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Catalyst for preparing propylene through propane dehydrogenation and preparation method of catalyst

A propane dehydrogenation and catalyst technology, applied in the direction of catalysts, carbon compound catalysts, chemical instruments and methods, to achieve good technical effects and high single-pass stability

Pending Publication Date: 2021-03-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Propane dehydrogenation catalysts have made great progress, but there is still room for improvement in catalyst activity

Method used

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  • Catalyst for preparing propylene through propane dehydrogenation and preparation method of catalyst
  • Catalyst for preparing propylene through propane dehydrogenation and preparation method of catalyst
  • Catalyst for preparing propylene through propane dehydrogenation and preparation method of catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0053] Weigh 297.49g of zinc nitrate hexahydrate, 120.04g of chromium nitrate nonahydrate and 637.72g of soluble salt of aluminum nitrate nonahydrate, dissolve them in 1L of deionized water, mix well, and slowly drip ammonia water under continuous stirring to adjust the pH to 8.0, the product was aged for 2 hours, filtered and washed with 4L of water to obtain a filter cake, dried at 100°C for 16 hours, and then roasted in a muffle furnace at 600°C for 20 hours to obtain ZnCr 0.3 al 1.7 o y Carrier, the composition is shown in Table 1. Weigh 9.78g of the carrier and put it into a beaker, then weigh 0.190g of stannous chloride dihydrate and dissolve it in 10mL of hydrochloric acid solution, add the above carrier under stirring, mix well, soak at 30°C for 12 hours, and then dry at 100°C for 16 Hour namely obtains catalyst precursor, denoted as I. Weigh 0.106g of chloroplatinic acid hexahydrate and 0.472g of calcium nitrate and dissolve them in 10mL of water, adjust the pH val...

Embodiment 2

[0055] Weigh 297.49g of zinc nitrate hexahydrate, 120.04g of chromium nitrate nonahydrate and 637.72g of soluble salt of aluminum nitrate nonahydrate, dissolve them in 1L of deionized water, mix well, and slowly drip ammonia water under continuous stirring to adjust the pH to 8.0, the product was aged for 2 hours, filtered and washed with 4L of water to obtain a filter cake, dried at 100°C for 16 hours, and then roasted in a muffle furnace at 600°C for 20 hours to obtain ZnCr 0.3 al 1.7 o y Carrier, the composition is shown in Table 1. Weigh 9.78g of the carrier and put it into a beaker, then weigh 0.190g of stannous chloride dihydrate and dissolve it in 10mL of hydrochloric acid solution, add the above carrier under stirring, mix well, soak at 30°C for 12 hours, and then dry at 100°C for 16 Hour namely obtains catalyst precursor, denoted as I. Weigh 0.106g of chloroplatinic acid hexahydrate and 0.472g of calcium nitrate and dissolve them in 10mL of water, adjust the pH val...

Embodiment 3

[0057] Weigh 297.49g of zinc nitrate hexahydrate, 120.04g of chromium nitrate nonahydrate and 637.72g of soluble salt of aluminum nitrate nonahydrate, dissolve them in 1L of deionized water, mix well, and slowly drip ammonia water under continuous stirring to adjust the pH to 8.0, the product was aged for 2 hours, filtered and washed with 4L of water to obtain a filter cake, dried at 100°C for 16 hours, and then roasted in a muffle furnace at 600°C for 20 hours to obtain ZnCr 0.3 al 1.7 o y Carrier, the composition is shown in Table 1. Weigh 9.78g of the carrier and put it into a beaker, then weigh 0.190g of stannous chloride dihydrate and dissolve it in 10mL of hydrochloric acid solution, add the above carrier under stirring, mix well, soak at 30°C for 12 hours, and then dry at 100°C for 16 Hour namely obtains catalyst precursor, denoted as I. Weigh 0.106g of chloroplatinic acid hexahydrate and 0.472g of calcium nitrate to dissolve in 10mL of water, adjust the pH value to ...

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Abstract

The invention relates to a catalyst for preparing propylene through propane dehydrogenation. The catalyst comprises Pt and / or an oxide thereof, Sn and / or an oxide thereof, alkaline earth metal and / oran alkaline earth metal oxide and a composite oxide carrier, wherein the composite oxide carrier comprises an oxide selected from IIB group elements and an oxide selected from VIB group elements. Thecatalyst adopts a composite oxide as a carrier, so that an acid center on the surface of the carrier can be effectively improved, and side reactions such as alkane cracking, isomerization, olefin cracking, isomerization, polymerization reaction and the like are reduced. The initial conversion rate of propane reaches 43% or above, the one-way stability is high, and a good technical effect is achieved.

Description

technical field [0001] The invention relates to a catalyst for producing propylene from propane dehydrogenation, a preparation method and application thereof. Background technique [0002] Propylene is a very important organic chemical raw material, and together with ethylene and isobutene, they are considered to be the basis of modern petrochemical industry. Propylene is mainly used in the production of polypropylene, followed by the production of acrylonitrile and propylene oxide. The traditional method of preparing propylene is to use ethylene co-production and cracking process of naphtha and light diesel oil. However, due to the restriction of petroleum reserves and distribution, propylene is difficult to obtain in large quantities, and contains elemental impurities such as S, so scientists are committed to developing and obtaining the target propylene new route. Among them, the method of preparing corresponding propylene through direct dehydrogenation process using pe...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/652C07C5/333C07C11/06
CPCB01J23/6522B01J23/6525B01J23/6527B01J23/002C07C5/3337C07C11/06B01J2523/00C07C2523/652B01J2523/23B01J2523/27B01J2523/31B01J2523/67B01J2523/28B01J2523/68B01J2523/69Y02P20/52
Inventor 姜冬宇缪长喜张磊张新玉
Owner CHINA PETROLEUM & CHEM CORP