CA2313874A1 - Metal catalysts - Google Patents
Metal catalysts Download PDFInfo
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- CA2313874A1 CA2313874A1 CA002313874A CA2313874A CA2313874A1 CA 2313874 A1 CA2313874 A1 CA 2313874A1 CA 002313874 A CA002313874 A CA 002313874A CA 2313874 A CA2313874 A CA 2313874A CA 2313874 A1 CA2313874 A1 CA 2313874A1
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- metal catalysts
- metal
- alloy
- catalyst
- catalysts according
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- 239000003054 catalyst Substances 0.000 title claims abstract description 91
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 49
- 239000002184 metal Substances 0.000 title claims abstract description 49
- 238000005984 hydrogenation reaction Methods 0.000 claims abstract description 6
- 150000002894 organic compounds Chemical class 0.000 claims abstract description 6
- 238000006356 dehydrogenation reaction Methods 0.000 claims abstract description 4
- 238000006703 hydration reaction Methods 0.000 claims abstract description 4
- 238000006317 isomerization reaction Methods 0.000 claims abstract description 4
- 239000000956 alloy Substances 0.000 claims description 57
- 229910045601 alloy Inorganic materials 0.000 claims description 57
- 229920006328 Styrofoam Polymers 0.000 claims description 41
- 239000008261 styrofoam Substances 0.000 claims description 41
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 37
- 238000000034 method Methods 0.000 claims description 21
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 17
- 230000008569 process Effects 0.000 claims description 17
- 239000011230 binding agent Substances 0.000 claims description 13
- 239000000843 powder Substances 0.000 claims description 13
- 229910052782 aluminium Inorganic materials 0.000 claims description 9
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 9
- 229910052759 nickel Inorganic materials 0.000 claims description 9
- 239000010949 copper Substances 0.000 claims description 8
- 229910052742 iron Inorganic materials 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 8
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 7
- 230000003197 catalytic effect Effects 0.000 claims description 5
- 229910017052 cobalt Inorganic materials 0.000 claims description 5
- 239000010941 cobalt Substances 0.000 claims description 5
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 5
- 229910052802 copper Inorganic materials 0.000 claims description 5
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 4
- 229910052715 tantalum Inorganic materials 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- 229910052720 vanadium Inorganic materials 0.000 claims description 4
- 229910052725 zinc Inorganic materials 0.000 claims description 4
- 239000011701 zinc Substances 0.000 claims description 4
- 239000004411 aluminium Substances 0.000 claims description 3
- 229910052804 chromium Inorganic materials 0.000 claims description 3
- 229910052750 molybdenum Inorganic materials 0.000 claims description 3
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 claims description 2
- 229910052749 magnesium Inorganic materials 0.000 claims description 2
- 229910052763 palladium Inorganic materials 0.000 claims description 2
- 229910052707 ruthenium Inorganic materials 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 238000005507 spraying Methods 0.000 claims description 2
- 229910001092 metal group alloy Inorganic materials 0.000 abstract description 3
- 238000005932 reductive alkylation reaction Methods 0.000 abstract 1
- 238000006268 reductive amination reaction Methods 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 44
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 39
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 24
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 description 22
- 239000011248 coating agent Substances 0.000 description 19
- 238000000576 coating method Methods 0.000 description 19
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 13
- 239000001257 hydrogen Substances 0.000 description 13
- 229910052739 hydrogen Inorganic materials 0.000 description 13
- 239000010410 layer Substances 0.000 description 13
- 235000011121 sodium hydroxide Nutrition 0.000 description 13
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- 239000004372 Polyvinyl alcohol Substances 0.000 description 12
- 239000007864 aqueous solution Substances 0.000 description 12
- 235000011187 glycerol Nutrition 0.000 description 12
- 235000019422 polyvinyl alcohol Nutrition 0.000 description 12
- 229920002451 polyvinyl alcohol Polymers 0.000 description 12
- 239000000725 suspension Substances 0.000 description 12
- 239000000203 mixture Substances 0.000 description 8
- 239000002245 particle Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 230000004913 activation Effects 0.000 description 6
- 150000002739 metals Chemical class 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- 238000005275 alloying Methods 0.000 description 5
- 238000001354 calcination Methods 0.000 description 5
- 239000011651 chromium Substances 0.000 description 5
- 238000001816 cooling Methods 0.000 description 5
- 238000000605 extraction Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000010953 base metal Substances 0.000 description 3
- 239000010703 silicon Substances 0.000 description 3
- 229910052710 silicon Inorganic materials 0.000 description 3
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000007868 Raney catalyst Substances 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- 230000003213 activating effect Effects 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000012018 catalyst precursor Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000007493 shaping process Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 description 2
- GPPXJZIENCGNKB-UHFFFAOYSA-N vanadium Chemical compound [V]#[V] GPPXJZIENCGNKB-UHFFFAOYSA-N 0.000 description 2
- 229910000531 Co alloy Inorganic materials 0.000 description 1
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- BLJNPOIVYYWHMA-UHFFFAOYSA-N alumane;cobalt Chemical compound [AlH3].[Co] BLJNPOIVYYWHMA-UHFFFAOYSA-N 0.000 description 1
- JRBRVDCKNXZZGH-UHFFFAOYSA-N alumane;copper Chemical compound [AlH3].[Cu] JRBRVDCKNXZZGH-UHFFFAOYSA-N 0.000 description 1
- FJMNNXLGOUYVHO-UHFFFAOYSA-N aluminum zinc Chemical compound [Al].[Zn] FJMNNXLGOUYVHO-UHFFFAOYSA-N 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000003889 chemical engineering Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- JIQVGGQJISZHSS-UHFFFAOYSA-N ethene N-octadecanoyloctadecanamide Chemical compound C=C.CCCCCCCCCCCCCCCCCC(=O)NC(=O)CCCCCCCCCCCCCCCCC JIQVGGQJISZHSS-UHFFFAOYSA-N 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 230000000977 initiatory effect Effects 0.000 description 1
- 239000012633 leachable Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- -1 nickel-chrom-iron-aluminium Chemical compound 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- 230000007420 reactivation Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000011877 solvent mixture Substances 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 1
- 229910052721 tungsten Inorganic materials 0.000 description 1
- 239000010937 tungsten Substances 0.000 description 1
- 230000035899 viability Effects 0.000 description 1
Classifications
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- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
- B01J37/0018—Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat)
-
- 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
- B01J25/00—Catalysts of the Raney type
- B01J25/02—Raney nickel
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/51—Spheres
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/024—Multiple impregnation or coating
- B01J37/0244—Coatings comprising several layers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F1/00—Metallic powder; Treatment of metallic powder, e.g. to facilitate working or to improve properties
- B22F1/06—Metallic powder characterised by the shape of the particles
- B22F1/065—Spherical particles
- B22F1/0655—Hollow particles
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C209/00—Preparation of compounds containing amino groups bound to a carbon skeleton
- C07C209/30—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds
- C07C209/32—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds by reduction of nitro groups
- C07C209/36—Preparation of compounds containing amino groups bound to a carbon skeleton by reduction of nitrogen-to-oxygen or nitrogen-to-nitrogen bonds by reduction of nitro groups by reduction of nitro groups bound to carbon atoms of six-membered aromatic rings in presence of hydrogen-containing gases and a catalyst
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Nanotechnology (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Superconductors And Manufacturing Methods Therefor (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Metal catalysts comprising hallow forms or spheres are made of metal alloy and optionally activated.
