CN106622220A - Hydrogenation catalyst, preparation method and application - Google Patents

Hydrogenation catalyst, preparation method and application Download PDF

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Publication number
CN106622220A
CN106622220A CN201610970790.5A CN201610970790A CN106622220A CN 106622220 A CN106622220 A CN 106622220A CN 201610970790 A CN201610970790 A CN 201610970790A CN 106622220 A CN106622220 A CN 106622220A
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hydrogenation catalyst
dimethyl
hydrogenation
brucite
catalyst
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CN201610970790.5A
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CN106622220B (en
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梅华
刘裕亮
焦宏伟
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JIANGSU NUOMENG CHEMICAL CO Ltd
Nanjing Tech University
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JIANGSU NUOMENG CHEMICAL CO Ltd
Nanjing Tech University
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/46Ruthenium, rhodium, osmium or iridium
    • B01J23/462Ruthenium
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C209/00Preparation of compounds containing amino groups bound to a carbon skeleton
    • C07C209/68Preparation of compounds containing amino groups bound to a carbon skeleton from amines, by reactions not involving amino groups, e.g. reduction of unsaturated amines, aromatisation, or substitution of the carbon skeleton
    • C07C209/70Preparation of compounds containing amino groups bound to a carbon skeleton from amines, by reactions not involving amino groups, e.g. reduction of unsaturated amines, aromatisation, or substitution of the carbon skeleton by reduction of unsaturated amines
    • C07C209/72Preparation of compounds containing amino groups bound to a carbon skeleton from amines, by reactions not involving amino groups, e.g. reduction of unsaturated amines, aromatisation, or substitution of the carbon skeleton by reduction of unsaturated amines by reduction of six-membered aromatic rings

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Catalysts (AREA)

Abstract

The invention relates to a hydrogenation catalyst as well as a preparation method and application of the hydrogenation catalyst, and in particular relates to a hydrogenation catalyst for synthesizing 3,3'-dimethyl-4,4'-diaminodicyclohexylmethane as well as a preparation method and application of the hydrogenation catalyst, and belongs to the technical field of chemistry. The catalyst is prepared from a carrier hydrotalcite and an active component metal ruthenium; the hydrotalcite is magnesium-aluminum or cerium-aluminum lamellar double-metal hydroxide. The catalyst has high catalytic activity and high selectivity, and is especially suitable for catalytic hydrogenation reaction for synthesizing the 3,3'-dimethyl-4,4'-diaminodicyclohexylmethane; reaction temperature and pressure are effectively reduced, and a product with relatively high content of stereoisomers can be obtained; requirements on equipment are not high and the catalyst has a good industrial application prospect.

