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Lawrencium base catalyst for preparing C2 oxygen-contained compound by using synthetic gas

A catalyst and compound technology, applied in the field of Rh-based catalysts, can solve the problems of low conversion rate of CO, decreased selectivity of oxygenated compounds, low total yield of oxygenated compounds, etc., and achieve high space-time yield and improved conversion rate

Inactive Publication Date: 2005-03-02
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 past literature, most of the SiO 2 As catalyst carrier, and the molecular sieve with regular pore structure is used as the research of carrier preparation catalyst also less, only NaY molecular sieve is used as the carrier of catalyst (Xu Baiqing, W.M.H.Sachtler, Chemical Journal of Chinese Universities, 1999,12(5 ): 794-796), the prepared Rh / NaY catalyst was used in C 2 Synthesis of oxygenates, although a single C 2 Oxygenated compounds --- Higher selective synthesis of acetic acid, the selectivity is about 50%, but because the conversion rate of CO is too low, only about 1%, making C 2 The total yield of oxygen-containing compounds is still very low, only about 0.5-0.6%, and the increase of reaction temperature can increase the conversion rate of CO, but the C 2 Oxygenate selectivity drops rapidly

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] Catalyst A was prepared by loading active metals on MCM-41 molecular sieves. The percentage of Rh in the catalyst A is 3%, and the percentage by weight of Rh, Mn and Li elements is Rh:Mn:Li=1:1:0.075. The specific preparation method and activity test steps are as follows:

[0020] (1) Treatment of raw molecular sieve powder

[0021] The all-silicon MCM-41 molecular sieve raw powder was calcined in a muffle furnace with a heating rate of 2°C / min and a constant temperature of 550°C for 6 hours. to N 2 The average pore size measured by adsorption and HRTEM was 3nm.

[0022] (2) Forming of molecular sieve carrier

[0023] Extrude the molecular sieve obtained in (1), crush and sieve, and take 20-40 mesh for later use.

[0024] (3) Impregnation of active components

[0025] The prepared RhCl containing 0.15g Rh, 0.15g Mn and 0.0113g Li 3 , Mn(NO 3 ) 2 and LiNO 3 Put the mixed solution of the mixture into a dipping bottle, weigh 5 g of the carrier obtained in (2) (th...

Embodiment 2

[0039] Catalyst B was prepared by loading active metals on MCM-22 molecular sieves. The Si / Al ratio in the molecular sieve is 30. The composition, preparation process and activity evaluation method of Catalyst B are the same as in Example 1.

[0040] Catalyst B of C 2 Oxygenate synthesis reaction performance is shown in Table 2:

[0041] Table 2 C of Catalyst B 2 Oxygenate Synthesis Reaction Performance

[0042] Reaction CO Conversion Alkanes C 2 Oxidized C 2 Oxidized C 2 Oxygenated

[0043]Temperature Rate Selectivity Compound Selection Compound Yield Compound Time and Space

[0044] (°C (mol (CO (CO%) yield

[0045] ) %) %) (CO%) (g / Kg.h)

[0046] 280 3.33 49.5 48.9 1.63 254.7

[0047] 300 7.68 54.0 45.0 3.45 500.5

[0048] 320 15.22 70.2 28.5 4.34 578.6

[0049] Reaction conditions: reaction pressure 3MPa, H 2 / CO=2, the space velocity is 40000ml / Kg.h.

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Abstract

The rhodium base catalyst for preparing 2 carbon compound containing oxygen is formed from active component Rh and carrier, the weight content of Rh is 0.01-10%, and it is characterized by that the carrier adopted by said invention is a molecular sieve with proper pore size and higher Si / Al ratio. Its pore size is 0.5 nm to 30 nm, surface area is above 100-1500 sq.m / g, and Si-Al ratio is 5-infinity. Said invented catalyst can be used for synthesis of C2 oxygen-contained compound, can raise the conversion rate of CO and yield rate of C2 oxygen-contained compound.

Description

technical field [0001] The present invention relates to the production of C from synthesis gas 2 Oxygenate technology, in particular, provides a novel Rh-based catalyst supported by molecular sieves. Background technique [0002] Ethanol, acetaldehyde and acetic acid etc. C 2 Oxygenates have always been important chemical raw materials. The traditional preparation methods of these products mostly use grain and petroleum as raw materials. If they can be synthesized from syngas in one step, a large amount of grain can be saved, and the abundant and cheap coal and natural gas can be fully utilized. resources and broad application prospects. [0003] In the production of C using synthesis gas as raw material 2 In the reaction of oxygen-containing compounds, Rh is a necessary active metal component in highly active catalysts, such as: United Carbide Corporation (UCC) uses Rh / SiO 2 One-stage synthesis of acetic acid (UCC, patent-opening 51 80806) as catalyst; Rh-V-M / SiO 2 Syn...

Claims

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Application Information

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IPC IPC(8): B01J23/56B01J29/068
Inventor 包信和马洪涛程谟杰罗洪原
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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