The metal catalysts can be used for the hydrogenation, dehydrogenation, isomerisation reductive alkylation, reductive amination, and/or hydration reaction of organic compounds.
The metal catalysts can be used for the hydrogenation, dehydrogenation, isomerisation reductive alkylation, reductive amination, and/or hydration reaction of organic compounds.
Description
Metal Catalysts The present invention relates metal catalysts Activated metal catalysts are known in the field of chemical engineering as Raney catalysts. They are used, largely in powder form, for a large number of hydrogenation, dehydrogenation, isomerization and hydration reactions of organic compounds. These powdered catalysts are prepared from an alloy of a catalytically-active metal, also referred to herein as a catalyst metal, with a further alloying component which is soluble in alkalis. Mainly nickel, cobalt, copper, or iron are used as catalyst metals. Aluminum is generally used as the alloying component which is~soluble in alkalis, but other components may also be used, in particular zinc and silicon or mixtures of these with aluminum.
These so-called Raney alloys are generally prepared by the ingot casting process. In that process a mixture of the catalyst metal and, for example, aluminum are first melted and casted into ingots. Typical alloy batches on a production scale amount to about ten to one hundred kg per ingot. According to DE 21 59 736 cooling times~of up to two hours were obtained. This corresponds to an average _rate of cooling of about 0. 2 /s. In contrast to this, rates of 102 to 106 K/s are achieved in processes where rapid cooling is applied (for example an atomizing process). The rate of cooling is affected in particular by the particle size and the cooling medium (see Materials Science and Technology edited by R. W. Chan, P. Haasen, E. J. Kramer, Vol. 15, Processing of Metals and Alloys, 1991, VCH-Verlag Weinheim, pages 57 to 110). A process of this type is used in EP 0 437 788 B 1 in order to prepare a Raney alloy powder. In that process the molten alloy at a temperature of 50 to 500°C above its melting point is atomized and cooled using water and/or a gas.
These so-called Raney alloys are generally prepared by the ingot casting process. In that process a mixture of the catalyst metal and, for example, aluminum are first melted and casted into ingots. Typical alloy batches on a production scale amount to about ten to one hundred kg per ingot. According to DE 21 59 736 cooling times~of up to two hours were obtained. This corresponds to an average _rate of cooling of about 0. 2 /s. In contrast to this, rates of 102 to 106 K/s are achieved in processes where rapid cooling is applied (for example an atomizing process). The rate of cooling is affected in particular by the particle size and the cooling medium (see Materials Science and Technology edited by R. W. Chan, P. Haasen, E. J. Kramer, Vol. 15, Processing of Metals and Alloys, 1991, VCH-Verlag Weinheim, pages 57 to 110). A process of this type is used in EP 0 437 788 B 1 in order to prepare a Raney alloy powder. In that process the molten alloy at a temperature of 50 to 500°C above its melting point is atomized and cooled using water and/or a gas.
To prepare a catalyst, the Raney alloy is first finely milled if it has not been produced in the desired powder form during preparation. Then the aluminum is entirely or partly removed by extraction with alkalis such as, for example, caustic soda solution. This activates the alloy powder. Following extraction of the aluminum the alloy power has a high specific surface area (BET), between 20 and 100 m2/g, and is rich in active hydrogen. The activated catalyst powder is pyrophoric and stored under water or organic solvents or is embedded in organic compounds which are solid at room temperature.
Powdered catalysts have the disadvantage that they can be used only in a batch process and, after the catalytic reaction, have to be separated from the reaction medium by costly sedimentation and/or filtration. Therefore a variety of processes for preparing moulded items which lead to activated metal fixed-bed catalysts after extraction of the aluminum have been disclosed. Thus, for example, coarse particulate Raney alloys, i.e., Raney alloys which have only been coarsely milled, are obtainable and these can be activated by a treatment with caustic soda solution.
Extraction and activation then occurs only in a surface layer the thickness of which can be adjusted by the conditions used during extraction.
A substantial disadvantage of catalysts prepared by these prior methods are the poor mechanical stability of the activated outer layer. Since only this outer layer of the catalysts the catalytically active, abrasion leads to rapid deactivation and renewed activation of deeper lying layers of alloy using caustic soda solution then leads at best to partial reactivation.
Patent application EP 0 648 534 B1 describes shaped, activated Raney metal fixed-bed catalysts and their preparation. These catalysts avoid the disadvantages described above, e.g., the poor mechanical stability resulting from activating an outer layer. To prepare these catalysts, a mixture of powers of a catalyst alloy and a binder are used, where in the catalyst alloys each contain at least one catalytically active catalyst metal and an extractable alloying component. The pure catalyst metals or mixtures thereof which do not contain extractable components are used as binder. The use of the binder in an amount of 0. 5 to 20 weight percent with respect to the catalyst alloy, is essential in order to achieve sufficient mechanical stability after activation. After shaping the catalyst alloy and the binder with conventional shaping aids and pore producers, the freshly prepared items which are obtained are calcined at temperatures below 850°C. As a result of sintering processes in the finely divided binder, this produces solid compounds between the individual granules of the catalysts alloy. These compounds, in contrast to catalyst alloys, are non-extractable or only extractable to a small extent so that a mechanical stable structure is obtained even after activation. However, the added binder has the disadvantage that it is substantially catalytically inactive and thus the number of active centers in the activated layer is reduced. In addition, the absolutely essential use of a binder means that only restricted range of amounts of pore producers can be used without endangering the stregnth of the shaped item:'- For this reason, the bulk density of these catalysts cannot be reduced to a value of less than 1. 9 kg per liter without incurring loss of strength. This leads to a considerable economic disadvantage when using these catalysts in industrial processes. In particular when using more expensive catalysts alloys, for example cobalt alloys, the high bulk density leads to a high investment per reactor bed, which is, however partly compensated for by the high activity and long-term stability of these catalyst. In certain cases, the high bulk density of the catalyst also requires a mechanically reinforced reactor structure.
Powdered catalysts have the disadvantage that they can be used only in a batch process and, after the catalytic reaction, have to be separated from the reaction medium by costly sedimentation and/or filtration. Therefore a variety of processes for preparing moulded items which lead to activated metal fixed-bed catalysts after extraction of the aluminum have been disclosed. Thus, for example, coarse particulate Raney alloys, i.e., Raney alloys which have only been coarsely milled, are obtainable and these can be activated by a treatment with caustic soda solution.
Extraction and activation then occurs only in a surface layer the thickness of which can be adjusted by the conditions used during extraction.
A substantial disadvantage of catalysts prepared by these prior methods are the poor mechanical stability of the activated outer layer. Since only this outer layer of the catalysts the catalytically active, abrasion leads to rapid deactivation and renewed activation of deeper lying layers of alloy using caustic soda solution then leads at best to partial reactivation.