Description

A kind of hydrogenation catalyst, preparation method and application
Technical field
The present invention relates to a kind of hydrogenation catalyst, its preparation method and application, more particularly to a kind of synthesis 3,3 '-diformazan Base -4, the hydrogenation catalyst of 4 '-diamino-dicyclohexyl methane, its preparation method and application, belong to technical field of chemistry.
Background technology
3,3 '-dimethyl -4,4 '-diamino-dicyclohexyl methane (MACM) is widely used in as a kind of important intermediate The synthesis of polyamide and polyimides, the polyamide or polyimide material of its synthesis have excellent calorifics, mechanics and optics Performance, is applied to the aspects such as aerospace industry, wind-power electricity generation and defence and military.Meanwhile, MACM can make as a kind of alicyclic diamine For polyurethane chain extender and epoxy curing agent.The elasticity of the existing rubber of polyurethane of MACM synthesis, there is the intensity of plastics again With excellent processing characteristics, especially there are other synthetic materials incomparable at the aspect such as sound insulation, heat-insulated, wear-resisting, oil resistant, elasticity Advantage;The polyamide of its synthesis has nontoxic, light weight, excellent mechanical strength, wearability and preferable corrosion resistance;It is applied to Epoxy resin has that cohesiveness is strong, electrical insulating property is excellent, stable chemical nature and a series of excellent properties such as processing characteristics is good. In recent years, MACM applications at home and abroad expand rapidly, and the good MACM of production performance has great industrial value and business Value, and MACM stereoisomers ratio affects to a great extent range of application and downstream product performance.
At present, it is little with regard to the Patents of the production method of MACM, and industrially by monopolization production.Patents It is as follows:The hydrate and hydrophobic silica that ru oxide is disclosed in patent WO2009090179 obtains oxygen containing ruthenium after hydrogenation Used as catalyst, under the pressure of 200bar, MDT liquid melts are hydrogenated in the presence of a catalyst the suspension of compound Reaction, reaction is cooled to 230-240 DEG C and obtains target product.The patent is carried out at high temperature and pressure, higher to equipment requirements, And reacting under high temperature easily increases the by-product of generation, and for MACM stereoisomer ratios are not referred to.
Disclose in patent US20120289747 in 500mL reactors, with silicon dioxide carried ruthenium as catalyst, with The tetrahydrofuran solution of 17.7% ortho-aminotoluene is solvent, and at 75bar hydrogen pressures, 180 DEG C of temperature 2.5h is reacted, and is obtained 98.15% MACM yields, but do not refer to MACM stereoisomer ratios yet.
Disclose in patent WO2010005859 in 300mL reactors, with alumina load ruthenium as catalyst, with methyl Tetrahydrofuran is solvent, and at 70bar hydrogen pressures, 185 DEG C of temperature 3h is reacted, and obtains 85% MACM yields, and reports gas phase The isomer proportion that chromatography is obtained.
MACM products can be obtained using prior art, but be industrially typically required to the harsher bar such as High Temperature High Pressure Part, there is higher requirement to equipment.And the product obtained in small-sized reaction kettle for reaction, it is more difficult to high income is obtained, while first Isomer proportion also meets the MACM products of requirement, and the solvent cost for using is also of a relatively high.
The content of the invention
The purpose of the present invention is to be directed to the defect that prior art is present, a kind of synthesis 3 of proposition, 3 '-dimethyl -4,4 '-two Hydrogenation catalyst, the preparation method and application of amino bicyclic hexyl methane.
Present invention firstly provides a kind of synthesis 3,3 '-dimethyl -4,4 ' hydrogenation catalyst of-diamino-dicyclohexyl methane Agent, the hydrogenation catalyst is made up of active component and carrier, and the active component is the metal Ru that weight content is 3-10%, The carrier is brucite, and brucite weight content is 90-97%.
The brucite is magnalium or cerium aluminum layered double hydroxide.
Aluminum nitrate and the mol ratio of magnesium nitrate or cerous nitrate are 1-3 in the brucite:1.
