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A catalyst and a method for preparing light olefins by direct carbon monoxide hydrogenation conversion

A technology of catalysts and oxides, applied in the direction of hydrocarbon production from carbon oxides, heterogeneous catalyst chemical elements, catalysts, etc., to achieve low methane selectivity, good application prospects, and the effect of product separation

Active Publication Date: 2018-09-25
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

In the patent they applied for (201610600945.6), they can significantly increase the selectivity of C3-C4 olefins by controlling the proportion of skeleton elements and the amount of medium-strong acid, but the selectivity of propylene itself can only reach a maximum of 40%.

Method used

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  • A catalyst and a method for preparing light olefins by direct carbon monoxide hydrogenation conversion
  • A catalyst and a method for preparing light olefins by direct carbon monoxide hydrogenation conversion
  • A catalyst and a method for preparing light olefins by direct carbon monoxide hydrogenation conversion

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Embodiment 1

[0026] 1. Preparation of Catalyst A Component

[0027] (1) The active metal oxide is M n+ MnCr 2 o 4+n / 2 , M n+ MnAl 2 o 4+n / 2 , M n+ ZnCr 2 o 4+n / 2 , M n+ ZnAl 2 o 4+n / 2 preparation of

[0028] (1) Use zinc nitrate, aluminum nitrate, chromium nitrate, and manganese nitrate as precursors, and then add 1-10% other metal nitrates and urea to mix with each other in water at room temperature; age the above mixed solution, and then take it out Washing, filtering and drying, the resulting solid is roasted under air atmosphere to obtain M n+ MnCr 2 o 4+n / 2 , M n+ MnAl 2 o 4+n / 2 , Mn+ ZnCr 2 o 4+n / 2 , M n+ ZnAl 2 o 4+n / 2 Metal oxide.

[0029] (2) Using etchant such as oleic acid, urotropine, ethylenediamine, ammonia water, hydrazine hydrate, etc., the above sample is ultrasonically mixed with the metal oxide at room temperature, and the metal oxide is soaked in the etchant solution, The etchant forms a complex with the metal oxide or undergoes a direct reductio...

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Abstract

The invention belongs to direct preparation of light olefins by carbon monoxide hydrogenation, and especially relates to a catalyst and a method for preparing light olefins by direct carbon monoxide hydrogenation conversion. Synthetic gas is adopted as a reaction raw material of the method, and is subjected to a conversion reaction in a fixed bed or a moving bed. The catalyst adopted by the methodis compounded by an A component and a B component, the A component being a metal oxide, and the B component being a molecular sieve, and the metal oxide and the molecular sieve are physically mixed and play a role of catalysis. The weight ratio range of the A component to the B component is 0.1-20; a product yield and selectivity of a reaction process are high; the selectivity of light olefins can reach 65-85%; the selectivity of propylene can reach 45-66%; and the selectivity of by-product methane is extremely low (less than 5%), and therefore, the catalyst and the method have good application prospects.

Description

technical field [0001] The invention belongs to carbon monoxide hydrogenation to prepare low-carbon olefins, in particular to a catalyst and a method for directly converting carbon monoxide hydrogenation to prepare 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 encoun...

Claims

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Application Information

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IPC IPC(8): B01J29/85C07C11/04C07C11/06C07C11/08C07C1/04
CPCC07C1/043C07C1/0435B01J23/002B01J23/06B01J23/08B01J23/26B01J23/30B01J23/31B01J23/34B01J23/685B01J23/80B01J23/864B01J23/8892B01J29/85C07C2529/85B01J2523/00B01J2229/20B01J35/19B01J2523/27B01J2523/54B01J2523/67B01J2523/31B01J2523/32B01J2523/48B01J2523/72B01J2523/33B01J2523/15C07C11/04C07C11/06C07C11/08Y02P20/52
Inventor 潘秀莲丁民正包信和焦峰
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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