CN108014802A - Prepare the catalyst and application method of alcohol - Google Patents
Prepare the catalyst and application method of alcohol Download PDFInfo
- Publication number
- CN108014802A CN108014802A CN201610962302.6A CN201610962302A CN108014802A CN 108014802 A CN108014802 A CN 108014802A CN 201610962302 A CN201610962302 A CN 201610962302A CN 108014802 A CN108014802 A CN 108014802A
- Authority
- CN
- China
- Prior art keywords
- solution
- oxide
- grams
- catalyst
- parts
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/80—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with zinc, cadmium or mercury
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
- C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
- C07C29/147—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof
- C07C29/149—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof with hydrogen or hydrogen-containing gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The present invention relates to a kind of catalyst and application method for preparing alcohol.Prepare in alcohol technology that there are the technical problem that hydrogen ester is lower than excessive, air speed and selectivity of product is poor present invention mainly solves existing.The present invention by using in terms of parts by weight including following components：A) 20~50 parts of metallic coppers or its oxide；B) metallic zinc or its oxide are selected from for 0~50 part；C) metallic iron or its oxide are selected from for 0~20 part；D) IV B races at least one element or its oxide are selected from for 0~20 part；E) 1~20 part of carrier, carrier are selected from least one of silica, aluminium oxide and molecular sieve；Wherein, component b), component c) and the component d) technical solutions for being zero when different preferably solve the problems, such as this, in the industrial production that alcohol is prepared available for ester through hydrogenation.
Description
Technical field
The invention belongs to field of catalytic chemistry, more particularly to a kind of catalyst and application method for preparing alcohol.
Background technology
1,6- hexylene glycol is a kind of important fine chemical material, plays the polyurethane elastomer mainly for the production of high-quality
Resin, polyester type plasticizer, ultraviolet-curing paint, makrolon, medicine intermediate, the thermostabilization modifying agent of lubricating oil, food
Product additive etc..1,6- hexylene glycol has two end position hydroxyls, and this structure can preferably participate in polymerisation, while 1,6-
The carbochain of hexylene glycol is longer, can effectively improve the mechanical strength of polymer.In terms of dyestuff and polyester, 1,6- hexylene glycol
The color and luster and adsorption capacity of product are improved, and there is good photostability.1,6-HD is also widely used in poly-
It in the production of urethane, can effectively improve the hydrolytic resistance and mechanical strength of product, be raw material production with 1,6- hexylene glycols
Its performance of polyurethane is much better than other kinds of polyurethane.In terms of the production of adhesive, pair that is produced using hexylene glycol as raw material
Ester of phthalic acid has faster crystallization rate and preferably viscosity, shows excellent flexibility and adhesion under cryogenic
Property.Therefore, hexylene glycol has been known as the new foundation stone of organic synthesis.The development of Chinese polyurethane, coiled material, paint industry drives
Domestic hexylene glycol consumption increases rapidly, since 1, the 6- hexylene glycol imports dependency degree of domestic market is high and import volume is with annual
10% speed increase, thus exploitation possess independent intellectual property right 1,6- hexylene glycol production technologies it is very urgent.At present more
Ripe 1,6- hexylene glycol manufacture methods are for raw material with 1,6- adipic acids, and esterification generation adipic acid diformazan is carried out with methanol
Ester, then hydrogenated obtain 1,6- hexylene glycols.
US6407294B1 discloses a kind of side that adipate ester and 6 hydroxycaproic acid ester through hydrogenation are prepared to 1,6-HD
Method, catalyst contains copper, manganese and aluminium as basis, or uses copper in Ruan.At 190 DEG C, 4.5MPa, hydrogen/ester molar ratio
280：1, when air speed 0.1 is small-1, feed stock conversion 100%, selectivity of product 98%, the preferable experimental result of the method acquirement, but
It is that the required hydrogen/ester molar ratio of reaction is of a relatively high and air speed is relatively low.
CN102380389B discloses a kind of catalyst of hexanedioic acid dialkyl ester Hydrogenation for 1,6- hexylene glycols, the catalysis
The component of percentage composition by weight in agent：Cu 5-30%；Ni 2-10%；B 5-20%；Metallic addition M 0-5%；It is porous
Carrier surplus.The catalyst of preparation is reduced using sodium borohydride/potassium borohydride, is applied to 1,6- adipic acid dialkyl group
Ester through hydrogenation is prepared in the reaction of hexylene glycol, and pressure needed for reaction system is higher (＞ 10MPa).