The present invention further provides a kind of synthesis 3,3 '-dimethyl -4,4 ' hydrogenation catalyst of-diamino-dicyclohexyl methane The preparation method of agent, comprises the following steps:
Step one, aluminum nitrate and magnesium nitrate or cerous nitrate are dissolved in deionized water, obtain mixed solution A;
Step 2, weigh alkali compoundss and be dissolved in deionized water configuration alkali compoundss aqueous solution B;
Step 3,65 DEG C, do not stop stirring under conditions of, while Deca mixed solution A and alkali compoundss aqueous solution B enter Row co-precipitation, mixture ageing, filtration, drying, finally roasting 3 hours at 200 DEG C, obtain hydrotalcite supports;
Step 4, the powder that hydrotalcite supports are ground to form 30-50 mesh, add into the ruthenium saline solution containing 35-40wt% Stirring 2-2.5 hours, stand overnight, and filter, and filter cake is washed to neutrality, are dried at 120 DEG C, and hydrogen reducing at 200 DEG C is urged Agent Ru/LDH.
The mixed solution A concentration of said method is 15-30wt%.
The alkali compoundss aqueous solution B is LiOH, NaOH, KOH or NH3·H2One kind in O, concentration is 10- 25wt%.
The present invention further provides a kind of synthesis 3,3 '-dimethyl -4,4 ' hydrogenation of-diamino-dicyclohexyl methane urges The application of agent, for 3,3 '-dimethyl -4,4 '-MDA hydrogenation synthesizing reaction, reaction temperature is 160 DEG C, hydrogen Atmospheric pressure is 8Mpa, and tetrahydrofuran 60mL, 5g 3,3 '-dimethyl -4,4 '-diaminourea hexichol first are added in 500ml reactors Alkane, 0.8g hydrogenation catalysts, the response time is 5h.
Reaction equation is as follows:
3,3 '-dimethyl -4,4 '-MDA product isomer shown in formula I:
In above-mentioned application, 3,3 '-dimethyl -4,4 '-diamino-dicyclohexyl methane yield >=97%, 3,3 '-diformazan Base -4,4 '-MDA product assay >=30wt%.
The invention has the beneficial effects as follows easily preparing, catalysis activity is good, and selectivity is high, MACM high incomes, is particularly suited for synthesis 3,3 '-dimethyl -4, the catalytic hydrogenation reaction of 4 '-diamino-dicyclohexyl methane effectively reduces reaction temperature and pressure, without the need for Addition auxiliary agent is just obtained the product of higher proportion isomer shown in formula I, and low production cost should with good industrialization Use prospect.
Specific embodiment
Embodiment 1
37.5g ANN aluminium nitrate nonahydrates and the nitric hydrate magnesium of 55.3g bis- are dissolved in 500g deionized waters, mixing is made into molten Liquid A.Configuration 15wt% lithium hydroxide aqueous solution B.Under not stopping stirring at 65 DEG C, in four-hole boiling flask simultaneously Deca solution A and Solution B is co-precipitated, mixture ageing, filtration, filtration cakes torrefaction, and roasting 3 hours, grind at 200 DEG C, obtain brucite Support powder.Take 5g brucite powder and be added to stirring 2 hours in the aqueous solution of 0.6g ruthenic chlorides (ruthenium content is 37wt%), it is quiet Put overnight, filter, filter cake deionized water is washed till neutrality, be dried, hydrogen reducing at 200 DEG C.Obtain catalyst Ru/LDH-1.
Embodiment 2
37.5g ANN aluminium nitrate nonahydrates and the nitric hydrate magnesium of 36.9g bis- are dissolved in 400g deionized waters, mixed solution is made into A.Configuration 10wt% lithium hydroxide aqueous solution B.Under not stopping stirring at 65 DEG C, the simultaneously Deca solution A and molten in four-hole boiling flask Liquid B is co-precipitated, mixture ageing, filtration, filtration cakes torrefaction, and roasting 3 hours, grind at 200 DEG C, obtains brucite load Body powder.Take 5g brucite powder and be added to stirring 2 hours in the aqueous solution of 0.6g ruthenic chlorides (ruthenium content is 37wt%), stand Overnight, filter, filter cake deionized water is washed till neutrality, be dried, hydrogen reducing at 200 DEG C.Obtain catalyst Ru/LDH-2.
Embodiment 3
37.5g ANN aluminium nitrate nonahydrates and the nitric hydrate magnesium of 55.3g bis- are dissolved in 400g deionized waters, mixed solution is made into A.Configuration 20wt% sodium hydrate aqueous solution B.Under not stopping stirring at 65 DEG C, the simultaneously Deca solution A and molten in four-hole boiling flask Liquid B is co-precipitated, mixture ageing, filtration, filtration cakes torrefaction, and roasting 3 hours, grind at 200 DEG C, obtains brucite load Body powder.Take 5g brucite powder and be added to stirring 2 hours in the aqueous solution of 0.6g ruthenic chlorides (ruthenium content is 37wt%), stand Overnight, filter, filter cake deionized water is washed till neutrality, be dried, hydrogen reducing at 200 DEG C.Obtain catalyst Ru/LDH-3.
