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Preparation method and application of catalyst for isopropanol prepared through propylene hydration

A technology of isopropanol and catalyst, applied in the field of catalysis, can solve the problems of high raw material price, complicated reaction process, and high equipment requirements, achieve high activity and selectivity, simple preparation process, and improve the effect of catalytic activity.

Inactive Publication Date: 2017-07-07
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

U.S. Patent No. 4499313 uses the direct hydration method of propylene to prepare isopropanol. H-type mordenite and Y-type zeolite are used as catalysts to carry out liquid-phase direct hydration to prepare isopropanol. The reaction temperature is 160 ° C, the reaction pressure is 10 MPa, and the conversion rate is 18%. In addition, U.S. Patent US5012014 uses beta zeolite as a catalyst. At a reaction temperature of 200°C and a reaction pressure of 7.0 MPa, the conversion rate is above 8.0%. High requirements for equipment
The world patent WO2008147596 uses metal oxides as catalysts to prepare isopropanol by direct hydration. The reaction temperature is 200-250°C, the reaction pressure is 6.8MPa, and the conversion rate can reach up to 17.9%. Catalyst preparation costs are high
Chinese patent CN103880591 adopts propylene indirect hydration method to prepare isopropanol, with propylene and acetic acid as raw materials, reaction temperature 40~120 ℃, reaction pressure 3.75~10.0MPa, carry out liquid phase addition esterification to generate isopropyl acetate; generated acetic acid Under the action of Cu-based catalyst, isopropyl ester is hydrogenated to generate isopropanol and ethanol at a reaction temperature of 200-280°C and a reaction pressure of 3.0-18.0 MPa. The catalyst of this method has high activity and high selectivity, but the reaction process is complicated and the catalyst preparation Complex process and high reaction pressure
Chinese patents CN103539635 and CN103706377 have developed nickel-based catalysts and platinum-based catalysts respectively. This method has the advantages of high catalyst activity and good selectivity, but is greatly affected by the price of acetone and is subject to certain restrictions in industrial applications.

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  • Preparation method and application of catalyst for isopropanol prepared through propylene hydration
  • Preparation method and application of catalyst for isopropanol prepared through propylene hydration

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preparation example Construction

[0028] The invention provides a kind of preparation method of the catalyst of hydration of propylene isopropanol, comprising the following steps:

[0029] Step 1: Etching and expanding the pores of the carrier with a substance containing HF, then filtering, washing with water, and drying at a drying temperature of 100-200° C. and a drying time of 3-15 hours to obtain a pore-expanding carrier;

[0030] Step 2, placing the pore-expanding carrier in a 10-85 wt% phosphoric acid solution, immersing it for 1-10 hours, filtering, and drying at a drying temperature of 70-200°C and a drying time of 3-15 hours to obtain a once-immersed phosphoric acid catalyst;

[0031] Step 3, impregnating the once-impregnated phosphoric acid catalyst in 10-85wt% phosphoric acid solution, impregnating, impregnating for 2-10 hours, filtering, drying, the drying temperature is 70-200°C, and the drying time is 3-15 hours to obtain phosphoric acid groups catalyst.

[0032] The present invention also provi...

Embodiment 1

[0047] (1) Weigh 10 g of silicon macrospheres (purchased from Nanjing Heyi Chemical Co., Ltd.) and dip them in 0.4% HF solution for 4 hours, filter, wash, and dry at 150° C. for 4 hours.

[0048] (2) Get 3.5g of catalyst after hole expansion, impregnate in 50wt%H 3 PO 4In the solution, immerse for 7 hours, filter, and dry. The drying temperature is 70° C., constant temperature for 7 hours, and then 150° C. for 3 hours to obtain a phosphoric acid impregnated catalyst, which contains 49wt% phosphoric acid and 51wt% silicon macrospheres.

[0049] (3) Take 3.5g of phosphoric acid catalyst soaked once and soak it in 50% H 3 PO 4 The solution was soaked for 7 hours, filtered and dried at a constant temperature of 70°C for 7 hours, then dried at 150°C for 3 hours to obtain the final catalyst, which contained 57wt% phosphoric acid and 43wt% silicon macrospheres.

[0050] (4) Get once soaked phosphoric acid catalyst 2.0g and place in fixed-bed reactor, feed propylene and water in fi...

Embodiment 2

[0053] It has the same steps as in Example 1, except that the concentration of the HF solution is 0.6%, and the result of the catalyzed reaction by soaking the phosphoric acid catalyst once is that the conversion rate of propylene is 4.15%, and the selectivity of isopropanol is 97.9%. The final catalytic reaction result of the catalyst is that the conversion rate of propylene is 4.93%, and the selectivity of isopropanol is 99.2%.

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Abstract

The invention discloses a preparation method of a catalyst for isopropanol prepared through propylene hydration. The preparation method includes step 1, etching and broaching a carrier by an HF-containing material, and performing filtration, washing and drying to obtain a broached carrier; step 2, putting the broached carrier into a 10-85wt% of phosphoric acid solution, and performing impregnation, filtration and drying to obtain a primary phosphoric-acid-impregnated catalyst; step 3, impregnating the primary phosphoric-acid-impregnated catalyst with the 10-85wt% of phosphoric acid solution, and performing impregnation, filtration and drying to obtain the phosphate catalyst. The invention further discloses a method for preparing the isopropanol through propylene hydration. The catalyst has high activity and selectively, and the conversion rate is close to a theoretical value and reaches a high level; the catalyst has the advantages of simplicity in preparation, low cost, stable performance and the like, and is suitable for industrial large-scale production.

Description

technical field [0001] The invention relates to a catalyst for preparing isopropanol and its preparation and application, belonging to the technical field of catalysis. Background technique [0002] Isopropanol is an important chemical product and chemical raw material, which is widely used in the fields of pharmaceuticals, organic raw materials, solvents, fragrances, cosmetics, plastics and coatings. In recent years, the coal chemical industry has developed rapidly. The technology of converting coal-to-synthesis gas to methanol to produce olefins is mature. The demand for downstream products of propylene cannot keep up with the expansion speed of propylene production capacity, resulting in excess propylene production and a shortage of isopropanol market. The direct hydration of raw materials to produce isopropanol can relieve the market pressure of propylene and isopropanol at the same time. [0003] At present, the preparation process of isopropanol is mainly propylene hy...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/16B01J29/00B01J37/00C07C29/04C07C31/10
CPCB01J27/16B01J29/00B01J37/0009C07C29/04C07C31/10
Inventor 孟庆伟刘泳涛唐晓飞齐晓梅牟维林王中平宋立红刘广志都健王家杰刘琳琳田存轩
Owner PETROCHINA CO LTD