Patent application EP 0 648 534 B1 describes shaped, activated Raney metal fixed-bed catalysts and their preparation. These catalysts avoid the disadvantages described above, e.g., the poor mechanical stability resulting from activating an outer layer. To prepare these catalysts, a mixture of powers of a catalyst alloy and a binder are used, where in the catalyst alloys each contain at least one catalytically active catalyst metal and an extractable alloying component. The pure catalyst metals or mixtures thereof which do not contain extractable components are used as binder. The use of the binder in an amount of 0. 5 to 20 weight percent with respect to the catalyst alloy, is essential in order to achieve sufficient mechanical stability after activation. After shaping the catalyst alloy and the binder with conventional shaping aids and pore producers, the freshly prepared items which are obtained are calcined at temperatures below 850°C. As a result of sintering processes in the finely divided binder, this produces solid compounds between the individual granules of the catalysts alloy. These compounds, in contrast to catalyst alloys, are non-extractable or only extractable to a small extent so that a mechanical stable structure is obtained even after activation. However, the added binder has the disadvantage that it is substantially catalytically inactive and thus the number of active centers in the activated layer is reduced. In addition, the absolutely essential use of a binder means that only restricted range of amounts of pore producers can be used without endangering the stregnth of the shaped item:'- For this reason, the bulk density of these catalysts cannot be reduced to a value of less than 1. 9 kg per liter without incurring loss of strength. This leads to a considerable economic disadvantage when using these catalysts in industrial processes. In particular when using more expensive catalysts alloys, for example cobalt alloys, the high bulk density leads to a high investment per reactor bed, which is, however partly compensated for by the high activity and long-term stability of these catalyst. In certain cases, the high bulk density of the catalyst also requires a mechanically reinforced reactor structure.
An object of the present invention is therefore to provide activated base metal catalysts from hallow metallic forms which largely avoids the disadvantages of the above known fixed-bed catalysts.
The above and other objects of the invention are achieved by producing hallow forms out of the desired alloys and activating it in order to make the catalyst. The major advantages of this invention are its low bulk density and its high activity these materials exhibit per gram of metal.
One object of the invention is metal catalysts comprising hallow forms. Preferably the hallow forms are hallow spheres. These spheres can show a diameter of 0,5 to 20 mm and a wall thickness of 0,1 to 5 mm. The shell of the spheres can be unpermeable or it can show an open porosity up to 80 ~. The shell of the spheres can consist of different layers and/or the metal can be graduated.
The metal catalysts comprising hallow forms can be activated.
Another object of the invention is a process for the for the production of the metal catalysts comprising spraying of metal powders, obtionally together with a binder on to forms consisting of a burnable material i.e. styrofoam, burning out the materal to receive the hallow form.
In another object of the invention in the process for the production of the metal catalysts where one of the metal powders consists of a rapidly cooled alloy. The rapidly cooled alloy can be made according to commonly used methods such spray drying in vanous atmospheres as rapidly cooling in liquids such as water. The hallow form consisting of the alloy and optionally a binder can then be activated with an alkali solutions such as agueous NaOH, to form the activated catalyst.
One of the metal powders can consist of a slowly cooled alloy. The hallow form consisting of the aloy and optionally a binder can then be activated with an alkalisolution, such as an aqueous NaOH solution , to form 5 the activated catalyst.
In the process for the production of the metal catalysts the alloy can consist of one or more catalytic metal such as nickel, iron, copper, palladium, ruthenium, and cobalt;
an alkali soluble component such as aluminium, zinc, and silica: and optionally one or more promoter elements such as Cr, Fe, Ti, V, Ta, Mo, Mg, Co, and/or W.
The hallow spheres according to this invention can be prepared according to Andersen, Schneider, and Stephani (See, "Neue Hochporbse Metallische Werkstoffe", Ingenieur-Werkstoffe, 4, 1998, pages 36-38). In this method, a mixture of the desired alloy, an organic binder, and optionally an inorganic binder were sprayed uniformly through a fluidized bed of Styrofoam balls where it coats the Styrofoam. The coated balls are then calciried at optionally temperatures ranging from 450 to 1000°C to burn out the Styrofoam followed by a higher calcination temperature to sinter the metal together in order to make the hallow form more stable. After calcination, the catalyst is then activated by a caustic soda solution to produce the activated base metal catalyst. An added benefit to this catalyst system is that one can easy control the thickness of the hollow form's walls from the coating conditions and the porosity of this wall by the particle size and composition of the original powdermixture.
The bulk density of the resulting fixed bed catalyst is very important for highly active catalysts. While the known standard fixed bed activated base metal catalysts have bulk densities ranging from 2.4 to 1.8 kg/1, bulk densities similar to other fixed bed applications such as 0.3 to 1.0 kg/1 are highly desirable to keep the cost to fill a commercial reactor at a minimum.
The ratio by weight of catalyst metal to extractable alloying component in the catalyst alloy is, as is conventional with Raney alloys, in the range from 20:80 to 80:20. Catalysts according to the invention may also be doped with other metals in order to have an effective on the catalytic properties. The purpose of this type of doping, is for example, to improve the selectivity in a specific reaction. Doping metals are frequently also called promoters. The doping or promoting of Raney catalyst is described for example in U.S. patent 4,153, 578 and DE-AS 21 O1 856 in DE-OS 21 00 373 and in the DE-AS 2053799.
In principle, any known metal alloys such as nickel-aluminium, cobalt-aluminium, copper-aluminium, nickel-chrom-iron-aluminium can be used. This means any Raney-type alloys that involved the combination of leachable materals such as zinc, silicon and/or aluminium in combination with catalytic materials such as nickel, cobalt, copper, and/or iron can be used.
The alloys can contain doping materials like chrom, iron, titanium, vanadium, tantalum with extractable elements such as aluminum zinc and silicon maybe used for the present invention. Suitable promoters are transition elements in groups of 3B to 7B and 8 and group 1B of the Periodic Table of Elements and also the rare-earth metals. They are also used in an amount of up to 20 wt$, with respect of the total weight of catalyst. Chromium, manganese, iron, cobalt, vanadium, tantalum, titanium, tungsten, and/or molybdenum and metals from platinum group are preferably used as promoters. They are expediently added as alloying constituents in the catalyst alloy. In addition, promoters with a different extractable metal alloy, in the form of a separable metal powder, may be used, or the promoters may be applied later to the catalyst's material. Later application of promoters may be performed either after calcination or after activation. Optimum adjustment of the catalyst properties to the particular catalyst process is thus possible.
The Raney type catalyst precursors resulting from calcination are also very important with regard the economic viability of invention. They are not pyrophoric and can be handled and transported without difficulty.
Activation can be performed by the user shortly before use.
Storage under water or organic solvents or embedding in organic compounds is not required for the catalyst precursors.
The metal catalysts of the invention can be used for the hydrogenation, dehydrogenation, isomerisation and/or hydration reaction of organic compounds.
Comparison Example 1 A free-flowing, pelletable catalyst mixture was prepared in accordance with the instructions in EP 0 648 534 A1 for a comparison catalyst consisting of 1000 g of 53$Ni and 47~A1 alloy powder, 150 g of pure nickel powder(99$Ni, and d50 =
21 um), and 25 g of ethylene bis-stearoylamide whilst adding about 150 g of water. Tablets with the diameter of 4 mm and a thickness of 4 mm were compressed from this mixture. The shaped items were calcined for 2 h at 700°C.
The tablets were activated in 20~ strength caustic soda solution for 2 hours at 80°C after calcination. Under the conditions of application example, this catalyst started to hydrogenate nitrobenzene at 120°C and the activity was 1,36 ml of consummed hydrogen per gram of catalyst per minute.
Example 1 A coating solution was prepared by suspending 600 grams of a rapidly cooled SOgNi/50~A1 alloy in a 800 ml aqueous solution containing 5 wt~ polyvinylalcohol and 1.25 wt~
The above and other objects of the invention are achieved by producing hallow forms out of the desired alloys and activating it in order to make the catalyst. The major advantages of this invention are its low bulk density and its high activity these materials exhibit per gram of metal.
