Dimethyl benzyl alcohol hydrogenolysis catalyst and preparation method thereof

A technology of dimethyl benzyl alcohol and catalyst, which is applied in the field of catalysis, can solve the problems of blockage of catalyst carrier pores, decrease of catalyst use strength, and threats to the stable operation of industrial devices, etc.

Active Publication Date: 2019-08-02
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The hydrogenolysis catalysts of dimethyl benzyl alcohol mainly include platinum-palladium precious metal catalysts, nickel-based catalysts and copper-based catalysts, etc., the cost of noble metal catalysts and nickel-based catalysts is high, and it is easy to cause Saturated aromatic ring, poor selectivity to cumene
[0018]The active center of the copper-based catalyst is the reduced metal copper grains. Because the melting point of metal copper is relatively low, the growth of copper grains and the Sintering will directly lead to a reduction in the number of active sites of the catalyst and a decrease in catalyst activity
The decrease in hydrogenolysis activity will induce side reactions such as polymerization, which will cause the active site of the catalyst to be covered by the polymer and the carrier pores to be blocked by the polymer, resulting in a decrease in the activity and stability of the catalyst.
[0019] In the prior...

Method used

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  • Dimethyl benzyl alcohol hydrogenolysis catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0081] (1) Add 300g water and 80.0g sodium silica sol (SiO in silica sol) into the reaction kettle 2 The content is 30wt%, SiO 2 The particle size is 30nm, the pH value is 9.0) and stirred evenly.

[0082] (2) 273.4g copper nitrate (Cu(NO 3 ) 2 ·3H 2 O, 242), 131.6g zinc nitrate (Zn(NO 3 ) 2 ·6H 2 O, 298), 63.6g magnesium nitrate (Mg(NO 3 ) 2 ·6H 2 (256), 3.0g lead nitrate (331) and 3.4g bismuth nitrate (395) are dissolved in 1226g water and prepare mixed salt solution, preparation concentration is the sodium carbonate aqueous solution of 15wt%, with above-mentioned two kinds of solutions heated to 60 ℃ respectively then Add it dropwise to the aforementioned reactor, the time of dropping is 40min, the temperature of the precipitation process is controlled at 60°C, and the pH value of the precipitation process is 7.0 (wherein, the consumption of the aqueous sodium carbonate solution is controlled according to the pH value of the precipitation process so that the metal ...

Embodiment 2

[0089] (1) Add 300g of water and 82.7g of sodium silica sol (SiO in silica sol) into the reaction kettle 2 The content is 30wt%, SiO 2 The particle size is 25nm, the pH value is 9.5) and stirred evenly.

[0090] (2) 303.7g copper nitrate, 102.4g zinc nitrate, 18.7g barium nitrate, 4.5g lead nitrate and 3.4g bismuth nitrate are dissolved in 1130g water to prepare mixed salt solution, preparation concentration is 15wt% sodium carbonate aqueous solution, above-mentioned two The solutions were heated to 45° C. and then added dropwise to the aforementioned reaction kettle in parallel. The dropping time was 30 min. The temperature of the precipitation process was controlled at 45° C., and the pH value of the precipitation process was 6.5 (wherein, the aqueous solution of sodium carbonate was controlled according to the pH value of the precipitation process. The amount used is 105% of the theoretically required amount to completely precipitate the metal particles), and then aged at ...

Embodiment 3

[0095] (1) Add 300g of water and 78g of sodium silica sol (SiO in silica sol) into the reaction kettle 2 The content is 30wt%, SiO 2 The particle size is 20nm, the pH value is 9.5) and stirred evenly.

[0096] (2) 334.1g copper nitrate, 102.4g zinc nitrate, 21.1g calcium nitrate (Ca(NO 3 ) 2 4H 2 (236), 3.0g lead nitrate and 5.1g bismuth nitrate are dissolved in 1225g water and prepare mixed salt solution, preparation concentration is the sodium carbonate aqueous solution of 15wt%, and above-mentioned two kinds of solutions are heated to 50 ℃ respectively and then co-current dropwise add to aforementioned In the reaction kettle, the dropping time is 50min, the temperature of the precipitation process is controlled at 50°C, and the pH value of the precipitation process is 6.8 (wherein, according to the pH value of the precipitation process, the amount of sodium carbonate aqueous solution is controlled to be 105% of the theoretically required amount of metal particles. %), a...

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Abstract

The invention discloses a dimethyl benzyl alcohol hydrogenolysis catalyst and a preparation method thereof. The catalyst comprises 35-70wt% of copper oxide, 5-25wt% of zinc oxide, 15-40wt% of silicondioxide, 0.5-15wt% of alkaline earth metal oxide and 0.1-5wt% of bismuth oxide and lead oxide. The preparation method comprises the following steps: (a) adding a mixed solution containing a Cu compound, a Zn compound, an alkaline earth metal compound, a Bi compound and a Pb compound and an alkaline precipitant solution into a silica sol aqueous solution for precipitation reaction and heating aging; (b) filtering, washing, drying and roasting the aged slurry to obtain complex compound powder; and (c) adding a binder, a forming assistant and the like into the complex compound powder, fully mixing, extruding and forming, drying and roasting to obtain the catalyst. When used for preparing cumene by hydrogenolysis of dimethylbenzyl alcohol, the method not only has good activity and selectivity,but also has good liquid resistance and high mechanical stability.

Description

technical field [0001] The invention belongs to the technical field of catalysis, and in particular relates to a dimethyl benzyl alcohol hydrogenolysis catalyst and a preparation method thereof. Background technique [0002] Propylene oxide (PO) is an important organic chemical raw material, mainly used in the production of polyether polyol (polyurethane raw material), propylene glycol, etc. developer etc. [0003] Industrial PO production methods mainly include chlorohydrin method, hydrogen peroxide direct oxidation method and co-oxidation method (Halcon method). The chlorohydrin method is the main route for producing PO in China. This process has serious problems such as equipment corrosion and environmental pollution. Due to the high raw material cost of the direct hydrogen peroxide oxidation route, the economy is affected. [0004] The co-oxidation method, also known as co-production method or indirect oxidation method, is to generate propylene oxide through the react...

Claims

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Application Information

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IPC IPC(8): B01J23/843B01J37/03B01J37/08C07C1/20C07C15/085
CPCB01J23/8437B01J23/002B01J37/03B01J37/0018C07C1/20B01J2523/00C07C15/085B01J2523/17B01J2523/22B01J2523/27B01J2523/41B01J2523/44B01J2523/54B01J2523/23B01J2523/25Y02P20/52
Inventor 李作金孙康于海波沙宇燕宸詹吉山王同济叶飞王雷雷王勤隆黎源
Owner WANHUA CHEM GRP CO LTD
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