CN101531568B discloses a kind of preparation method of dimethyl adipate hydrogenation catalyst：Mesopore silicon oxide is carried
Body and the aqueous solution containing mantoquita, stirring, microwave are evaporated, microwave drying and roasting, up to hydrogenation catalyst.In the method for the present invention
, can not possibly large area use in commercial Application using microwave treatment catalyst.In addition, catalyst is for dimethyl adipate
In hydrogenation reaction, feed stock conversion 90% or so, the selective ＜ 90% of product.
CN101113128A discloses a kind of method of dimethyl adipate Hydrogenation for 1,6- hexylene glycols, wherein, catalysis
Agent is cupric oxide 25~60% by weight percentage, zinc oxide 25~60%, aluminium oxide 10~30%, which is used for oneself two
Dimethyl phthalate hydrogenation reaction prepares 1,6- hexylene glycols, feed stock conversion ＞ 99%, selectivity of product ＞ 96%.The patent is to catalysis
The details of agent are not described further.
In conclusion Cu catalyst prepared by the prior art is applied to hexanedioic acid dialkyl ester Hydrogenation for 1,6- hexylene glycols
During, there are part the deficiencies of hydrogen/ester molar ratio height, reaction pressure height, preparation method limitation, catalyst stability.
The content of the invention
The first technical problem to be solved by the present invention is to exist in the prior art to be difficult to prepare the good ester selection of stability
Property hydrogenation catalyst technical problem, there is provided a kind of new ester through hydrogenation prepares the catalyst of alcohol, the catalyst have stability it is good,
Good conversion ratio and selectivity, catalyst are easy to the advantages that shaping.The two of technical problem solved by the invention are to provide one
Kind and the purposes for solving one of technical problem corresponding catalyst.
To solve one of above-mentioned technical problem, the technical solution adopted by the present invention is as follows：A kind of catalyst for preparing alcohol, with
Parts by weight meter includes following components：
A) 20~50 parts of metallic coppers or its oxide；
B) metallic zinc or its oxide are selected from for 0~50 part；
C) metallic iron or its oxide are selected from for 0~20 part；
D) IV B races at least one element or its oxide are selected from for 0~20 part；
E) 1~20 part of carrier, carrier are selected from least one of aluminium oxide, silica and molecular sieve；
Wherein, it is zero when component b), component c) are different with component d).
In above-mentioned technical proposal, in terms of parts by weight, the dosage of metallic copper or its oxide is preferably 25~45 parts, more excellent
Elect 30~45 parts as；Metallic zinc or the dosage of its oxide are preferably 35~55 parts, more preferably 35~50 parts；Metallic iron or its
The dosage of oxide is 1~15 part, more preferably 2~12 parts；Use selected from least one of IV B races element or its oxide
Measure as 1~15 part, more preferably 2~12 parts；The dosage of alumina support is preferably 1~15 part, more preferably 1~10 part.
In above-mentioned technical proposal, the element in IV B races is selected from least one of titanium, zirconium；It is furthermore preferred that titanium oxide and
The weight ratio of zirconium oxide is (1：9)~(1：1).
In above-mentioned technical proposal, carrier is preferably aluminium oxide.
In above-mentioned technical proposal, it is preferred that carrier is selected from aluminium oxide and/or silica；It is furthermore preferred that aluminium oxide and oxygen
The weight ratio of SiClx is (9：1)~(99：1).
To solve the two of above-mentioned technical problem, the technical solution adopted by the present invention is as follows：A kind of 1,6-HD of preparing
Method, is 100~250 in hydrogen/ester molar ratio, volume space velocity is 0.1~1.5 using hexanedioic acid dialkyl ester and hydrogen as raw material
Hour-1, reaction temperature is 150~250 DEG C, and under the conditions of reaction pressure is 1.0~10.0MPa, raw material is contacted with above-mentioned catalyst
Reaction, makes the hexanedioic acid dialkyl ester in raw material be hydroconverted into 1,6- hexylene glycols.
In above-mentioned technical proposal, hydrogen ester molar ratio is preferably 150~200；When volume space velocity is preferably 0.1~0.6 small-1；
Reaction temperature is preferably 160~220 DEG C；Reaction pressure is preferably 4.0~6.0MPa.
The preparation method of catalyst of the present invention is：(a) by mantoquita, zinc salt, builder salts and aluminium/silicon source wiring solution-forming I；(b)
Deposited salt wiring solution-forming II needed for active component；In 50~90 DEG C of conditions, solution I is mixed with solution II, controls the pH of terminal
6.0~8.0, when aging 3~6 is small, filtering, roasts for 300~600 DEG C in washed, dry, air atmosphere, is molded and urges to obtain the final product
Agent finished product.Finished catalyst need to only lead to hydrogen reducing in the reactor and can be used.
In above-mentioned technical proposal, it is preferred that molding mode is compression molding.