One object of the invention is metal catalysts comprising hallow forms. Preferably the hallow forms are hallow spheres. These spheres can show a diameter of 0,5 to 20 mm and a wall thickness of 0,1 to 5 mm. The shell of the spheres can be unpermeable or it can show an open porosity up to 80 ~. The shell of the spheres can consist of different layers and/or the metal can be graduated.
The metal catalysts comprising hallow forms can be activated.
Another object of the invention is a process for the for the production of the metal catalysts comprising spraying of metal powders, obtionally together with a binder on to forms consisting of a burnable material i.e. styrofoam, burning out the materal to receive the hallow form.
In another object of the invention in the process for the production of the metal catalysts where one of the metal powders consists of a rapidly cooled alloy. The rapidly cooled alloy can be made according to commonly used methods such spray drying in vanous atmospheres as rapidly cooling in liquids such as water. The hallow form consisting of the alloy and optionally a binder can then be activated with an alkali solutions such as agueous NaOH, to form the activated catalyst.
One of the metal powders can consist of a slowly cooled alloy. The hallow form consisting of the aloy and optionally a binder can then be activated with an alkalisolution, such as an aqueous NaOH solution , to form 5 the activated catalyst.
In the process for the production of the metal catalysts the alloy can consist of one or more catalytic metal such as nickel, iron, copper, palladium, ruthenium, and cobalt;
an alkali soluble component such as aluminium, zinc, and silica: and optionally one or more promoter elements such as Cr, Fe, Ti, V, Ta, Mo, Mg, Co, and/or W.
The hallow spheres according to this invention can be prepared according to Andersen, Schneider, and Stephani (See, "Neue Hochporbse Metallische Werkstoffe", Ingenieur-Werkstoffe, 4, 1998, pages 36-38). In this method, a mixture of the desired alloy, an organic binder, and optionally an inorganic binder were sprayed uniformly through a fluidized bed of Styrofoam balls where it coats the Styrofoam. The coated balls are then calciried at optionally temperatures ranging from 450 to 1000°C to burn out the Styrofoam followed by a higher calcination temperature to sinter the metal together in order to make the hallow form more stable. After calcination, the catalyst is then activated by a caustic soda solution to produce the activated base metal catalyst. An added benefit to this catalyst system is that one can easy control the thickness of the hollow form's walls from the coating conditions and the porosity of this wall by the particle size and composition of the original powdermixture.
The bulk density of the resulting fixed bed catalyst is very important for highly active catalysts. While the known standard fixed bed activated base metal catalysts have bulk densities ranging from 2.4 to 1.8 kg/1, bulk densities similar to other fixed bed applications such as 0.3 to 1.0 kg/1 are highly desirable to keep the cost to fill a commercial reactor at a minimum.
The ratio by weight of catalyst metal to extractable alloying component in the catalyst alloy is, as is conventional with Raney alloys, in the range from 20:80 to 80:20. Catalysts according to the invention may also be doped with other metals in order to have an effective on the catalytic properties. The purpose of this type of doping, is for example, to improve the selectivity in a specific reaction. Doping metals are frequently also called promoters. The doping or promoting of Raney catalyst is described for example in U.S. patent 4,153, 578 and DE-AS 21 O1 856 in DE-OS 21 00 373 and in the DE-AS 2053799.
In principle, any known metal alloys such as nickel-aluminium, cobalt-aluminium, copper-aluminium, nickel-chrom-iron-aluminium can be used. This means any Raney-type alloys that involved the combination of leachable materals such as zinc, silicon and/or aluminium in combination with catalytic materials such as nickel, cobalt, copper, and/or iron can be used.
The alloys can contain doping materials like chrom, iron, titanium, vanadium, tantalum with extractable elements such as aluminum zinc and silicon maybe used for the present invention. Suitable promoters are transition elements in groups of 3B to 7B and 8 and group 1B of the Periodic Table of Elements and also the rare-earth metals. They are also used in an amount of up to 20 wt$, with respect of the total weight of catalyst. Chromium, manganese, iron, cobalt, vanadium, tantalum, titanium, tungsten, and/or molybdenum and metals from platinum group are preferably used as promoters. They are expediently added as alloying constituents in the catalyst alloy. In addition, promoters with a different extractable metal alloy, in the form of a separable metal powder, may be used, or the promoters may be applied later to the catalyst's material. Later application of promoters may be performed either after calcination or after activation. Optimum adjustment of the catalyst properties to the particular catalyst process is thus possible.
The Raney type catalyst precursors resulting from calcination are also very important with regard the economic viability of invention. They are not pyrophoric and can be handled and transported without difficulty.
Activation can be performed by the user shortly before use.
Storage under water or organic solvents or embedding in organic compounds is not required for the catalyst precursors.
The metal catalysts of the invention can be used for the hydrogenation, dehydrogenation, isomerisation and/or hydration reaction of organic compounds.
Comparison Example 1 A free-flowing, pelletable catalyst mixture was prepared in accordance with the instructions in EP 0 648 534 A1 for a comparison catalyst consisting of 1000 g of 53$Ni and 47~A1 alloy powder, 150 g of pure nickel powder(99$Ni, and d50 =
21 um), and 25 g of ethylene bis-stearoylamide whilst adding about 150 g of water. Tablets with the diameter of 4 mm and a thickness of 4 mm were compressed from this mixture. The shaped items were calcined for 2 h at 700°C.
The tablets were activated in 20~ strength caustic soda solution for 2 hours at 80°C after calcination. Under the conditions of application example, this catalyst started to hydrogenate nitrobenzene at 120°C and the activity was 1,36 ml of consummed hydrogen per gram of catalyst per minute.
Example 1 A coating solution was prepared by suspending 600 grams of a rapidly cooled SOgNi/50~A1 alloy in a 800 ml aqueous solution containing 5 wt~ polyvinylalcohol and 1.25 wt~
glycerin. This suspension was then sprayed onto 1500 ml of Styrofoam balls ranging from 4 to 5 mm while they were suspended in an upward air steam. After coating the styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). These dried coated styrofoam spheres had a bulk density of 0.45 g/ml and half of these spheres were further coated with an alloy solution so as to demonstrate the flexibility of this process. The solution for the second layer consisted of 700 grams of a rapidly cooled 50$Ni/50$A1 alloy that was suspended in a 800 ml aqueous solution containing 5 wt~ polyvinylalcohol and 1.25 wt~
glycerin. This suspension was then sprayed onto 750 ml of the Ni/A1 precoated and dried Styrofoam balls mentioned above while they were suspended in an upward air steam.
After coating the styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). Although the solution for the second layer was similar to the first, this technique clearly demonstrates the ability of this process to make layered hallow spheres.
The dried coated spheres were then heated in a controlled nitrogen/air stream at 830°C for 1 hour to burn out the Styrofoam and to sinter together the alloy particles, The hallow spheres were then activated in a 20 wt~ NaOH
solution for 1.5 hours at 80°C. The resulting activated hallow spheres had diameters ranging from 5 to 6 mm, a shell thickness range of 700-1000u, a crush strength of 90 N, and the bulk density of 0.62 g/ml. Under the conditions of application example 1, this catalyst started to hydrogenate nitrobenzene at 110-120°C and the catalyst's nitrobenzene activity was 1.54 ml of consummed hydrogen per gram of catalyst per minute.
