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Mixed carbon four-component selective hydrogenation catalyst and preparation method

A hydrogenation catalyst and a technology for mixing C4, which are used in catalyst activation/preparation, hydrocarbon production by hydrogenation, chemical instruments and methods, etc., can solve the problems of large loss of monobutene, insufficient removal depth, and low yield, etc. The effect of improving the removal depth, taking into account the activity and selectivity, and long life

Active Publication Date: 2021-11-26
大连华邦化学有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Palladium system catalysts have the characteristics of low operating temperature and few side reactions, but there are problems such as insufficient removal depth of carbon tetraynes, dienes, and vinyl acetylene, and large loss of monobutene and low yield.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0014] a. Weigh 1000g CeCl 3 and 1000gZrCl 4 , prepare a 2L aqueous solution and an ammonia solution with a mass concentration of 0.33% to generate CeO by co-precipitation 2 -ZrO 2 mixture, washed CeO 2 -ZrO 2 until the mixture is free of Cl - 1150g CeO was made by drying at 120°C for 5h 2 -ZrO 2 mixture;

[0015] b. Take 400gCeO 2 -ZrO 2 , 500gγAl 2 o 3 and 100g of attapulgite, mixed evenly with a mixer and then extruded into 1 / 16" strips with an extruder, dried with water mist for 12 hours, and used N 2 The protection program heats up to 350°C and roasts to make a catalyst support carrier;

[0016] c. With 2.52gPdCl 2 , 34.36gMnCl 2 , 2ml of concentrated hydrochloric acid with a mass concentration of 37%, and 200ml of deionized water are heated and dissolved to make a mixed solution;

[0017] d. Take 500g of the catalyst support carrier prepared above, dip it in an equal volume mixed solution, let it stand for 1h, soak it with 500ml of glucose (reducing cataly...

Embodiment 2

[0033] a. Weigh 50gCeCl 3 and 80gZrCl 4 , prepare a 500ml aqueous solution and an ammonia solution with a mass concentration of 0.33% to generate CeO by co-precipitation 2 -ZrO 2 mixture, washed CeO 2 -ZrO 2 until the mixture is free of Cl - Dry at 120°C for 5 hours to make CeO 2 -ZrO 2 mixture;

[0034] b. Take 40gCeO 2 -ZrO 2 Mixture, 50gγAl 2 o 3 and 10g of attapulgite were mixed evenly and made into a 1.2mm spherical shape with a sugar coating machine, and dried after 24 hours of water mist preservation. 2 The protection program heats up to 500°C and roasts to make a catalyst support carrier;

[0035] c. With 0.35gPdCl 2 , 11.45gMnCl2, 0.5ml mass concentration 37% concentrated hydrochloric acid, 300ml deionized water are heated and dissolved to make a mixed solution;

[0036] d. Take 100g of the support carrier prepared above, soak it in an equal volume of mixed solution, let it stand for 2 hours, soak it with 1L of glucose (reducing catalyst) with a mass con...

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Abstract

The invention discloses a mixed carbon four-component selective hydrogenation catalyst and a preparation method thereof. The mixed carbon four-component selective hydrogenation catalyst is composed of an active component and a support carrier, the active component is palladium and manganese, and the support carrier is γAl 2 o 3 , CeO 2 -ZrO 2 and attapulgite; palladium accounts for 0.08% to 1.5% of the mass of the support carrier, manganese accounts for 3 to 5% of the mass of the support carrier, γAl 2 o 3 , CeO 2 -ZrO 2 , The mass ratio of attapulgite is 50~60:30~40:10~20. The specific surface area of ​​the support carrier is 120~180m 2 / g, effectively taking into account the catalyst activity and selectivity, the active component Pd interacts with Mn, which is conducive to improving the removal depth of butadiene, carbon tetraacetylene, vinyl acetylene and increasing the yield of monobutene. It does not need to be activated before use, has high mechanical strength and is not easy to pulverize, has the advantages of convenient use and long service life, and can be widely used in large-scale industrial production.

Description

technical field [0001] The invention relates to a catalyst and a preparation method, in particular to a mixed carbon four-component selective hydrogenation catalyst capable of effectively increasing the yield of monobutene and a preparation method. Background technique [0002] Mixed carbon four is the general term for alkanes, monoolefins and diolefins, mainly derived from the torch gas containing vinyl acetylene produced by petroleum olefin cracking, coal chemical industry and carbon four extraction devices. Petroleum olefin cracking units mainly produce ethylene, and co-produce propylene and C4 fraction at the same time. The C4 fraction mainly produces MTBE and monobutene; coal chemical industry uses coal to produce methanol, and methanol produces olefins, ethylene and propylene, and at the same time produces some carbon Four products, its carbon four is used to produce products such as MTBE, monobutene and 2PH; while most of the torch gas containing vinyl acetylene is ev...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/656B01J37/03B01J37/02B01J23/10B01J35/10C07C5/05C07C11/08
Inventor 侯鹏李文强刘超杨瑞云赵艳东皮山丹张文刚
Owner 大连华邦化学有限公司
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