Unlock instant, AI-driven research and patent intelligence for your innovation.

Preparation and activation method of Raney nickel-aluminum-x catalyst for 1,4-butynediol hydrogenation to 1,4-butanediol

A technology of butynediol and activation method, which is applied in the field of preparation and activation of Raney nickel-aluminum-X catalyst, can solve the problems affecting the purity of catalyst active products, and achieve the effects of easy pulverization, simple preparation method and improved efficiency

Active Publication Date: 2015-11-18
HAISO TECH
View PDF5 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method has the disadvantage of easily introducing other harmful ions, affecting the activity of the catalyst and the purity of the product

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Weigh 250g of Ni block, 500g of Al block and 0.75g of B respectively and place them in an intermediate frequency induction furnace, turn on the current, after Ni, Al and X are melted, after melting at 900°C for 60 minutes, pour into water to cool; The catalyst obtained after grinding to 200 mesh powder; Weigh 200g of catalyst powder and add in batches 400g of NaOH solution with a mass concentration of 25% and mix evenly, then control the temperature at 60°C for 30min, after the reaction is completed, wash with distilled water 3 times, and then washed with absolute ethanol until neutral; the whole activation process was controlled for 2 hours; the activated catalyst was moved into a high-pressure reactor with 3000g35wt% 1,4-butynediol solution inside, and the reaction pressure was 3MPa. The reaction temperature was 50°C and the stirring speed was 1500 rpm for 3 hours. The conversion rate of 1,4-butynediol was 98.3%, and the selectivity of 1,4-butanediol was 90.8%.

Embodiment 2

[0026] Weigh 250g of Ni block, 500g of Al block and 0.75g of Mg and place them in the medium frequency induction furnace, turn on the current, after Ni, Al and X are melted, after melting at 900°C for 60min, pour into water to cool; The catalyst obtained after grinding to 200 mesh powder; Weigh 200g of catalyst powder and add in batches 400g of NaOH solution with a mass concentration of 25% and mix evenly, then control the temperature at 60°C for 30min, after the reaction is completed, wash with distilled water 3 times, and then washed with absolute ethanol until neutral; the whole activation process was controlled for 2 hours; the activated catalyst was moved into a high-pressure reactor with 3000g35wt% 1,4-butynediol solution inside, and the reaction pressure was 3MPa. The reaction temperature was 50°C and the stirring speed was 1500 rpm for 3 hours. The conversion rate of 1,4-butynediol was 98.7%, and the selectivity of 1,4-butanediol was 92.8%.

Embodiment 3

[0028] Weigh 300g of Ni block, 500g of Al block and 1.6g of Sr respectively and put them in the medium frequency induction furnace, turn on the current, after Ni, Al and X are melted, after smelting at 1000℃ for 60min, pour into water to cool; The obtained catalyst was ground to 200-mesh powder; weighed 200g of catalyst powder and added in batches to 400g of KOH solution with a mass concentration of 25% and mixed evenly, then controlled the temperature at 60°C for 30min, after the reaction was completed, washed with distilled water 3 times, and then washed with absolute ethanol until neutral; the whole activation process was controlled for 2 hours; the activated catalyst was moved into a high-pressure reactor with 3000g35wt% 1,4-butynediol solution inside, and the reaction pressure was 3MPa. The reaction temperature was 50°C and the stirring speed was 1500 rpm for 3 hours. The conversion rate of 1,4-butynediol was 98.7%, and the selectivity of 1,4-butanediol was 93.5%.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention discloses a preparation method and an activation method of a Raney nickel-aluminum-X catalyst specially for hydrogenation preparation of 1,4-butanediol from 1,4-butynediol. The Raney nickel-aluminum-X catalyst is characterized in that a mass ratio of nickel to aluminum is (0.5 to 1): 1; X of which mass is 0.1 to 2% of total mass of nickel and aluminum is adopted; and X represents Mg, B, Sr, Cr, S, Ti, La, Sn, W, Mo or Fe. The preparation method comprises the following steps of putting nickel, aluminum and X into a medium frequency induction smelting furnace according to the mass ratio, carrying out smelting, pouring out melt, cooling, crushing, and grinding to obtain powder which is the Raney nickel-aluminum-X catalyst. The activation method comprises the following steps that an alkali solution and the Raney nickel-aluminum-X catalyst which is powder are uniformly mixed according to a mass ratio of (2: 1) to (10: 1) and then undergo a reaction with stirring, wherein the alkali solution is a sodium hydroxide or potassium hydroxide solution having a concentration of 5 to 25wt%; after the reaction is finished, the reaction products are washed by distilled water and anhydrous ethanol until a pH value of the reaction products is 7; and the reaction products having a pH value of 7 are preserved in ethanol. In the presence of the Raney nickel-aluminum-X catalyst, in hydrogenation preparation of 1,4-butanediol from 1,4-butynediol, a conversion rate is in a range of 98 to 100% and selectivity of 1,4-butanediol is in a range of 90 to 98%.

Description

Technical field [0001] The present invention is the field of organic chemical catalysts, and specifically a method for preparing and activating methods for 1,4-butanol hydrogen hydrogenation of 1,4-butanol. Background technique [0002] 1,4-butanol (BDO) is a very important organic synthetic intermediate. It is widely used in the production of polyphyamisytolitetal (PTMEG) and polyzibenal dilately glycol (PBT)., Tetra Hydrogen Fu Fu (THF) and other fields, as well as the pharmaceutical and cosmetics industry.At present, there are many processes in the production of BDOs in the world. Among them, the most widely used is the REPPE method, that is, the first formaldehyde and acetylene are prepared by formaldehyde and acetylene.Method.In a process of butyl hydrogen glycol in the United States Patent 2967893, the catalyst used is to add a certain percentage of CU to the reaction solution of the nickel catalyst of the skeleton 2+ , To improve the activity of catalysts.This method has t...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): B01J25/02B01J37/00B01J25/04C07C29/17C07C31/20
CPCY02P20/584
Inventor 胡燕李耀会章小林张雄斌李新怀吕小婉李小定
Owner HAISO TECH