Example 2 A coating solution was prepared by suspending 500 grams of a rapidly cooled 50%Ni/50%A1 alloy and 37.5 grams of nickel powder in a 750 ml aqueous solution containing 5 wt%
polyvinylalcohol and 1.25 wt% glycerin. This suspension was then sprayed onto 1000 ml of styrofoam balls ranging from 4 to 5 mm while they were suspended in an upward air steam.
After coating the Styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). The dried coated spheres were then heated in a controlled nitrogen/air stream at 840°C for 1 hour to burn out the styrofoam and to sinter together the nickel and alloy particles. The hallow spheres were then activated in a 20 wt% NaOH solution for 1.5 hours at 80°C. The resulting activated hallow spheres had diameters ranging from 5 to 6 mm, an average shell thickness of 500 p, and the bulk density of 0.34 g/ml. Under the conditions of application example 1, this catalyst started to hydrogenate nitrobenzene at 110-120°C and the catalyst's nitrobenzene activity was 1.82 ml of consummed hydrogen per gram of catalyst per minute.
Example 3 A coating solution was prepared by suspending 800 grams of a 50%Co/50%A1 alloy in a 1000 ml aqueous solution '-containing 5 wt% polyvinylalcohol and 1.25 wt% glycerin.
This suspension was then sprayed onto 2000 ml of Styrofoam balls ranging from 4 to 5 mm while they were suspended in an upward air steam. After coating the Styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). These dried coated Styrofoam spheres had a bulk density of 0.35 g/ml and half of these spheres were further coated with an alloy solution. The solution for the second layer consisted of 800 grams of a 50%Co/50%A1 alloy that was suspended in a 1000 ml aqueous solution containing 5 wt% polyvinylalcohol and 1.25 wt~ glycerin. This suspension was then sprayed onto 1000 ml of the Co/A1 precoated and dried styrofoam balls mentioned above while they were suspended in an upward air steam. After coating the Styrofoam balls with 5 the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). The dried coated spheres were then heated in a controlled nitrogen/air stream at 700°C to burn out the styrofoam and to sinter together the 10 alloy particles. The hallow spheres were then activated in a 20 wt~ NaOH solution for 1.5 hours at 80°C. The resulting activated hallow spheres had diameters ranging from 5 to 6 mm, a shell thickness of 700 u, a crush strength of 71 N, and the bulk density of 0.50 g/ml. As could be visually seen from the evolution of hydrogen bubbles, the catalyst had a large reservoir of active hydrogen.
Example 4 A coating solution was prepared by suspending 800 grams of a 50~Cu/50$A1 alloy and 104 grams of copper powder in a 1000 ml aqueous solution containing 5 wt$ polyvinylalcohol and 1.25 wt~ glycerin. This suspension was then sprayed onto 2000 ml of styrofoam balls ranging from 4 to 5 mm while they were suspended in an upward air steam. After coating the Styrofoam balls with the above mentioned~
solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). These dried coated styrofoam spheres had a bulk density of 0.26 g/ml and half of these spheres were further coated with an alloy solution. The solution for the second layer consisted of 800 grams of a 50$Cu/50~A1 alloy and 104 grams of copper powder that were suspended in a 1000 ml aqueous solution containing 5 wt~ polyvinylalcohol and 1.25 wt$ glycerin. This suspension was then sprayed onto 1000 ml of the Cu/A1 precoated and dried Styrofoam balls mentioned above while they were suspended in an upward air steam. After coating the styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). The dried coated spheres were then heated in a controlled nitrogen/air stream at 550°C to burn out the styrofoam and to sinter together the copper and alloy particles. The hallow spheres were then activated in a 20 wto NaOH solution for 1.5 hours at 80°C. The resulting activated hallow spheres had an average diameter 6 mm, a shell thickness ranging from 600 to 700 u, and the bulk density of 0.60 g/ml. As could be visually seen from the evolution of hydrogen bubbles, the catalyst had a large reservoir of active hydrogen.
Example 5 A coating solution was prepared by suspending 800 grams of a slowly cooled 50$Ni / 0.5$Fe / 1.2$Cr / 48.3~A1 alloy and 60 grams of nickel powder in a 1000 ml aqueous solution containing 5 wt$ polyvinylalcohol and 1.25 wt~ glycerin.
This suspension was then sprayed onto 2000 ml of ~styrofoam balls ranging from 4 to 5 mm while they were suspended in an upward air steam. After coating the Styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). These dried coated Styrofoam spheres had a bulk density of 0.30 g/ml and half of these spheres were further coated with an alloy solution. The solution for the second layer consisted of 800 grams of a slowly cooled 50$Ni / 0.5$Fe / 1.2$Cr /
48.3~A1 alloy and 60 grams of nickel powder that were suspended in a 1000 ml aqueous solution containing 5 wt$
polyvinylalcohol and 1.25 wt$ glycerin. This suspension was then sprayed onto 1000 ml of the Ni/Fe/Cr/Al precoated and dried Styrofoam balls mentioned above while they were suspended in an upward air steam. After coating the styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). The dried coated spheres were then heated in a controlled nitrogen/air stream at 700°C to burn out the Styrofoam and to sinter together the nickel and alloy particles. The hallow spheres were then activated in a 20 wt~ NaOH solution for 1.5 hours at 80°C. The resulting activated hallow spheres had an average diameter 5.9 mm, a shell thickness of 700 u, the crush strength of 85 N, and the bulk density of 0.55 g/ml. Under the conditions of application example 1, this catalyst started to hydrogenate nitrobenzene at 110°C and the catalyst's nitrobenzene activity was 2.40 ml of consummed hydrogen per gram of catalyst per minute.
Example 6 A coating solution was prepared by suspending 1000 grams of a rapidly cooled 50%Ni/50$A1 alloy and 75 grams of nickel powder in a 1000 ml aqueous solution containing 5 wt$
polyvinylalcohol and 1.25 wt$ glycerin. This suspension was then sprayed onto 2000 ml of Styrofoam balls ranging from 2 to 3 mm while they were suspended in an upward air steam.
After coating the Styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). These dried coated styrofoam spheres had a bulk density of 0.33 g/ml and half of these spheres were further coated with an alloy solution. The solution for the second layer consisted of 1000 grams of a rapidly cooled 50~Ni/50gA1 alloy and 75 grams of nickel powder that were suspended in a 1000 ml aqueous solution containing 5 wt$
polyvinylalcohol and 1.25 wt~ glycerin. This suspension was then sprayed onto 1000 ml of the Ni/A1 precoated and dried styrofoam balls mentioned above while they were suspended in an upward air steam. After coating the styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C
(higher temperatures can also be used). These dried double coated Styrofoam spheres had a bulk density of 0.75 g/ml and half of these spheres were once again coated further with a third addition of the alloy solution. The solution for the third layer consisted of 1000 grams of a rapidly cooled 50$Ni/50~A1 alloy and 75 grams of nickel powder that were suspended in a 1000 ml aqueous solution containing 5 wt~ polyvinylalcohol and 1.25 wt~ glycerin. This suspension was then sprayed onto 500 ml of the Ni/Al double-precoated and dried styrofoam balls mentioned above while they were suspended in an upward air steam. After coating the Styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). The dried triple-coated spheres were then heated in a controlled nitrogen/air stream at 700°C to burn out the styrofoam and to sinter together the nickel and alloy particles. The hallow spheres were then activated in a 20 wt$ NaOH solution for 1.5 hours at 80°C. The resulting activated hallow spheres had an average diameter 4.5 mm, a shell thickness of 600 to 700 u, and the bulk density of 0.85 g/ml. Under the conditions of application example 1, this catalyst started to hydrogenate nitrobenzene at 78°C
and the catalyst's nitrobenzene activity was 3.46 ml of consummed hydrogen per gram of catalyst per minute.
