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Integral catalyst for producing dimethyl ether by synthesis gas directly as well as its preparing method

A monolithic catalyst, dimethyl ether technology, applied in ether preparation, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of large particles, easy sintering of active components, poor catalytic activity, etc., and achieve the effect of high catalyst activity

Inactive Publication Date: 2008-04-09
ENERGY RES INST OF SHANDONG ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The present invention provides a new monolithic catalyst for directly preparing dimethyl ether from synthesis gas and its preparation method, which breaks through the traditional granular catalyst system. This monolithic honeycomb cordierite is used as the catalyst substrate, and it is active with a series of metal oxides. The monolithic dimethyl ether catalyst made by combining the components overcomes the problems of large particles, easy sintering of active components, and poor catalytic activity of the dimethyl ether synthesis catalyst in the prior art, and makes the monolithic catalyst for synthesis of dimethyl ether from syngas Has good catalytic activity and stability

Method used

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  • Integral catalyst for producing dimethyl ether by synthesis gas directly as well as its preparing method

Examples

Experimental program
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Effect test

Embodiment 1

[0026] Embodiment 1 (method 1): (1) the commercially available 400cpsi monolithic honeycomb cordierite (the same cordierite used in the following examples) was cut into a cylindrical sample of φ7mm×20mm, washed and dried; 26wt% HNO 3 The cordierite was treated with solution for 2 hours, then washed with deionized water until the filtrate was neutral, dried at 120°C for 1 hour, calcined at 550°C for 4 hours, and cooled naturally to obtain the pretreated cordierite matrix.

[0027] (2) Weigh a certain amount of NaOH, NaAlO 2 Dissolve in deionized water, stir to dissolve, slowly add tetrapropylammonium bromide (TPRBr), stir evenly, add quantitative tetraethyl orthosilicate dropwise and stir evenly, the molar ratio of each component in the final solution is: Al 2 o 3 : 80SiO 2 :9.6Na 2 O: 4800H 2 O: 17.2TPABr. Then put the pretreated cordierite obtained in step (1) into the autoclave together with the synthesis solution, and crystallize at 190°C for 48 hours. After cooling, ...

Embodiment 2

[0030] Embodiment 2 (method 1): (1) monolithic cordierite pretreatment method, with the step (1) of embodiment 1. (2) In-situ growth of HZSM-5 molecular sieve on monolithic cordierite, the method is the same as step (2) in Example 1, except that the molar ratio of the raw material solution is Al 2 o 3 : 80SiO 2 : 20Na 2 O: 10000H 2 O: 21.5TPABr.

[0031] (3) 10.872 grams of Cu(NO 3 ) 2 ·3H 2 O, 8.8902 g Zn(NO 3 ) 2 ·6H 2 O and 2.813 g Al(NO 3 ) 3 9H 2 O was dissolved in 82.3 mL of deionized water. Mix the mixed nitrate solution with 1mol / LNa 2 CO 3 The aqueous solution was added dropwise to a beaker filled with 100 mL of deionized water for co-precipitation. The precipitation temperature is 80°C, and the pH is maintained at about 7.0. After co-precipitation, continue to stir and age at 70°C for 1.0h. Others are with embodiment 1 step (3).

[0032] (4) Add the granular catalyst obtained in step (3) to dilute HNO 3 Grinding with deionized water with a ball mi...

Embodiment 3

[0033] Embodiment 3 (method 2): with 10.872 grams of Cu (NO 3 ) 2 ·3H 2 O, 6.693 g Zn(NO 3 ) 2 ·6H 2 O, 1.125 g Al(NO 3 ) 3 9H 2 O and 1.45 g ZrOCl 2 ·8H 2 O was dissolved in 82.8 mL of deionized water. Mix the mixed nitrate solution with 1mol / LNa 2 CO 3 The aqueous solution was added dropwise to a beaker filled with 100 mL of deionized water for co-precipitation. The precipitation temperature is 75°C, and the pH is maintained at about 8.0. After co-precipitation, continue to stir and age at 75°C for 1.0h. The precipitate was filtered and washed to obtain precipitate 1. Add 2.016g of HZSM-5 into 100mL of deionized water, and oscillate ultrasonically for 20min to obtain suspension 2. The precipitate 1 was added to the suspension 2, stirred for 3 hours, filtered and washed, baked under an infrared lamp for 10 hours, and roasted at 350° C. for 4 hours to obtain a dimethyl ether synthesis catalyst. Others are the same as example 1 step (4), but repeat the cordierit...

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Abstract

The invention relates to monolithic catalyst directly producing dimethyl ether with synthetic gas, and the preparation method thereof. The monolithic catalyst takes monolithic honeycomb cordierite as the matrix, and takes CuO-ZnO-MxOy / HZSM-5 as active components, MxOy expresses auxiliary agent of the active components, and M can be selected from Al, Zr, B, Ce or La; by quality, the CuO-ZnO-MxOy has 12 to 30 parts, the HZSM-5 has 5 to 16 parts, and the cordierite has 60 to 80 parts. The preparation method of the monolithic catalyst includes that a coating method and a uniform co-precipitation method are utilized. The preparation method has the coating method that dilute nitric acid, surface active agent, deionized water, etc are added into the CuO-ZnO-MxOy obtained in the co-precipitation method or the CuO-ZnO-MxOy-HZSM-5 obtained in the co-precipitation method for the ball milling; after being pulped, the mixture is coated on HZSM-5 / cordierite or the cordierite; and after being dried and roasted, a dimethyl ether monolithic catalyst finished product is obtained. Prepared in the method provided by the invention, the monolithic catalyst directly producing the dimethyl ether with the synthetic gas has good catalytic activity and stability.

Description

technical field [0001] The invention relates to a catalyst and a preparation method thereof, in particular to an integral catalyst used for directly producing dimethyl ether from synthesis gas and a preparation method thereof. Background technique [0002] The direct synthesis of DME from synthesis gas is a two-reaction process in which synthesis gas simultaneously completes methanol synthesis and methanol dehydration in a reactor, so the DME synthesis catalyst includes a methanol synthesis catalyst and a methanol dehydration catalyst. Early dimethyl ether synthesis catalysts were formed by mechanically mixing the two catalysts directly, but this mechanical mixing method would cause the two active centers to be far apart on the microcosm, and the synergistic effect of the two could not be well exerted; CN1233527A, CN1132664A, CN1356163A etc. have adopted co-precipitation deposition or co-precipitation impregnation method to prepare bifunctional dimethyl ether synthesis catal...

Claims

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Application Information

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IPC IPC(8): B01J29/46C07C43/04C07C41/01
Inventor 蔡飞鹏王建梅王波许敏孙立
Owner ENERGY RES INST OF SHANDONG ACAD OF SCI
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