The selection that the catalyst of the present invention is suitable for hexanedioic acid dialkyl ester is hydrogenated with, preferably to 1,6- dimethyl adipates
Or the hydrogenation of 1,6- diethylene adipates；Above-mentioned catalyst is reacted suitable for ester through hydrogenation.
Above-mentioned catalyst is reacted suitable for hydrogenation of oxalate for preparing ethylene glycol.
Above-mentioned catalyst is reacted suitable for acetate preparation of ethanol by hydrogenating.
It is anti-that above-mentioned catalyst is suitable for 1,4 cyclohexanedicarboxylic acid dimethyl ester Hydrogenation 1,4 cyclohexanedicarboxylic acid dimethanol
Should.
During the catalyst of the present invention is used for hexanedioic acid dialkyl ester Hydrogenation for 1,6- hexylene glycols, copper, copper oxidation
Thing and its mixture are main active components, the high dispersive of active component be reactivity and catalyst stability it is important because
Element.And the catalyst of carrier is made using aluminium oxide, the more acid selectivity to product of carrier surface has considerable influence, Yi Fa
Produce etherificate, dehydration and the dehydration etherificate of thing.For 1,6- di adipates Hydrogenation for the reaction of 1,6- hexylene glycols in itself, mainly
There are four class side reactions：(1) raw material side reaction, generation cyclopentanol, methylcyclopentanol, cyclopentyl-ethanol occur for dimethyl adipate；
(2) the dehydration etherificate generation hexamethylene ether of product 1,6-HD；(3) the excessive hydrogenation generation hexanol of product 1,6-HD；(4) produce
Terminal hydroxy group dehydration generation 5- hexenols and 5- hexene methyl ethers occur for thing 1,6-HD；(5) raw material dimethyl adipate and production
Ester exchange reaction occurs for thing 1,6- hexylene glycols, generates higher boiling C12 esters.Wherein, (2), (3), (4), (5) it is excess by carrier surface
Caused by acidity.In order to solve this problem, the present invention both ensure that active component by being introduced into element in iron and IV B races
High dispersive, in turn ensure that the good thermal stability for preparing catalyst.The catalyst of the present invention is for 1,6- adipic acid diformazans
Keep good with high feed stock conversion and high 1,6-HD selectivity and catalyst activity during ester selective hydrogenation.
The catalyst prepared using the present invention, is 190 DEG C in reaction temperature using dimethyl adipate and hydrogen as raw material,
Reaction pressure is 5.0MPa, and hydrogen/ester molar ratio is 170:1, when air speed is 0.2 small-1Under conditions of, dimethyl adipate conversion ratio
＞ 99%, 1,6- hexylene glycol liquid phase selective ＞ 98.5%, catalyst continuously run 1000 it is small when, for 1,6- hexylene glycol liquid phases
For selectivity, 0.1% is often improved on the basis of 98% and is also required to pay performing creative labour, therefore technical scheme
Achieve preferable technique effect.
In concept used in the present invention, carboxylate Hydrogenation for alcohol conversion ratio and molar selectivity calculation formula such as
Under：
Below by embodiment, the invention will be further elaborated, but these embodiments are not anyway to this hair
Bright scope is construed as limiting.
Embodiment
【Embodiment 1】
73.6 grams of nine water aluminum nitrate is weighed, the solution that concentration is 0.6M is configured to, stirs evenly, be transferred to three-necked flask
In, it is heated to 65 DEG C.Neutralize the solution with 25% ammonium hydroxide, the pH value for controlling terminal is 8.0, be made gel aging 4 it is small when, take out
Filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate, 50.5 grams of nine water ferric nitrate are weighed, being configured to concentration is
The solution of 0.6M, is solution I；137.6 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.Will system
Standby alumina powder is placed in the liquid of bottom, is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, and control endpoint pH is left 7.0
The right side, filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding obtains catalyst
C1, catalyst composition are shown in Table 1.
【Embodiment 2】
73.6 grams of nine water aluminum nitrate is weighed, the solution that concentration is 0.6M is configured to, stirs evenly, be transferred to three-necked flask
In, it is heated to 65 DEG C.Neutralize the solution with 25% ammonium hydroxide, the pH value for controlling terminal is 8.0, be made gel aging 4 it is small when, take out
Filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate, 50.5 grams of nine water ferric nitrate are weighed, being configured to concentration is
The solution of 0.6M, is solution I；137.6 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.Will system
Standby alumina powder is placed in the liquid of bottom, is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, and control endpoint pH is left 7.0
The right side, filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, roller forming obtains catalyst
C2, catalyst composition are shown in Table 1.
