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Catalyst for preparing neopentyl glycol

A neopentyl glycol and catalyst technology, which is applied in the direction of heterogeneous catalyst chemical elements, physical/chemical process catalysts, hydroxyl compound preparation, etc., can solve the problems of affecting the life of the catalyst, the catalyst is easily broken, pulverized, and has no running time. , to achieve the effect of improving catalyst selectivity, remarkable technical effect and reducing cost

Active Publication Date: 2020-12-15
上海翼湍科技有限责任公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] Due to the poor thermal stability of hydroxypivalaldehyde, when its hydrogenation reaction is carried out under liquid phase conditions, the actual use strength of the catalyst will be greatly reduced due to liquid immersion, swelling, etc., resulting in the catalyst being easily broken and pulverized in the liquid phase hydrogenation system. It will cause blockage of the reactor, threaten the stable operation of industrial equipment, and affect the life of the catalyst
In existing patents, the catalyst for the hydrogenation of hydroxypivalaldehyde to neopentyl glycol has a maximum running time of 1800 hours, and there is no report of a longer running time

Method used

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  • Catalyst for preparing neopentyl glycol
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  • Catalyst for preparing neopentyl glycol

Examples

Experimental program
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Effect test

preparation example Construction

[0026] Preparation of θ-Al2O3 crystal form alumina:

[0027] Prepare 250mL of 2.4mol / L sodium aluminate aqueous solution and pour it into the reactor, seal it, vacuumize it and heat it to 40°C in a water bath, start stirring, slowly introduce carbon dioxide and finally keep the pressure of carbon dioxide at 1MPa, during , the following reaction occurs in solution:

[0028] 2NaAlO2+CO2+3H2O——2Al(OH)3+Na2CO3

[0029] NaAlO2+2H2O——Al(OH)3+NaOH

[0030] Na2CO3+2CO2+2Al(OH)3——2NaAl(CO3)(OH)2+H2O

[0031] 2NaOH+CO2——Na2CO3+H2O

[0032] The reaction mother liquor was continuously stirred for 48 hours, and the pH of the mother liquor was measured to be 10 when the reaction ended. Subsequently, the white precipitate generated by the reaction was taken out, washed and filtered with desalinated water for more than three times to remove residual alkaline substances, and the mixture was diluted and dried overnight at 120° C. in an oven to obtain a mixture. The mixture was characterize...

Embodiment 1

[0036] 9.1g Cu(NO 3 ) 2 ·3H 2 O, 11.3g Zn(NO 3 ) 2 ·6H 2 O, 0.7g AgNO 3 , 1.4g Ga(NO 3 ) 3 Dissolve in 500ml of water to make metal salt solution A; weigh 16.9g of sodium carbonate and dissolve in 100ml of water, add 3g of θ-Al to it 2 o 3 Powder, stir vigorously to form a precipitant-carrier suspension solution B; under mechanical stirring, control the water bath at 60°C and slowly add solution A to solution B dropwise, the reaction will form a white precipitate, and continue at 60-70°C after the addition is complete Stir and age for 1-2 hours to obtain a suspension of the corresponding mixture; wash the solid phase with deionized water until the conductivity is less than 1000 us / cm, then granulate, dry, and roast to obtain a catalyst. The catalyst contains 31wt% copper oxide, 31wt% zinc oxide, 30wt% alumina, 3wt% silver oxide, 5wt% gallium oxide, wherein alumina is θ-Al 2 o 3 crystal form.

[0037] Catalyst in embodiment 1 is 1.0h at 80 ℃, 2.0MPa, raw material we...

Embodiment 2

[0039] The synthesis method is basically the same as that of Example 2, except that the proportions of A and B solutions are different. 4.5g Cu(NO 3 ) 2 ·3H 2 O, 13.2g Zn(NO 3 ) 2 ·6H 2 O, 0.7g AgNO 3 , 1.4g Ga(NO 3 ) 3 Dissolve in 500ml of water to configure metal salt solution A; weigh 14.1g of sodium carbonate and dissolve in 100ml of water, add 4g of θ-Al to it 2 o 3 powder, stirred vigorously to form precipitant-carrier suspension solution B. The catalyst contains 15wt% copper oxide, 35wt% zinc oxide, 40wt% aluminum oxide, 3.5wt% silver oxide and 5wt% gallium oxide.

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Abstract

The invention discloses a catalyst for preparing neopentyl glycol, and solves the problem that the catalytic activity and stability of the existing catalyst need to be further improved. The catalyst is composed of copper oxide, zinc oxide, aluminum oxide and silver oxide and / or gallium oxide, and the aluminum oxide is aluminum oxide in a theta Al2O3 crystal form. The catalyst is low in raw material cost, high in catalyst activity, good in stability and long in operation time.

Description

technical field [0001] The invention relates to a catalyst, in particular to a catalyst for hydrogenation to prepare neopentyl glycol (NPG). Background technique [0002] Neopentyl glycol is an important chemical intermediate. It is mainly used in the production of unsaturated resins, polyester powder coatings, oil-free alkyd resins, polyurethane foams, plasticizers for elastomers, synthetic plasticizers, surfactants, insulating materials, printing inks, polymerization inhibitors, Synthetic aviation lubricating oil additives, etc. In addition, it is also used in the pharmaceutical industry. At the same time, neopentyl glycol is also an excellent solvent and can be used for the selective separation of aromatics and cycloalkyl hydrocarbons. [0003] In industry, neopentyl glycol usually has two processes: disproportionation method and condensation hydrogenation method. The disproportionation method uses an excessive amount of strong basic catalyst such as sodium hydroxide,...

Claims

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Application Information

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IPC IPC(8): B01J23/89B01J23/825B01J23/80C07C29/141C07C31/20
CPCB01J23/002B01J23/896B01J23/8953B01J23/825B01J23/80C07C29/141B01J2523/00B01J2523/17B01J2523/18B01J2523/27B01J2523/31B01J2523/32C07C31/20Y02P20/52
Inventor 卢文新刘佳张大洲胡媛夏吴
Owner 上海翼湍科技有限责任公司