight space velocity is 0.5-10 h<-1>. The method of the invention has advantages of low reaction temperature, high liquid yield of products and high octane number.

Description

technical field [0001] The invention relates to a method for non-hydrogenation upgrading of low-quality gasoline, more specifically, the invention relates to a non-hydrogenation method for by-product gasoline in the process of producing isobutene through n-butene skeletal isomerization. Background technique [0002] As the market demand for high-octane gasoline continues to grow, so too does the need for the incorporation of methyl tert-butyl ether (MTBE) as an octane booster. In 2011, the total output of MTBE in my country has exceeded 4.5 million tons, while the average operating rate of domestic MTBE devices is only 60%. The insufficient supply of raw material isobutylene has become the bottleneck of the development of MTBE industry. [0003] With the lightening of ethylene cracking raw materials, and the impact of ethane cracking route and methanol to olefins project. In recent years, the output of cracking raffinate C4, which is the main source of isobutene, has been d...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G35/095
CPCC10G35/095C10G2300/1037C10G2300/1044C10G2400/02
Inventor 周峰马会霞乔凯
Owner CHINA PETROLEUM & CHEM CORP