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Hydrogenation Catalyst of Butadiene to 1,4-Diacetoxybutane

A technology of diacetoxybutane and hydrogenation catalyst, applied in the directions of metal/metal oxide/metal hydroxide catalyst, catalyst activation/preparation, physical/chemical process catalyst, etc., can solve the problem of diacetoxybutane Problems such as low yield and selectivity

Active Publication Date: 2020-02-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The technical problem to be solved by the present invention is the problem of low yield and selectivity of 1,4-diacetoxybutane, and a new butadiene is provided for the hydrogenation of 1,4-diacetoxybutane Catalyst, the catalyst has the characteristics of high yield and high selectivity of 1,4-diacetoxybutane

Method used

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  • Hydrogenation Catalyst of Butadiene to 1,4-Diacetoxybutane
  • Hydrogenation Catalyst of Butadiene to 1,4-Diacetoxybutane
  • Hydrogenation Catalyst of Butadiene to 1,4-Diacetoxybutane

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] Preparation of hydrogenation catalyst:

[0043] ① Ammonium chloroplatinite containing 2.05gPt ((NH 4 ) 2 PtCl 4 ) is dissolved in the hydrochloric acid aqueous solution that concentration is 8wt%, obtains impregnation solution 200ml, and 1L diameter 3mm, length 2cm, pore volume are 0.80cm 3 / g, the specific surface area is 1200cm 2 The coal-based cylindrical activated carbon carrier of / g is impregnated in the above-mentioned impregnating liquid, obtains catalyst precursor I;

[0044] ② Standing and aging for 24 hours to obtain catalyst precursor II;

[0045] ③ with a concentration of 8% (in N 2 h 4 ·H 2 The 500ml hydrazine hydrate of (2 weight ratio) reduces catalyst precursor II for 3h, obtains catalyst precursor III;

[0046] ④ washed with water to no chloride ion, dried at 50°C for 4 hours to obtain catalyst precursor IV;

[0047] ⑤ Manganese acetate (Mn(OAc) containing 1.95g Mn 2 4H 2 O) 180ml of aqueous solution was impregnated on the catalyst precursor...

Embodiment 2

[0053] Preparation of hydrogenation catalyst:

[0054] ① Ammonium chloroplatinite containing 2.05gPt ((NH 4 ) 2 PtCl 4 ) is dissolved in the hydrochloric acid aqueous solution that concentration is 8wt%, obtains impregnation solution 200ml, and 1L diameter 3mm, length 2cm, pore volume are 0.80cm 3 / g, the specific surface area is 1200cm 2 The coal-based cylindrical activated carbon carrier of / g is impregnated in the above-mentioned impregnating liquid, obtains catalyst precursor I;

[0055] ② Standing and aging for 24 hours to obtain catalyst precursor II;

[0056] ③ with a concentration of 8% (in N 2 h 4 ·H 2 The 500ml hydrazine hydrate of (2 weight ratio) reduces catalyst precursor II for 3h, obtains catalyst precursor III;

[0057] ④ washed with water to no chloride ion, dried at 50°C for 4 hours to obtain catalyst precursor IV;

[0058] ⑤ Ammonium tellurate containing 1.95g Te ((NH 4 ) 2 TeO 4 ) was fully dissolved in an aqueous acetic acid solution with a con...

Embodiment 3

[0088] Preparation of hydrogenation catalyst:

[0089] ① Ammonium chloroplatinite containing 2.05gPt ((NH 4 ) 2 PtCl 4 ) is dissolved in the hydrochloric acid aqueous solution that concentration is 8wt%, obtains impregnation solution 200ml, and 1L diameter 3mm, length 2cm, pore volume are 0.80cm 3 / g, the specific surface area is 1200cm 2 The coal-based cylindrical activated carbon carrier of / g is impregnated in the above-mentioned impregnating liquid, obtains catalyst precursor I;

[0090] ② Standing and aging for 24 hours to obtain catalyst precursor II;

[0091] ③ with a concentration of 8% (in N 2 h 4 ·H 2 The 500ml hydrazine hydrate of (2 weight ratio) reduces catalyst precursor II for 3h, obtains catalyst precursor III;

[0092] ④ washed with water to no chloride ion, dried at 50°C for 4 hours to obtain catalyst precursor IV;

[0093] ⑤ Ammonium perrhenate (NH 4 ReO 4 ) was dissolved in an aqueous acetic acid solution with a concentration of 10 wt%, to obtain...

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Abstract

The invention relates to a hydrogenation catalyst for preparation of 1,4-diacetoxybutane from butadiene and mainly solves the problems of low yield and selectivity of 1,4-diacetoxybutane in the priorart. The technical problem is better solved by means of the technical scheme as follows: the hydrogenation catalyst for preparation of 1,4-diacetoxybutane from butadiene comprises a carrier and activecomponents, wherein the carrier is activated carbon, the active components comprise a Pt element and a cocatalyst element, and the cocatalyst element is selected from at least one metal element of metalloid-group metals. The hydrogenation catalyst can be used for industrial production of 1,4-diacetoxybutane.

Description

technical field [0001] The invention relates to a hydrogenation catalyst for preparing 1,4-diacetoxybutane from butadiene. Background technique [0002] 1,4-Butanediol (1,4-BDO) is an important organic and fine chemical raw material, which is widely used in the fields of medicine, chemical industry, textile, papermaking, automobile and daily chemical industry. It can derive a series of high value-added fine chemical products. For example, tetrahydrofuran (THF), polybutylene terephthalate (PBT), γ-butyrolactone (GBL) and polyurethane resin (PU Resin) can be produced from 1,4-BDO, especially as the production of PBT engineering The basic raw material of plastic and PBT fiber has received extensive attention from research institutions. [0003] There are many process routes for the preparation of 1,4-butanediol. From the raw materials used, there are acetylene, ethylene, propylene, butadiene and maleic anhydride and other raw material routes. The same raw materials also have ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/42B01J23/656B01J27/057B01J37/02C07C67/283C07C69/16
CPCB01J23/42B01J23/6562B01J23/6567B01J27/0576B01J37/0201C07C67/283C07C69/16
Inventor 查晓钟杨运信
Owner CHINA PETROLEUM & CHEM CORP