【Embodiment 3】
73.6 grams of nine water aluminum nitrate is weighed, the solution that concentration is 0.6M is configured to, stirs evenly, be transferred to three-necked flask
In, it is heated to 65 DEG C.Neutralize the solution with 25% ammonium hydroxide, the pH value for controlling terminal is 8.0, be made gel aging 4 it is small when, take out
Filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate, 50.5 grams of nine water ferric nitrate are weighed, being configured to concentration is
The solution of 0.6M, is solution I；137.6 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.Will system
Standby alumina powder is placed in the liquid of bottom, is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, and control endpoint pH is left 7.0
The right side, filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, extruded moulding obtains catalyst
C3, catalyst composition are shown in Table 1.
【Embodiment 4】
1.0 grams of silica powder is weighed, adds in round-bottomed flask, weighs 66.2 grams of nine water aluminum nitrate, being configured to concentration is
The solution of 0.6M, stirs evenly, and is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, controls terminal
PH value is 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate, 50.5 grams of nine water ferric nitrate are weighed, being configured to concentration is
The solution of 0.6M, is solution I；137.6 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.Will system
Standby silica-alumina powder is placed in the liquid of bottom, is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, controls endpoint pH
Filtered when gained slurry aging 3 is small 7.0 or so, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding obtains
Catalyst C4, catalyst composition are shown in Table 1.
【Embodiment 5】
0.1 gram of silica powder is weighed, adds in round-bottomed flask, weighs 72.8 grams of nine water aluminum nitrate, being configured to concentration is
The solution of 0.6M, stirs evenly, and is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, controls terminal
PH value is 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate, 50.5 grams of nine water ferric nitrate are weighed, being configured to concentration is
The solution of 0.6M, is solution I；137.6 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.Will system
Standby silica-alumina powder is placed in the liquid of bottom, is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, controls endpoint pH
Filtered when gained slurry aging 3 is small 7.0 or so, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding obtains
Catalyst C5, catalyst composition are shown in Table 1.
【Embodiment 6】
Weigh 60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate, 8.2 grams of nine water ferric nitrate, nine water aluminum nitrates
132.4 grams, the solution that concentration is 0.6M is configured to, is solution I；181.8 grams of sodium carbonate is weighed, it is 1.0M's to be configured to concentration
Solution, is solution II.Water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, control endpoint pH 7.0 or so,
Filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding obtains catalyst C6, urges
Agent composition is shown in Table 1.
【Embodiment 7】
Weigh 60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate, 25.2 grams of nine water ferric nitrate, nine water aluminum nitrates
110.3 grams, the solution that concentration is 0.6M is configured to, is solution I；178.1 grams of sodium carbonate is weighed, it is 1.0M's to be configured to concentration
Solution, is solution II.Water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, control endpoint pH 7.0 or so,
Filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding obtains catalyst C7, urges
Agent composition is shown in Table 1.
【Embodiment 8】
Weigh 60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate, 4.0 grams of nine water ferric nitrate, nine water aluminum nitrates
141.2 grams, the solution that concentration is 0.6M is configured to, is solution I；183.3 grams of sodium carbonate is weighed, it is 1.0M's to be configured to concentration
Solution, is solution II.Water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, control endpoint pH 7.0 or so,
Filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding obtains catalyst C8, urges
Agent composition is shown in Table 1.
【Embodiment 9】
34.9 grams of five water zirconium nitrate, 66.2 grams of nine water aluminum nitrate, 6.4 grams of magnesium nitrate hexahydrate are weighed, being configured to concentration is
The solution of 0.6M, stirs evenly, and is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, controls terminal
PH value is 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate are weighed, is configured to the solution that concentration is 0.4M, it is as molten
Liquid I；115.7 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.By zirconium oxide-oxidation of preparation
Aluminium-magnesium oxide powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, and control endpoint pH exists
7.0 or so, filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding is urged
Agent C9, catalyst composition are shown in Table 1.
【Embodiment 10】
7.0 grams of five water zirconium nitrate, 125.0 grams of nine water aluminum nitrate, 6.4 grams of magnesium nitrate hexahydrate are weighed, being configured to concentration is
The solution of 0.6M, stirs evenly, and is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, controls terminal
PH value is 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate are weighed, is configured to the solution that concentration is 0.4M, it is as molten
Liquid I；115.7 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.By zirconium oxide-oxidation of preparation
Aluminium-magnesium oxide powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, and control endpoint pH exists
7.0 or so, filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding is urged
Agent C10, catalyst composition are shown in Table 1.