Embodiment 4
37.5g ANN aluminium nitrate nonahydrates and the nitric hydrate magnesium of 55.3g bis- are dissolved in 350g deionized waters, mixed solution is made into A.Configuration 20wt% potassium hydroxide aqueous solution B.Under not stopping stirring at 65 DEG C, the simultaneously Deca solution A and molten in four-hole boiling flask Liquid B is co-precipitated, mixture ageing, filtration, filtration cakes torrefaction, and roasting 3 hours, grind at 200 DEG C, obtains brucite load Body powder.Take 5g brucite powder and be added to stirring 2 hours in the aqueous solution of 1.2g ruthenic chlorides (ruthenium content is 37wt%), stand Overnight, filter, filter cake deionized water is washed till neutrality, be dried, hydrogen reducing at 200 DEG C.Obtain catalyst Ru/LDH-4.
Embodiment 5
37.5g ANN aluminium nitrate nonahydrates and the nitric hydrate ceriums of 43.4g six are dissolved in 450g deionized waters, mixed solution is made into A.Configuration 15wt% lithium hydroxide aqueous solution B.Under not stopping stirring at 65 DEG C, the simultaneously Deca solution A and molten in four-hole boiling flask Liquid B is co-precipitated, mixture ageing, filtration, filtration cakes torrefaction, and roasting 3 hours, grind at 200 DEG C, obtains brucite load Body powder.Take 5g brucite powder and be added to stirring 2 hours in the aqueous solution of 0.6g ruthenic chlorides (ruthenium content is 37wt%), stand Overnight, filter, filter cake deionized water is washed till neutrality, be dried, hydrogen reducing at 200 DEG C.Obtain catalyst Ru/LDH-5.
Embodiment 6
37.5g ANN aluminium nitrate nonahydrates and the nitric hydrate magnesium of 55.3g bis- are dissolved in 500g deionized waters, mixed solution is made into A.Configuration 10wt% ammonia spirit B.Under not stopping stirring at 65 DEG C, simultaneously Deca solution A and solution B are carried out in four-hole boiling flask Co-precipitation, mixture ageing, filtration, filtration cakes torrefaction, roasting 3 hours, grind at 200 DEG C, obtain hydrotalcite supports powder. Take 5g brucite powder and be added to stirring 2 hours in the aqueous solution of 0.84g ruthenic chlorides (ruthenium content is 37wt%), stand overnight, Filter, filter cake deionized water is washed till neutrality, be dried, hydrogen reducing at 200 DEG C.Obtain catalyst Ru/LDH-6.
Embodiment 7
37.5g ANN aluminium nitrate nonahydrates and the nitric hydrate ceriums of 43.4g six are dissolved in 500g deionized waters, mixed solution is made into A.Configuration 10wt% lithium hydroxide solution B.Under not stopping stirring at 65 DEG C, in four-hole boiling flask while Deca solution A and solution B It is co-precipitated, mixture ageing, filtration, filtration cakes torrefaction, roasting 3 hours, grind at 200 DEG C, obtain hydrotalcite supports Powder.Take 5g brucite powder and be added to stirring 2 hours in the aqueous solution of 0.36g ruthenic chlorides (ruthenium content is 37wt%), stand Overnight, filter, filter cake deionized water is washed till neutrality, be dried, hydrogen reducing at 200 DEG C.Obtain catalyst Ru/LDH-7.
Brucite supported ruthenium catalyst obtained in embodiment 1 to the methods described of embodiment 7 is used for into 3,3 '-dimethyl -4, 4 '-MDA (MDT) hydrogenation synthesis 3,3 '-dimethyl -4,4 '-diamino-dicyclohexyl methane (MACM) reaction, Test its catalyst performance.Specifically reaction condition is:It it is 160 DEG C in temperature, Hydrogen Vapor Pressure is under conditions of 8MPa, in 500mL Solvents tetrahydrofurane 60mL, 5g raw materials 3,3 '-dimethyl -4,4 '-MDA, 0.8g catalysis are added in reactor Agent, the response time is 5h.
Catalyst performance test result such as following table:
It can be seen that, the catalyst prepared by above example is synthesizing 3,3 '-dimethyl -4, the hexamethylene of 4 '-diaminourea two In the reaction of methylmethane, MACM high incomes are just obtained the product of higher proportion isomer shown in formula I without the need for adding auxiliary agent Product, with higher commercial price and value, are conducive to further synthesizing downstream product.
In addition to above-mentioned enforcement, the present invention can also have other embodiment.All employing equivalents or equivalent transformation are formed Technical scheme, all fall within the protection domain of application claims.