Application example 1 The catalytic activity of the catalyst from comparison examples 1 and 2 and from examples 1 to 5 were compared during the hydrogenation of nitrobenzene. For this purpose, 100 g of nitrobenzene and 100 g of ethanol were placed in a stirred autoclave with a capacity of 0.5 1, fitted with a gas stirrer. 10 g of the catalyst being investigated were suspended each time in the stirred autoclave using a catalyst basket so that the catalyst material was thoroughly washed by the reactant/solvent mixture, and hydrogen was introduced. Hydrogenation was performed at a hydrogen pressure of 40 bar and a temperature of 150°C. The initiation temperature and the rate of hydrogen consumption were determined. The results are given in table 1. As a check, samples were withdrawn after 1, 2, 3, 4, and 5 h and analyzed using gas chromatography.
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glycerin. This suspension was then sprayed onto 750 ml of the Ni/A1 precoated and dried Styrofoam balls mentioned above while they were suspended in an upward air steam.
After coating the styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). Although the solution for the second layer was similar to the first, this technique clearly demonstrates the ability of this process to make layered hallow spheres.
The dried coated spheres were then heated in a controlled nitrogen/air stream at 830°C for 1 hour to burn out the Styrofoam and to sinter together the alloy particles, The hallow spheres were then activated in a 20 wt~ NaOH
solution for 1.5 hours at 80°C. The resulting activated hallow spheres had diameters ranging from 5 to 6 mm, a shell thickness range of 700-1000u, a crush strength of 90 N, and the bulk density of 0.62 g/ml. Under the conditions of application example 1, this catalyst started to hydrogenate nitrobenzene at 110-120°C and the catalyst's nitrobenzene activity was 1.54 ml of consummed hydrogen per gram of catalyst per minute.
Example 2 A coating solution was prepared by suspending 500 grams of a rapidly cooled 50%Ni/50%A1 alloy and 37.5 grams of nickel powder in a 750 ml aqueous solution containing 5 wt%
polyvinylalcohol and 1.25 wt% glycerin. This suspension was then sprayed onto 1000 ml of styrofoam balls ranging from 4 to 5 mm while they were suspended in an upward air steam.
After coating the Styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). The dried coated spheres were then heated in a controlled nitrogen/air stream at 840°C for 1 hour to burn out the styrofoam and to sinter together the nickel and alloy particles. The hallow spheres were then activated in a 20 wt% NaOH solution for 1.5 hours at 80°C. The resulting activated hallow spheres had diameters ranging from 5 to 6 mm, an average shell thickness of 500 p, and the bulk density of 0.34 g/ml. Under the conditions of application example 1, this catalyst started to hydrogenate nitrobenzene at 110-120°C and the catalyst's nitrobenzene activity was 1.82 ml of consummed hydrogen per gram of catalyst per minute.
Example 3 A coating solution was prepared by suspending 800 grams of a 50%Co/50%A1 alloy in a 1000 ml aqueous solution '-containing 5 wt% polyvinylalcohol and 1.25 wt% glycerin.
This suspension was then sprayed onto 2000 ml of Styrofoam balls ranging from 4 to 5 mm while they were suspended in an upward air steam. After coating the Styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). These dried coated Styrofoam spheres had a bulk density of 0.35 g/ml and half of these spheres were further coated with an alloy solution. The solution for the second layer consisted of 800 grams of a 50%Co/50%A1 alloy that was suspended in a 1000 ml aqueous solution containing 5 wt% polyvinylalcohol and 1.25 wt~ glycerin. This suspension was then sprayed onto 1000 ml of the Co/A1 precoated and dried styrofoam balls mentioned above while they were suspended in an upward air steam. After coating the Styrofoam balls with 5 the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). The dried coated spheres were then heated in a controlled nitrogen/air stream at 700°C to burn out the styrofoam and to sinter together the 10 alloy particles. The hallow spheres were then activated in a 20 wt~ NaOH solution for 1.5 hours at 80°C. The resulting activated hallow spheres had diameters ranging from 5 to 6 mm, a shell thickness of 700 u, a crush strength of 71 N, and the bulk density of 0.50 g/ml. As could be visually seen from the evolution of hydrogen bubbles, the catalyst had a large reservoir of active hydrogen.
Example 4 A coating solution was prepared by suspending 800 grams of a 50~Cu/50$A1 alloy and 104 grams of copper powder in a 1000 ml aqueous solution containing 5 wt$ polyvinylalcohol and 1.25 wt~ glycerin. This suspension was then sprayed onto 2000 ml of styrofoam balls ranging from 4 to 5 mm while they were suspended in an upward air steam. After coating the Styrofoam balls with the above mentioned~
solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). These dried coated styrofoam spheres had a bulk density of 0.26 g/ml and half of these spheres were further coated with an alloy solution. The solution for the second layer consisted of 800 grams of a 50$Cu/50~A1 alloy and 104 grams of copper powder that were suspended in a 1000 ml aqueous solution containing 5 wt~ polyvinylalcohol and 1.25 wt$ glycerin. This suspension was then sprayed onto 1000 ml of the Cu/A1 precoated and dried Styrofoam balls mentioned above while they were suspended in an upward air steam. After coating the styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). The dried coated spheres were then heated in a controlled nitrogen/air stream at 550°C to burn out the styrofoam and to sinter together the copper and alloy particles. The hallow spheres were then activated in a 20 wto NaOH solution for 1.5 hours at 80°C. The resulting activated hallow spheres had an average diameter 6 mm, a shell thickness ranging from 600 to 700 u, and the bulk density of 0.60 g/ml. As could be visually seen from the evolution of hydrogen bubbles, the catalyst had a large reservoir of active hydrogen.
Example 5 A coating solution was prepared by suspending 800 grams of a slowly cooled 50$Ni / 0.5$Fe / 1.2$Cr / 48.3~A1 alloy and 60 grams of nickel powder in a 1000 ml aqueous solution containing 5 wt$ polyvinylalcohol and 1.25 wt~ glycerin.
This suspension was then sprayed onto 2000 ml of ~styrofoam balls ranging from 4 to 5 mm while they were suspended in an upward air steam. After coating the Styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). These dried coated Styrofoam spheres had a bulk density of 0.30 g/ml and half of these spheres were further coated with an alloy solution. The solution for the second layer consisted of 800 grams of a slowly cooled 50$Ni / 0.5$Fe / 1.2$Cr /
48.3~A1 alloy and 60 grams of nickel powder that were suspended in a 1000 ml aqueous solution containing 5 wt$
polyvinylalcohol and 1.25 wt$ glycerin. This suspension was then sprayed onto 1000 ml of the Ni/Fe/Cr/Al precoated and dried Styrofoam balls mentioned above while they were suspended in an upward air steam. After coating the styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). The dried coated spheres were then heated in a controlled nitrogen/air stream at 700°C to burn out the Styrofoam and to sinter together the nickel and alloy particles. The hallow spheres were then activated in a 20 wt~ NaOH solution for 1.5 hours at 80°C. The resulting activated hallow spheres had an average diameter 5.9 mm, a shell thickness of 700 u, the crush strength of 85 N, and the bulk density of 0.55 g/ml. Under the conditions of application example 1, this catalyst started to hydrogenate nitrobenzene at 110°C and the catalyst's nitrobenzene activity was 2.40 ml of consummed hydrogen per gram of catalyst per minute.