【Embodiment 11】
17.5 grams of five water zirconium nitrate, 103.0 grams of nine water aluminum nitrate, 6.4 grams of magnesium nitrate hexahydrate are weighed, being configured to concentration is
The solution of 0.6M, stirs evenly, and is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, controls terminal
PH value is 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate are weighed, is configured to the solution that concentration is 0.4M, it is as molten
Liquid I；115.7 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.By zirconium oxide-oxidation of preparation
Aluminium-magnesium oxide powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, and control endpoint pH exists
7.0 or so, filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding is urged
Agent C11, catalyst composition are shown in Table 1.
【Embodiment 12】
2.8 grams of five water zirconium nitrate, 133.9 grams of nine water aluminum nitrate, 6.4 grams of magnesium nitrate hexahydrate are weighed, being configured to concentration is
The solution of 0.6M, stirs evenly, and is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, controls terminal
PH value is 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate are weighed, is configured to the solution that concentration is 0.4M, it is as molten
Liquid I；115.7 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.By zirconium oxide-oxidation of preparation
Aluminium-magnesium oxide powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, and control endpoint pH exists
7.0 or so, filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding is urged
Agent C12, catalyst composition are shown in Table 1.
【Embodiment 13】
10 grams of titanium oxide powder is weighed, adds in round-bottomed flask, weighs 73.6 grams of nine water aluminum nitrate, being configured to concentration is
The solution of 0.6M, stirs evenly, and is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, controls terminal
PH value is 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate are weighed, is configured to the solution that concentration is 0.4M, it is as molten
Liquid I；115.7 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.By the titanium dioxide-aluminum oxide of preparation
Powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, control endpoint pH 7.0 or so,
Filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding obtains catalyst C13,
Catalyst composition is shown in Table 1.
【Embodiment 14】
2 grams of titanium oxide powder is weighed, adds in round-bottomed flask, weighs 132.4 grams of nine water aluminum nitrate, being configured to concentration is
The solution of 0.6M, stirs evenly, and is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, controls terminal
PH value is 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate are weighed, is configured to the solution that concentration is 0.4M, it is as molten
Liquid I；115.7 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.By the titanium dioxide-aluminum oxide of preparation
Powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, control endpoint pH 7.0 or so,
Filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding obtains catalyst C14,
Catalyst composition is shown in Table 1.
【Embodiment 15】
5 grams of titanium oxide powder is weighed, adds in round-bottomed flask, weighs 110.3 grams of nine water aluminum nitrate, being configured to concentration is
The solution of 0.6M, stirs evenly, and is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, controls terminal
PH value is 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate are weighed, is configured to the solution that concentration is 0.4M, it is as molten
Liquid I；115.7 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.By the titanium dioxide-aluminum oxide of preparation
Powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, control endpoint pH 7.0 or so,
Filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding obtains catalyst C15,
Catalyst composition is shown in Table 1.
【Embodiment 16】
0.8 gram of titanium oxide powder is weighed, adds in round-bottomed flask, weighs 141.2 grams of nine water aluminum nitrate, being configured to concentration is
The solution of 0.6M, stirs evenly, and is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, controls terminal
PH value is 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate are weighed, is configured to the solution that concentration is 0.4M, it is as molten
Liquid I；115.7 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.By the titanium dioxide-aluminum oxide of preparation
Powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, control endpoint pH 7.0 or so,
Filtered when gained slurry aging 3 is small, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, compression molding obtains catalyst C16,
Catalyst composition is shown in Table 1.
【Embodiment 17】
17.4 grams of five water zirconium nitrate, 73.6 grams of nine water aluminum nitrate are weighed, is configured to the solution that concentration is 0.6M, stirring is equal
It is even, it is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, the pH value for controlling terminal is 8.0, is made solidifying
When glue aging 4 is small, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate, 25.3 grams of nine water ferric nitrate are weighed, being configured to concentration is
The solution of 0.4M, is solution I；126.6 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.Will system
Standby Zirconia-alumina powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, and control is eventually
Point pH value is filtered when gained slurry aging 3 is small 7.0 or so, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, tabletting into
Type obtains catalyst C17, and catalyst composition is shown in Table 1.
【Embodiment 18】
5 grams of titanium oxide powder is weighed, adds in round-bottomed flask, weighs 110.3 grams of nine water aluminum nitrate, being configured to concentration is
The solution of 0.6M, stirs evenly, and is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, controls terminal
PH value is 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
60.4 grams of nitrate trihydrate copper, 220.4 grams of zinc nitrate hexahydrate, 25.3 grams of nine water ferric nitrate are weighed, being configured to concentration is
The solution of 0.4M, is solution I；126.6 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.Will system
Standby titanium dioxide-aluminum oxide powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, and control is eventually
Point pH value is filtered when gained slurry aging 3 is small 7.0 or so, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, tabletting into
Type obtains catalyst C18, and catalyst composition is shown in Table 1.