Claims (8)

1. a kind of hydrogenation catalyst, the hydrogenation catalyst is made up of active component and carrier, it is characterised in that:The activearm It is divided into the metal Ru that weight content is 3-10%, the carrier is brucite, and brucite weight content is 90-97%.
2. hydrogenation catalyst according to claim 1, it is characterised in that:The brucite is magnalium or cerium aluminum hydrotalcite.
3. hydrogenation catalyst according to claim 2, it is characterised in that:Aluminum nitrate and magnesium nitrate or nitre in the brucite The mol ratio of sour cerium is 1-3:1.
4. a kind of preparation method of hydrogenation catalyst, comprises the following steps:
Step one, aluminum nitrate and magnesium nitrate or cerous nitrate are dissolved in deionized water, obtain mixed solution A;
Step 2, weigh alkali compoundss and be dissolved in deionized water configuration alkali compoundss aqueous solution B;
Step 3,65 DEG C, do not stop stirring under conditions of, while Deca mixed solution A and alkali compoundss aqueous solution B are carried out altogether Precipitation, mixture ageing, filtration, drying, finally roasting 3 hours at 200 DEG C, obtain hydrotalcite supports;
Step 4, the powder that hydrotalcite supports are ground to form 30-50 mesh, add and are stirred into the ruthenium saline solution containing 35-40wt% 2-2.5 hours, stand overnight, and filter, and filter cake is washed to neutrality, are dried at 120 DEG C, and hydrogen reducing at 200 DEG C obtains catalyst Ru/LDH。
5. the preparation method of hydrogenation catalyst according to claim 4, it is characterised in that:The mixed solution A concentration is 15-30wt%.
6. the preparation method of hydrogenation catalyst according to claim 4, it is characterised in that:The alkali compoundss aqueous solution B is LiOH, NaOH, KOH or NH3·H2One kind in O, concentration is 10-25wt%.
7. a kind of application of hydrogenation catalyst, it is characterised in that:For 3,3 '-dimethyl -4,4 '-MDA hydrogenation Synthetic reaction, reaction temperature is 160 DEG C, and Hydrogen Vapor Pressure is 8Mpa, and tetrahydrofuran 60mL, 5g 3 are added in 500ml reactors, 3 '-dimethyl -4,4 '-MDA, 0.8g hydrogenation catalysts, the response time is 5h.
8. the application of hydrogenation catalyst according to claim 7, it is characterised in that:3,3 '-dimethyl -4,4 '-diaminourea Dicyclohexyl methyl hydride yield >=97%, 3,3 '-dimethyl -4,4 '-MDA product assay >=30wt%.
CN201610970790.5A 2016-10-28 2016-10-28 A kind of hydrogenation catalyst, preparation method and application Expired - Fee Related CN106622220B (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112110926A (en) * 2020-09-29 2020-12-22 北京阳光诺和药物研究股份有限公司 Method for preparing tebipenem pivoxil
CN113289637A (en) * 2021-06-15 2021-08-24 南京工业大学 Hydrotalcite-like catalyst, preparation method and application thereof
CN113522004A (en) * 2021-08-11 2021-10-22 中建材蚌埠玻璃工业设计研究院有限公司 CIGS tail gas purifying agent and preparation method thereof
CN117358235A (en) * 2023-08-01 2024-01-09 江苏清泉化学股份有限公司 Catalyst for preparing MACM by continuous hydrogenation and preparation method and application thereof

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102030657A (en) * 2010-11-25 2011-04-27 浙江台州清泉医药化工有限公司 Synthesizing method of 3,3'-dimethyl-4,4'-diamido-dicyclohexyl methane
CN102627569A (en) * 2012-03-01 2012-08-08 江苏清泉化学有限公司 Method for synthesizing 3,3'-dimethyl-4,4'-diamino dicyclohexyl methane
CN105921155A (en) * 2016-05-16 2016-09-07 北京化工大学 High-dispersion supported ruthenium dioxide catalyst and preparing method thereof

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102030657A (en) * 2010-11-25 2011-04-27 浙江台州清泉医药化工有限公司 Synthesizing method of 3,3'-dimethyl-4,4'-diamido-dicyclohexyl methane
CN102627569A (en) * 2012-03-01 2012-08-08 江苏清泉化学有限公司 Method for synthesizing 3,3'-dimethyl-4,4'-diamino dicyclohexyl methane
CN105921155A (en) * 2016-05-16 2016-09-07 北京化工大学 High-dispersion supported ruthenium dioxide catalyst and preparing method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112110926A (en) * 2020-09-29 2020-12-22 北京阳光诺和药物研究股份有限公司 Method for preparing tebipenem pivoxil
CN112110926B (en) * 2020-09-29 2022-05-17 北京阳光诺和药物研究股份有限公司 Method for preparing tebipenem pivoxil
CN113289637A (en) * 2021-06-15 2021-08-24 南京工业大学 Hydrotalcite-like catalyst, preparation method and application thereof
CN113522004A (en) * 2021-08-11 2021-10-22 中建材蚌埠玻璃工业设计研究院有限公司 CIGS tail gas purifying agent and preparation method thereof
CN117358235A (en) * 2023-08-01 2024-01-09 江苏清泉化学股份有限公司 Catalyst for preparing MACM by continuous hydrogenation and preparation method and application thereof

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