Example 6 A coating solution was prepared by suspending 1000 grams of a rapidly cooled 50%Ni/50$A1 alloy and 75 grams of nickel powder in a 1000 ml aqueous solution containing 5 wt$
polyvinylalcohol and 1.25 wt$ glycerin. This suspension was then sprayed onto 2000 ml of Styrofoam balls ranging from 2 to 3 mm while they were suspended in an upward air steam.
After coating the Styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). These dried coated styrofoam spheres had a bulk density of 0.33 g/ml and half of these spheres were further coated with an alloy solution. The solution for the second layer consisted of 1000 grams of a rapidly cooled 50~Ni/50gA1 alloy and 75 grams of nickel powder that were suspended in a 1000 ml aqueous solution containing 5 wt$
polyvinylalcohol and 1.25 wt~ glycerin. This suspension was then sprayed onto 1000 ml of the Ni/A1 precoated and dried styrofoam balls mentioned above while they were suspended in an upward air steam. After coating the styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C
(higher temperatures can also be used). These dried double coated Styrofoam spheres had a bulk density of 0.75 g/ml and half of these spheres were once again coated further with a third addition of the alloy solution. The solution for the third layer consisted of 1000 grams of a rapidly cooled 50$Ni/50~A1 alloy and 75 grams of nickel powder that were suspended in a 1000 ml aqueous solution containing 5 wt~ polyvinylalcohol and 1.25 wt~ glycerin. This suspension was then sprayed onto 500 ml of the Ni/Al double-precoated and dried styrofoam balls mentioned above while they were suspended in an upward air steam. After coating the Styrofoam balls with the above mentioned solution, the balls were then dried in upwardly flowing air at temperatures upto 80°C (higher temperatures can also be used). The dried triple-coated spheres were then heated in a controlled nitrogen/air stream at 700°C to burn out the styrofoam and to sinter together the nickel and alloy particles. The hallow spheres were then activated in a 20 wt$ NaOH solution for 1.5 hours at 80°C. The resulting activated hallow spheres had an average diameter 4.5 mm, a shell thickness of 600 to 700 u, and the bulk density of 0.85 g/ml. Under the conditions of application example 1, this catalyst started to hydrogenate nitrobenzene at 78°C
and the catalyst's nitrobenzene activity was 3.46 ml of consummed hydrogen per gram of catalyst per minute.
Application example 1 The catalytic activity of the catalyst from comparison examples 1 and 2 and from examples 1 to 5 were compared during the hydrogenation of nitrobenzene. For this purpose, 100 g of nitrobenzene and 100 g of ethanol were placed in a stirred autoclave with a capacity of 0.5 1, fitted with a gas stirrer. 10 g of the catalyst being investigated were suspended each time in the stirred autoclave using a catalyst basket so that the catalyst material was thoroughly washed by the reactant/solvent mixture, and hydrogen was introduced. Hydrogenation was performed at a hydrogen pressure of 40 bar and a temperature of 150°C. The initiation temperature and the rate of hydrogen consumption were determined. The results are given in table 1. As a check, samples were withdrawn after 1, 2, 3, 4, and 5 h and analyzed using gas chromatography.
G +~
O rd U
O G
1~-a O
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Claims (12)
1. Metal catalysts comprising hallow forms.
2. Metal catalysts according to claim 1 comprising hallow spheres.
3. Metal catalysts according to claim 2 comprising a diameter of 0,5 to 20 mm and a wallthickness of 0,1 to mm.
4. Metal catalysts according to claim 2 comprising a shell which is unpermeable.
5. Metal catalysts according to claim 2 comprising a shell which shows an open porosity of maximum of about 80 %.
6. Metal catalysts according to claim 2 comprising a shell which consists of different layers.
7. Metal catalysts according to claim 2 comprising a shell which is graduated.
8. Process for the production of the metal catalysts according to claim 1, comprising spraying of metal powders, obtionally together with a binder on to forms consisting of a burnable material i.e. styrofoam, burning out the materal to receive the hallow form.
9. Process for the production of the metal catalysts according to claim 5 and 8 where one of the metal powders consists of a rapidly cooled alloy.
10. Process for the production of the metal catalysts according to claims 1 and 8 where one of the metal powders consists of a slowly cooled alloy.
11. Process for the production of the metal catalysts accroding to claim 9 and 10 where the alloy consist of one or more catalytic metal such as nickel, iron, copper, palladium, ruthenium, and cobalt; an alkaly soluble component such as aluminium, zinc, and silica;
and optionally one or more promoter elements such as Cr, Fe, Ti, V, Ta, Mo, Mg, Co, and/or W.
and optionally one or more promoter elements such as Cr, Fe, Ti, V, Ta, Mo, Mg, Co, and/or W.
12. Use of the metal catalysts according to claim 1 for the hydrogenation, dehydrogenation, isomerisation and/or hydration reaction of organic compounds.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19933450.1 | 1999-07-16 | ||
DE19933450A DE19933450A1 (en) | 1999-07-16 | 1999-07-16 | Metal catalysts |
Publications (1)
Publication Number | Publication Date |
---|---|
CA2313874A1 true CA2313874A1 (en) | 2001-01-16 |
Family
ID=7915061
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA002313874A Abandoned CA2313874A1 (en) | 1999-07-16 | 2000-07-13 | Metal catalysts |
Country Status (15)
Country | Link |
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EP (1) | EP1068900B1 (en) |
JP (1) | JP2001054735A (en) |
KR (1) | KR20010061920A (en) |
AT (1) | ATE243073T1 (en) |
BR (1) | BR0002920A (en) |
CA (1) | CA2313874A1 (en) |
DE (2) | DE19933450A1 (en) |
DK (1) | DK1068900T3 (en) |
ES (1) | ES2198246T3 (en) |
HU (1) | HUP0002632A3 (en) |
ID (1) | ID26548A (en) |
MX (1) | MXPA00006944A (en) |
NO (1) | NO20003618L (en) |
PL (1) | PL341469A1 (en) |
ZA (1) | ZA200003524B (en) |
Families Citing this family (24)
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EP1125634B1 (en) * | 2000-02-18 | 2010-12-08 | Evonik Degussa GmbH | Shaped fixed bed Raney-Cu catalyst |
US6486366B1 (en) * | 2000-12-23 | 2002-11-26 | Degussa Ag | Method for producing alcohols by hydrogenation of carbonyl compounds |