【Embodiment 19】
34.9 grams of five water zirconium nitrate, 73.6 grams of nine water aluminum nitrate are weighed, is configured to the solution that concentration is 0.6M, stirring is equal
It is even, it is transferred in flask, is heated to 65 DEG C.The solution is neutralized with 25% ammonium hydroxide, the pH value for controlling terminal is 8.0, is made solidifying
When glue aging 4 is small, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
105.7 grams of nitrate trihydrate copper, 146.9 grams of zinc nitrate hexahydrate, 25.3 grams of nine water ferric nitrate are weighed, being configured to concentration is
The solution of 0.4M, is solution I；119.8 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.Will system
Standby Zirconia-alumina powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is added dropwise with II cocurrent of solution, and control is eventually
Point pH value is filtered when gained slurry aging 3 is small 7.0 or so, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small, tabletting into
Type obtains catalyst C19, and catalyst composition is shown in Table 1.
【Embodiment 20】
5 grams of titanium oxide powder is weighed, adds in round-bottomed flask, weighs 73.6 grams of nine water aluminum nitrate, five water zirconium nitrates 17.5
Gram, the solution that concentration is 0.6M is configured to, stirs evenly, is transferred in flask, be heated to 65 DEG C.Being neutralized with 25% ammonium hydroxide should
Solution, the pH value for controlling terminal are 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
105.7 grams of nitrate trihydrate copper, 146.9 grams of zinc nitrate hexahydrate, 25.3 grams of nine water ferric nitrate are weighed, being configured to concentration is
The solution of 0.4M, is solution I；119.8 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.Will system
Standby zirconia-titania-alumina powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is dripped with II cocurrent of solution
Add, control endpoint pH is filtered when gained slurry aging 3 is small 7.0 or so, washing, 90 DEG C of dryings, and 500 DEG C of roastings 4 are small
When, compression molding obtains catalyst C20, and catalyst composition is shown in Table 1.
【Embodiment 21】
1 gram of titanium oxide powder is weighed, adds in round-bottomed flask, weighs 73.6 grams of nine water aluminum nitrate, five water zirconium nitrates 31.4
Gram, the solution that concentration is 0.6M is configured to, stirs evenly, is transferred in flask, be heated to 65 DEG C.Being neutralized with 25% ammonium hydroxide should
Solution, the pH value for controlling terminal are 8.0, be made gel aging 4 it is small when, filter, washing, 90 DEG C of dryings, when 500 DEG C of roastings 4 are small.
105.7 grams of nitrate trihydrate copper, 146.9 grams of zinc nitrate hexahydrate, 25.3 grams of nine water ferric nitrate are weighed, being configured to concentration is
The solution of 0.4M, is solution I；119.8 grams of sodium carbonate is weighed, is configured to the solution that concentration is 1.0M, is solution II.Will system
Standby zirconia-titania-alumina powder is placed in the liquid of bottom, and water-bath is maintained at 75 DEG C, and solution I is dripped with II cocurrent of solution
Add, control endpoint pH is filtered when gained slurry aging 3 is small 7.0 or so, washing, 90 DEG C of dryings, and 500 DEG C of roastings 4 are small
When, compression molding obtains catalyst C21, and catalyst composition is shown in Table 1.
【Comparative example 1】
Comparative example catalyst is prepared according to the patent CN1565729A methods provided, forms and is calculated as 60 parts with parts by weight
CuO-20 parts of ZnO-10 parts of Al2O3- 10 parts of BaO.
【Comparative example 2】
Comparative example catalyst is prepared according to the patent CN1097038C methods provided, forms and is calculated as 70 parts with parts by weight
CuO-10 parts of Mn2O3- 20 parts of Al2O3。
Table 1
【Embodiment 22】
This example demonstrates that 1~21 gained catalyst of embodiment is in dimethyl adipate or diethylene adipate selection hydrogenation
Middle application.
1~21 each 30mL of gained catalyst of the embodiment of the present invention is taken, using pure hydrogen, 10h is reduced at 300 DEG C.With oneself
Adipate and pure hydrogen are raw material, change process conditions tested, analyzed using on-line chromatograph, 100 it is small when it is anti-
2 should be the results are shown in Table.
【Comparative example 3】
Comparative example 1,2 gained catalyst 30ml of comparative example are taken, when reduction 10 is small under 300 DEG C of pure hydrogen.With adipic acid
Dialkyl ester and pure hydrogen are tested for raw material, are analyzed using on-line chromatograph, reaction result is shown in Table 2.
Table 2
【Embodiment 23】
This example demonstrates that examinations of the 21 gained catalyst C21 of embodiment when during dimethyl adipate selection is hydrogenated with 1000 is small
Test result.
