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Catalyst for preparing etherified benzine by etherifying catalytic cracking benzine, preparation method thereof and application thereof

A catalytic cracking and light gasoline technology, applied in catalyst activation/preparation, physical/chemical process catalysts, chemical instruments and methods, etc., can solve problems such as increasing catalyst costs, reduce vapor pressure, increase octane number, and save use Effect

Active Publication Date: 2012-07-11
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the preparation of zeolite-type catalysts requires the use of organic matter as a template, which will greatly increase the cost of the catalyst

Method used

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  • Catalyst for preparing etherified benzine by etherifying catalytic cracking benzine, preparation method thereof and application thereof
  • Catalyst for preparing etherified benzine by etherifying catalytic cracking benzine, preparation method thereof and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] 45g (NH 4 ) 2 SO 4 Dissolved in 100mL deionized water, 80g amorphous silica-alumina (Qingdao Ocean Chemical Group Co., silica-alumina gel, HY-W type, Al 2 o 3 The content is 17% by weight, SiO 2 The content is 83% by weight and the specific surface area is 534m 2 / g, the pore volume is 0.35mL / g, and the most probable pore diameter is 33.4 ) in it for 2 hours, filtered, dried at 70°C for 1 hour, dried at 90°C for 1 hour, dried at 120°C for 1 hour, then fired at 300°C for 1 hour in an air atmosphere, and then fired at 350°C Calcined at low temperature for 1 hour, at 450° C. for 1 hour, and at 600° C. for 2 hours to obtain 89.1 g of catalyst A1. Measured by chemical analysis method in catalyst A1, sulfur oxides as SO 4 2- The total amount is 10.1% by weight, based on the weight of catalyst A1.

[0046] Cutting the fraction from the initial boiling point to 75°C in catalytic cracking gasoline to obtain light gasoline fraction, wherein the content of olefins is 47....

Embodiment 2

[0051] Add 230g of 25% by weight silica sol solution into a 500mL beaker, add 5% hydrochloric acid solution dropwise at 50°C until the pH value is 4, and age for 2 hours, add 200mL of an aqueous solution containing 85g of aluminum sulfate into the beaker, and heat it at 50°C Stir under low temperature, then adjust the pH value to 9 with ammonia water, age for 3 hours, filter the formed precipitate and wash 5-8 times with 2000mL water, dry at 120°C for 4 hours, and roast at 500°C for 4 hours to obtain 82g of amorphous Si-alumina carrier (Al 2 o 3 The content is 30% by weight, SiO 2 The content is 70% by weight and the specific surface area is 509m 2 / g, the pore volume is 0.34mL / g, and the most probable pore diameter is 35 ).

[0052] 45g (NH 4 ) 2 SO 4 Dissolve in 100 mL of deionized water, impregnate 80 g of the above-prepared amorphous silica-alumina in it for 2 hours, filter, dry at 70 °C for 1 hour, at 90 °C for 1 hour, and at 120 °C for 1 hour, then in In an air ...

Embodiment 3

[0057] 13.5g (NH 4 ) 2 SO 4 Dissolve in 100mL of deionized water, immerse 80g of amorphous silicon aluminum (same as Example 1) in it for 2 hours, filter, dry at 70°C for 1 hour, at 90°C for 1 hour, and at 120°C for 1 hour , and then in an air atmosphere, calcined at 300°C for 1 hour, at 350°C for 1 hour, at 450°C for 1 hour, and at 600°C for 2 hours to obtain 82g of catalyst A3. Measured by chemical analysis method in catalyst A3, sulfur oxides as SO 4 2- 2.5% by weight, based on the weight of catalyst A3.

[0058] Catalyst A3 was used to etherify the light gasoline fraction with an initial boiling point of 75° C. in FCC gasoline, and the other reaction conditions were the same as in Example 1.

[0059] During the process of etherifying light gasoline to prepare etherified light gasoline, the conversion rate of C5 active olefins is 48.8%, and the conversion rate of C6 active olefins is 19%. The content of ether in the etherified light gasoline was 7.4% by weight, and th...

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Abstract

The invention relates to a catalyst for preparing etherified benzine by etherifying catalytic cracking benzine. The catalyst comprises an amorphous sliicon-alumininm carrier and sulfur oxide carried on the carrier. The invention also relates to a method for preparing the catalyst. The method comprises the following steps of: soaking the amorphous sliicon-alumininm carrier in ammonium sulfate solution, ammonium bisulfate solution, sulfuric acid solution or mixed solution of the ammonium sulfate solution, ammonium bisulfate solution and sulfuric acid solution; and drying and calcining the soaked amorphous sliicon-alumininm carrier in section. The invention also relates to a method for preparing etherified benzine by etherifying catalytic cracking benzine. The method comprises the step of contacting the mixed material of benzine and methanol with the catalyst. By the method, isoolefine which is contained in the benzine is stably etherified into ether in low cost, so the octane number of the benzine is increased, the vapor pressure of the benzine is reduced, and the consumption of additives with large octane number, such as methyl tert-butyl ether and the like, is also saved.

Description

technical field [0001] The invention relates to a catalyst for preparing etherified light gasoline by etherifying catalytically cracked light gasoline, a method for preparing the catalyst and an application of the catalyst in preparing etherified light gasoline by etherifying catalytically cracked light gasoline. Background technique [0002] At present, about 80% of motor gasoline in my country comes from catalytic cracking gasoline. FCC gasoline is very high in olefins. In order to meet the olefin content standard of less than 35% in GB 17930-1999 "Unleaded Gasoline for Vehicles", the C5-C6 active olefins in catalytic cracking light gasoline are usually etherified with methanol under the action of a catalyst to generate ether compounds. This can not only reduce the olefin content in gasoline, but also increase the octane number and oxygen content of gasoline, reduce the vapor pressure of gasoline, and improve its stability. [0003] The reported etherification reaction p...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/04B01J21/12B01J37/02C10G29/22
Inventor 贾志光栗同林雷鸣杨怀军庄书红赵岚
Owner CHINA PETROLEUM & CHEM CORP