JP2004516308A (en) * | 2000-12-23 | 2004-06-03 | デグサ アクチエンゲゼルシャフト | Method for producing primary and secondary amines by hydrogenation of nitriles and imines |
DE10065030A1 (en) * | 2000-12-23 | 2002-07-04 | Degussa | Process for the preparation of 3-aminomethyl-3,5,5-trimethylcyclohexylamine |
DE10101646A1 (en) * | 2001-01-16 | 2002-07-18 | Degussa | Process for the production of saturated organic compounds |
DE10355298B4 (en) * | 2003-11-21 | 2006-10-26 | Glatt Systemtechnik Gmbh | Precursor for and process for producing green bodies for sintered lightweight components |
DE102005040599B4 (en) * | 2005-08-19 | 2007-07-05 | Glatt Systemtechnik Gmbh | A method for the production of hollow bodies with a spherical curved surface, hollow bodies produced by the process and their use |
EP1922146A1 (en) | 2005-09-08 | 2008-05-21 | Evonik Degussa GmbH | The production and use of supported activated base metal catalysts for organic transformation |
DE102007009981A1 (en) * | 2007-03-01 | 2008-09-04 | Evonik Degussa Gmbh | Hollow form mixed oxide catalyst for catalysis of gaseous phase oxidation of olefins, has general formula |
DE102007011483A1 (en) | 2007-03-07 | 2008-09-18 | Evonik Degussa Gmbh | Process for the preparation of 3-aminomethyl-3,5,5-trimethylcyclohexylamine |
DE102007011484A1 (en) | 2007-03-07 | 2008-09-11 | Evonik Degussa Gmbh | Process for the preparation of trimethylhexamethylenediamine |
JP5818244B2 (en) * | 2011-03-25 | 2015-11-18 | 国立研究開発法人物質・材料研究機構 | Metal catalyst structure and method for producing the same |
KR101403157B1 (en) * | 2012-08-30 | 2014-06-27 | 한국에너지기술연구원 | Method for producing ceramic honeycomb structure |
EP3216522A1 (en) | 2013-02-06 | 2017-09-13 | Alantum Europe GmbH | Surface modified metallic foam body, process for its production and use thereof |
EP3075721A1 (en) | 2015-03-30 | 2016-10-05 | Evonik Degussa GmbH | Method for the preparation of 3-aminomethyl-3,5,5-trimethylcyclohexylamine |
CN104888794B (en) * | 2015-05-21 | 2017-05-24 | 浙江新和成股份有限公司 | Metal composition catalyst, preparation method thereof and application thereof in preparation of D, L-menthol |
EP3162790A1 (en) | 2015-10-30 | 2017-05-03 | Evonik Degussa GmbH | Method for producing isophorone amino alcohol (ipaa) |
SG11201901336RA (en) | 2016-09-23 | 2019-04-29 | Basf Se | Method for providing a fixed catalyst bed containing a doped structured shaped catalyst body |
EP3515593A1 (en) | 2016-09-23 | 2019-07-31 | Basf Se | Method for activating a fixed catalyst bed which contains monolithic shaped catalyst bodies or consists of monolithic shaped catalyst bodies |
EP3515597A1 (en) | 2016-09-23 | 2019-07-31 | Basf Se | Method for the hydrogenation of organic compounds in the presence of co and a fixed catalyst bed which contains monolithic shaped catalyst body |
SG11201901571RA (en) | 2016-09-23 | 2019-04-29 | Basf Se | Process for providing a catalytically active fixed bed for the hydrogenation of organic compounds |
EP3300799A1 (en) * | 2016-09-30 | 2018-04-04 | Evonik Degussa GmbH | Method and catalyst for producing 1,4-butanediol |
US11173479B2 (en) | 2017-09-20 | 2021-11-16 | Basf Se | Method for producing a shaped catalyst body |
CN115945684B (en) * | 2022-12-02 | 2024-09-03 | 中国核动力研究设计院 | Tungsten alloy hollow sphere and preparation method and application thereof |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2172755A1 (en) * | 1972-02-21 | 1973-10-05 | Norton Co | Catalyst support - for gaseous reactions, comprising hollow refractory spheres |
DE2353631A1 (en) * | 1973-10-26 | 1975-05-07 | Hoechst Ag | Process for the production of a material consisting of stable hollow spheres |
US4039480A (en) * | 1975-03-21 | 1977-08-02 | Reynolds Metals Company | Hollow ceramic balls as automotive catalysts supports |
US4576926A (en) * | 1984-04-23 | 1986-03-18 | California Institute Of Technology | Catalytic hollow spheres |
US4804796A (en) * | 1984-04-23 | 1989-02-14 | California Institute Of Technology | Catalytic, hollow, refractory spheres, conversions with them |
DE3535483A1 (en) * | 1985-10-04 | 1987-04-09 | Hoechst Ag | METHOD FOR PRODUCING HYDROXYCARBONYL COMPOUNDS FROM 1.2-DIOLES |
DE3724156A1 (en) * | 1987-07-22 | 1989-02-02 | Norddeutsche Affinerie | METHOD FOR PRODUCING METALLIC OR CERAMIC HOLLOW BALLS |
US4826799A (en) * | 1988-04-14 | 1989-05-02 | W. R. Grace & Co.-Conn. | Shaped catalyst and process for making it |
DE19721897A1 (en) * | 1997-05-26 | 1998-12-03 | Degussa | Molded metal fixed bed catalyst, process for its production and its use |
-
1999
- 1999-07-16 DE DE19933450A patent/DE19933450A1/en not_active Ceased
-
2000
- 2000-07-13 ES ES00115180T patent/ES2198246T3/en not_active Expired - Lifetime
- 2000-07-13 ID IDP20000589Q patent/ID26548A/en unknown
- 2000-07-13 JP JP2000212796A patent/JP2001054735A/en active Pending
- 2000-07-13 CA CA002313874A patent/CA2313874A1/en not_active Abandoned
- 2000-07-13 AT AT00115180T patent/ATE243073T1/en not_active IP Right Cessation
- 2000-07-13 DK DK00115180T patent/DK1068900T3/en active
- 2000-07-13 EP EP00115180A patent/EP1068900B1/en not_active Expired - Lifetime
- 2000-07-13 ZA ZA200003524A patent/ZA200003524B/en unknown
- 2000-07-13 DE DE50002574T patent/DE50002574D1/en not_active Expired - Lifetime
- 2000-07-14 HU HU0002632A patent/HUP0002632A3/en unknown
- 2000-07-14 PL PL00341469A patent/PL341469A1/en not_active Application Discontinuation
- 2000-07-14 NO NO20003618A patent/NO20003618L/en unknown
- 2000-07-14 KR KR1020000040569A patent/KR20010061920A/en not_active Application Discontinuation
- 2000-07-14 MX MXPA00006944A patent/MXPA00006944A/en unknown
- 2000-07-17 BR BR0002920-3A patent/BR0002920A/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
HU0002632D0 (en) | 2000-09-28 |
ID26548A (en) | 2001-01-18 |
NO20003618L (en) | 2001-01-17 |
ES2198246T3 (en) | 2004-02-01 |
HUP0002632A2 (en) | 2001-12-28 |
HUP0002632A3 (en) | 2002-01-28 |
ZA200003524B (en) | 2001-02-06 |
KR20010061920A (en) | 2001-07-07 |
DE50002574D1 (en) | 2003-07-24 |
MXPA00006944A (en) | 2002-04-24 |
PL341469A1 (en) | 2001-01-29 |
NO20003618D0 (en) | 2000-07-14 |
DE19933450A1 (en) | 2001-01-18 |
DK1068900T3 (en) | 2003-09-15 |
BR0002920A (en) | 2001-04-03 |
EP1068900A1 (en) | 2001-01-17 |
JP2001054735A (en) | 2001-02-27 |
ATE243073T1 (en) | 2003-07-15 |
EP1068900B1 (en) | 2003-06-18 |
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