21 gained catalyst C21 30mL of the embodiment of the present invention are taken, using pure hydrogen, 10h is reduced at 250 DEG C.Reacting
Temperature is 190 DEG C, reaction pressure 5.0MPa, and hydrogen/ester molar ratio is 170:1, when air speed is 0.2 small-1Under conditions of, gained sample
Product are analyzed using on-line chromatograph, and reaction result is shown in Table 3.
【Comparative example 4】
2 gained catalyst CD2 30ml of comparative example are taken, when reduction 10 is small under 250 DEG C of pure hydrogen.Take embodiment 23
Same materials, same reaction conditions are tested, and reaction result is shown in Table 3.
Table 3
【Embodiment 24~27】
The catalyst C21 that embodiment 21 is obtained is used for ester through hydrogenation, and raw material, reaction condition and evaluation result are shown in Table 4.
Table 4
Claims (10)
- A kind of 1. catalyst for preparing alcohol, including following components in terms of parts by weight：A) 20~50 parts of metallic coppers or its oxide；B) metallic zinc or its oxide are selected from for 0~50 part；C) metallic iron or its oxide are selected from for 0~20 part；D) IV B races at least one element or its oxide are selected from for 0~20 part；E) 1~20 part of carrier, carrier are selected from least one of aluminium oxide, silica and molecular sieve；Wherein, it is zero when component b), component c) are different with component d).
- 2. the catalyst according to claim 1 for preparing alcohol, it is characterised in that in terms of parts by weight, metallic copper or its oxidation The dosage of thing is 25~45 parts, and the dosage of metallic zinc or its oxide is 35~55 parts, and the dosage of metallic iron or its oxide is 1 ~15 parts, the dosage selected from least one of IV B races element or its oxide is 1~15 part, and the dosage of carrier is 1~15 Part.
- 3. the catalyst according to claim 2 for preparing alcohol, it is characterised in that in terms of parts by weight, metallic copper or its oxidation The dosage of thing is 30~45 parts, and the dosage of metallic zinc or its oxide is 35~50 parts, the dosage 2 of metallic iron or its oxide~ 12 parts, the dosage selected from least one of IV B races element or its oxide is 2~12 parts, and the dosage of carrier is 1~10 part.
- 4. the catalyst according to claim 1 for preparing alcohol, it is characterised in that carrier is selected from aluminium oxide and/or silica.
- 5. the catalyst according to claim 1 for preparing alcohol, it is characterised in that the weight ratio of aluminium oxide and silica is (9： 1)~(99：1).
- 6. the catalyst according to claim 1 for preparing alcohol, it is characterised in that the element in IV B races is selected from titanium, zirconium At least one of.
- 7. the catalyst according to claim 6 for preparing alcohol, it is characterised in that the weight ratio of titanium oxide and zirconium oxide is (1： 9)~(1：1).
- 8. the method that one kind prepares 1,6- hexylene glycols, with 1,6- hexanedioic acid dialkyl esters and hydrogen for raw material, in hydrogen/ester molar ratio For 100~250, volume space velocity for 0.1~1.5 it is small when-1, reaction temperature is 150~250 DEG C, reaction pressure for 1.0~ Under the conditions of 10.0MPa, raw material and any one of the claim 1~7 catalyst haptoreaction, make 1, the 6- adipic acids in raw material Dialkyl ester is hydroconverted into 1,6-HD.
- 9. any one of claim 1~7 catalyst is used for the purposes in ester through hydrogenation reaction.
