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Catalyst composition and application thereof in direct preparation of low-carbon olefin from synthesis gas

A composition and catalyst technology, applied in the direction of producing hydrocarbons from carbon oxides, hydrocarbons, hydrocarbons, etc., can solve the problems of low isobutene selectivity and low CO conversion rate, and achieve high CO conversion rate, high low carbon Effects of olefin selectivity, excellent butene selectivity

Pending Publication Date: 2021-12-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The purpose of the present invention is to solve the shortcomings of low CO conversion rate and low isobutene selectivity in the prior art, and provide a new catalyst composition for producing low-carbon olefins from synthesis gas and its direct production of low-carbon olefins from synthesis gas. Applications in olefins

Method used

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  • Catalyst composition and application thereof in direct preparation of low-carbon olefin from synthesis gas
  • Catalyst composition and application thereof in direct preparation of low-carbon olefin from synthesis gas
  • Catalyst composition and application thereof in direct preparation of low-carbon olefin from synthesis gas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] ZnAl 1.3 Oxides are prepared as follows:

[0033] Weigh 1.0 mol of zinc nitrate and 1.3 mol of aluminum nitrate, dissolve them in 2000 mL of distilled water, then dissolve 6.0 mol of NaOH in 2000 mL of water, co-precipitate the two aqueous solutions, age at 70°C for 3 hours, and filter at 100 Dry overnight at ℃, calcined at 400℃ for 12h to get ZnAl 1.3 oxide.

[0034] AlPO 4 -14 molecular sieves are prepared as follows:

[0035] Pseudoboehmite, phosphoric acid, and isopropylamine are used as aluminum source, phosphorus source, and template agent respectively, and the molar ratio of Al 2 o 3 :P 2 o 5 :Isopropylamine:H 2 O=1:1:1:50, add to the reaction kettle and age for 2 hours, stir and crystallize at 200°C for 72h, wash the obtained solid with deionized water until neutral, separate the solid, dry it, and put it in a muffle furnace for 550 ℃ roasting for 6 hours to get AlPO 4 -14 molecular sieves. See XRD figure 1 .

[0036] 0.75 g of prepared ZnAl 1.3 ox...

Embodiment 2

[0038] InAl 0.8 Oxides are prepared as follows:

[0039] Weigh 1.0 mol of indium nitrate and 0.8 mol of aluminum nitrate, dissolve them in 2000 mL of distilled water, then dissolve 5.5 mol of NaOH in 2000 mL of water, co-precipitate the two aqueous solutions, age at 70°C for 3 hours, and filter at 100 °C dried overnight, then fired at 400 °C for 12 hours to obtain InAl 0.8 oxide.

[0040] AlPO 4 -14 molecular sieves were prepared according to [Example 1].

[0041] GaPO 4 -14 molecular sieves are prepared as follows:

[0042] With gallium nitrate, phosphoric acid, and isopropylamine (Isopropylamine) as the gallium source, phosphorus source, and template agent, the molar ratio of Ga(NO 3 ) 3 :P 2 o 5 :Isopropylamine:H 2 O=2:1:1:50, put into the reaction kettle and age for 2 hours, stir and crystallize at 200°C for 72h, wash the obtained solid with deionized water until neutral, separate the solid, dry it, and put it in a muffle furnace for 550 ℃ roasting for 6 hours t...

Embodiment 3

[0045] Zn 0.75 Cr oxides are prepared as follows:

[0046] Weigh 0.75 mol of zinc nitrate and 1 mol of chromium nitrate, dissolve them in 1500 mL of distilled water, then dissolve 4.8 mol of NaOH in 1500 mL of water, co-precipitate the two aqueous solutions, age at 70°C for 3 hours, and filter at 100 It was dried overnight at ℃ and calcined at 400℃ for 12h. Get Zn 0.75 Cr oxide.

[0047] ZnO is prepared as follows:

[0048] Weigh 1mol of zinc nitrate, dissolve it in 1000mL of distilled water, then dissolve 2mol of NaOH in 1000mL of water, co-precipitate the two aqueous solutions, age at 70°C for 3h, filter and dry at 100°C overnight, at 400°C Baking at ℃ for 12h. Obtain ZnO oxide.

[0049] Al-GaPO 4 -14 molecular sieves are prepared as follows:

[0050] Pseudoboehmite, gallium nitrate, phosphoric acid, and isopropylamine are used as aluminum source, gallium source, phosphorus source, and template respectively, and the molar ratio of Al 2 o 3 : Ga(NO 3 ) 3 :P 2 o ...

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Abstract

The invention discloses a catalyst composition and application thereof in direct preparation of low-carbon olefin from synthesis gas, in particular to application in preparation of mixed low-carbon olefin rich in isobutene from synthesis gas by a one-step method. The catalyst composition comprises an AFN topological structure molecular sieve and a CO adsorption component. With the catalyst, the isobutene-rich mixed low-carbon olefin can be prepared from the synthesis gas through the high-selectivity one-step method, and the isobutene content in the product can be significantly improved. The method can be used for efficiently, continuously and stably preparing the mixed low-carbon olefin product rich in isobutene, and can be used for industrial production of preparing low-carbon olefin from synthesis gas.

Description

technical field [0001] The invention belongs to the technical field of chemistry and chemical engineering, and relates to a catalyst composition and its application in the one-step synthesis gas preparation of low-carbon olefins, especially the application in the one-step synthesis gas high-selectivity preparation of isobutene-rich mixed light olefins. Background technique [0002] Low-carbon olefins are an important standard to measure the level of a country's chemical industry, and are also important organic chemical raw materials, which can produce bulk synthetic materials such as plastics, synthetic resins, fibers, and rubber. In recent years, the production capacity of low-carbon olefins in China has continued to increase, and the production has reached a considerable scale, but the import volume has continued to grow for a long time. With the rapid growth of the national economy, China's demand for chemical raw materials such as ethylene, propylene, and butene will inc...

Claims

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Application Information

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IPC IPC(8): B01J29/83B01J29/84C07C1/04C07C11/02C07C11/04C07C11/06C07C11/08C07C11/09
CPCB01J29/83B01J29/84C07C1/043B01J2229/18C07C11/04C07C11/06C07C11/08C07C11/09Y02P20/52
Inventor 周海波焦文千刘苏王仰东苏俊杰张琳刘畅
Owner CHINA PETROLEUM & CHEM CORP