Catalyst and method for direct conversion of synthesis gas for preparation of low carbon olefins

A catalyst and synthesis gas technology, which is applied in catalyst activation/preparation, molecular sieve catalyst, hydrocarbon production from carbon oxides, etc. The effect of low methane selectivity and good application prospects

Active Publication Date: 2018-06-12
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The catalyst in the above report uses metallic iron or iron carbide as the active component, the reaction follows the chain growth reaction

Method used

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  • Catalyst and method for direct conversion of synthesis gas for preparation of low carbon olefins
  • Catalyst and method for direct conversion of synthesis gas for preparation of low carbon olefins
  • Catalyst and method for direct conversion of synthesis gas for preparation of low carbon olefins

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Experimental program
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Embodiment 1

[0031] One, the preparation of catalyst A

[0032] (1), the etching method synthesizes the ZnO material with polar surface:

[0033] (1) Weigh 0.446g (1.5mmol) Zn(NO3) 2 6H2O, then weigh 0.480g (12mmol) NaOH and add it to the above container, then weigh 30ml deionized water and add it to the container, stir for more than 0.5h, Allow the solution to mix well. The temperature was raised to 160°C, the reaction time was 20 hours, and the precipitate was decomposed into zinc oxide; naturally cooled to room temperature. The reaction solution was centrifuged to collect the precipitate after centrifugation, and washed twice with deionized water to obtain ZnO oxide;

[0034] (2) using an etchant, ultrasonically mixing with the ZnO oxide at room temperature, soaking the ZnO oxide in the etchant solution, and forming a complex or direct reduction reaction between the etchant and the zinc oxide;

[0035] The above suspension is heated, then taken out, washed and filtered to obtain a nano...

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Abstract

The invention belongs to direct preparation of low carbon olefins from synthesis gas, and particularly relates to a catalyst and a method for direct conversion of the synthesis gas for preparation ofthe low carbon olefins. According to the method, the synthesis gas is adopted as a reaction raw material, a conversion reaction is carried out on a fixed bed or a moving bed, and the catalyst is a A+Bcomposite catalyst which is compounded by mixing a catalyst A and a catalyst B mechanically, wherein the active ingredient of the catalyst A is active metal oxide, and the catalyst B is one or two ormore selected from a molecular sieve of a CHA and AEI structure or a metal-modified CHA and/or AEI molecular sieve; a spacing between the geometric center of particles of the active metal oxide of the catalyst A and the geometric center of particles of the catalyst B is 5[mu]m-40 mm, a spacing between axial centers of particles is preferably 100 [mu]m-5 mm, more preferably 200 [mu]m-4 mm, and theweight ratio of the active ingredient in the catalyst A to the catalyst B is in a range of 0.1-20, preferably 0.3-5.

Description

technical field [0001] The invention belongs to the preparation of low-carbon olefins by synthesis gas, and in particular relates to a catalyst and a method for directly converting synthesis gas to produce low-carbon olefins. Background technique [0002] Low-carbon olefins refer to olefins with carbon atoms less than or equal to 4. Low-carbon olefins represented by ethylene and propylene are very important basic organic chemical raw materials. With the rapid growth of my country's economy, the supply of low-carbon olefins has been in short supply for a long time. At present, the production of low-carbon olefins mainly adopts the petrochemical route of cracking light hydrocarbons (ethane, naphtha, light diesel oil). Due to the increasing shortage of global oil resources and the long-term high price of crude oil, the development of low-carbon olefins industry only relies on oil The tubular cracking furnace process with light hydrocarbons as raw materials will encounter more ...

Claims

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Application Information

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IPC IPC(8): B01J29/82B01J29/83B01J29/85B01J29/84B01J29/70C07C1/04C07C11/04C07C11/06
CPCC07C1/043B01J29/7049B01J29/7065B01J29/82B01J29/83B01J29/84B01J29/85B01J35/0006B01J23/34B01J23/06B01J2229/186C07C11/04C07C11/06B01J29/70B01J29/78B01J29/87B01J29/89C07C1/04C07C9/04B01J23/005B01J37/033B01J37/088B01J37/16B01J37/18B01J37/035B01J35/023B01J35/0013B01J37/343B01J29/783B01J29/763B01J29/7015B01J23/26B01J23/75B01J23/745B01J29/76C07C11/02B01J37/0036B01J37/04Y02P20/52B01J2229/18B01J37/28B01J37/30B01J23/16B01J23/64B01J23/54C07C11/08B01J23/6522C07C1/0425C07C1/10C07C1/044C07C1/0435C07C1/0445C07C11/09C07C1/0455
Inventor 包信和焦峰潘秀莲丁民正
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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