- 10. any one of claim 1~7 catalyst is used for the purposes in the reaction of acetate preparation of ethanol by hydrogenating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610962302.6A CN108014802A (en) | 2016-11-04 | 2016-11-04 | Prepare the catalyst and application method of alcohol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610962302.6A CN108014802A (en) | 2016-11-04 | 2016-11-04 | Prepare the catalyst and application method of alcohol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108014802A true CN108014802A (en) | 2018-05-11 |
Family
ID=62084116
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610962302.6A Pending CN108014802A (en) | 2016-11-04 | 2016-11-04 | Prepare the catalyst and application method of alcohol |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108014802A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112691674A (en) * | 2019-10-22 | 2021-04-23 | 中国石油化工股份有限公司 | Ester hydrogenation catalyst, preparation method and application thereof |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102712559A (en) * | 2009-11-17 | 2012-10-03 | 巴斯夫欧洲公司 | Method for producing a supported hydrogenation catalyst having increased hydrogenation activity |
| CN105032439A (en) * | 2015-07-29 | 2015-11-11 | 上海华谊（集团）公司 | Catalyst for producing sec-butyl alcohol and ethyl alcohol through sec-butyl acetate hydrogenationm, preparation method and application thereof |
| CN105363457A (en) * | 2014-08-27 | 2016-03-02 | 中国石油化工股份有限公司 | Catalyst used for carboxylic ester hydrogenation |
| CN105435797A (en) * | 2014-08-27 | 2016-03-30 | 中国石油化工股份有限公司 | A catalyst for carboxylate hydrogenation |
| CN105727962A (en) * | 2016-02-02 | 2016-07-06 | 上海华峰新材料研发科技有限公司 | Catalyst for preparing hexanediol from dimethyl adipate and preparation method and application thereof |
-
2016
- 2016-11-04 CN CN201610962302.6A patent/CN108014802A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102712559A (en) * | 2009-11-17 | 2012-10-03 | 巴斯夫欧洲公司 | Method for producing a supported hydrogenation catalyst having increased hydrogenation activity |
| CN105363457A (en) * | 2014-08-27 | 2016-03-02 | 中国石油化工股份有限公司 | Catalyst used for carboxylic ester hydrogenation |
| CN105435797A (en) * | 2014-08-27 | 2016-03-30 | 中国石油化工股份有限公司 | A catalyst for carboxylate hydrogenation |
| CN105032439A (en) * | 2015-07-29 | 2015-11-11 | 上海华谊（集团）公司 | Catalyst for producing sec-butyl alcohol and ethyl alcohol through sec-butyl acetate hydrogenationm, preparation method and application thereof |
| CN105727962A (en) * | 2016-02-02 | 2016-07-06 | 上海华峰新材料研发科技有限公司 | Catalyst for preparing hexanediol from dimethyl adipate and preparation method and application thereof |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112691674A (en) * | 2019-10-22 | 2021-04-23 | 中国石油化工股份有限公司 | Ester hydrogenation catalyst, preparation method and application thereof |
| CN112691674B (en) * | 2019-10-22 | 2023-08-29 | 中国石油化工股份有限公司 | Ester hydrogenation catalyst, and preparation method and application thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106607044A (en) | Catalyst and method for preparing 1, 6-hexanediol by hydrogenation of dialkyl 1, 6-adipate | |
| CN102388008B (en) | Method for producing 1,6-hexanediol by hydrogenation of oligo- and polyesters | |
| CN102806086B (en) | Preparation method of catalyst for coproducing isopropanol and methyl isobutyl ketone by acetone hydrogenation | |
| CN102617518B (en) | One-step preparation method for tetrahydrofuran by employing maleic anhydride gas phase hydrogenation | |
| CN103657658B (en) | Carboxylic ester hydrogenation catalyst and prepare the method for cyclohexanol and ethanol | |
| CN104926657B (en) | The method of oxalate gas phase hydrogenation synthesizing alcohol acid esters | |
| CN105435809B (en) | The method of hydrogenation catalyst and its preparation method and application and hydrogenation reaction | |
| CN108014815A (en) | Prepare the catalyst and method of alcohol | |
| CN106866360B (en) | Method for preparing 1, 6-hexanediol by catalytic conversion of 5-hydroxymethylfurfural | |
| CN102463122A (en) | Cu-Ag/SiO2 catalyst for hydrogenating oxalate | |
| CN108014805A (en) | Prepare the catalyst and its method of alcohol | |
| CN110467517A (en) | A kind of hydrogenation of acetophenone prepares the method and catalyst of alpha-phenyl ethyl alcohol | |
| CN102924233A (en) | Method for preparing propylene glycol by glycerin hydrogenolysis | |
| CN105037161A (en) | Continuous synthesis method of cyclohexane polyacid ester | |
| CN105363438B (en) | Synthesizing of glycolate ester catalyst, preparation method and its usage | |
| CN113426457B (en) | Catalyst for preparing alcohol by ketone hydrogenation and preparation method and application thereof | |
| CN103240095A (en) | Methyl acetate hydrogenation catalyst and preparation method thereof | |
| CN103664587B (en) | Method for preparing cyclohexyl acetate and method for preparing cyclohexanol ethanol | |
| CN103769110B (en) | A kind of BDO dehydrogenation gamma-butyrolacton catalyst and its preparation method and application | |
| CN105776134A (en) | Hydrogen production method by methanol-steam reforming | |
| CN108014802A (en) | Prepare the catalyst and application method of alcohol | |
| CN114054034B (en) | Multi-element copper-based non-noble metal hydrogenation catalyst, and preparation method and application thereof | |
| CN104870088B (en) | The manufacture method of alcohol catalyst for synthesizing, the manufacture device of alcohol and alcohol | |
| CN108014801A (en) | Produce the catalyst and method of alcohol | |
| CN102806085B (en) | Preparation method of catalyst for co-generating of isopropanol and diisobutyl ketone through acetone hydrogenation and application |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180511 |