CH308889A - Method of making a catalyst. - Google Patents
Method of making a catalyst.Info
- Publication number
- CH308889A CH308889A CH308889DA CH308889A CH 308889 A CH308889 A CH 308889A CH 308889D A CH308889D A CH 308889DA CH 308889 A CH308889 A CH 308889A
- Authority
- CH
- Switzerland
- Prior art keywords
- catalyst
- bismuth
- palladium
- selective
- making
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title claims description 18
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 24
- 229910052763 palladium Inorganic materials 0.000 claims description 12
- 229910052797 bismuth Inorganic materials 0.000 claims description 7
- JCXGWMGPZLAOME-UHFFFAOYSA-N bismuth atom Chemical compound [Bi] JCXGWMGPZLAOME-UHFFFAOYSA-N 0.000 claims description 7
- 238000005984 hydrogenation reaction Methods 0.000 claims description 4
- 150000001621 bismuth Chemical class 0.000 claims description 3
- 239000012736 aqueous medium Substances 0.000 claims description 2
- 238000000034 method Methods 0.000 claims description 2
- 239000000243 solution Substances 0.000 description 6
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- WZGWWPARMFQTAY-UHFFFAOYSA-N ethene;methanol Chemical class OC.C=C WZGWWPARMFQTAY-UHFFFAOYSA-N 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 239000004280 Sodium formate Substances 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- WFYPICNXBKQZGB-UHFFFAOYSA-N butenyne Chemical group C=CC#C WFYPICNXBKQZGB-UHFFFAOYSA-N 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- RXPAJWPEYBDXOG-UHFFFAOYSA-N hydron;methyl 4-methoxypyridine-2-carboxylate;chloride Chemical compound Cl.COC(=O)C1=CC(OC)=CC=N1 RXPAJWPEYBDXOG-UHFFFAOYSA-N 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- HLBBKKJFGFRGMU-UHFFFAOYSA-M sodium formate Chemical compound [Na+].[O-]C=O HLBBKKJFGFRGMU-UHFFFAOYSA-M 0.000 description 1
- 235000019254 sodium formate Nutrition 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 239000005061 synthetic rubber Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/56—Platinum group metals
- B01J23/64—Platinum group metals with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/644—Arsenic, antimony or bismuth
- B01J23/6447—Bismuth
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Verfahren zur Herstellung eines Katalysators.
In der Literatur sind viele Katalysatoren zur selektiven Hydrierung von Dreifachbin- dungen zu Doppelbindungen beschrieben. Die Herstellung dieser Katalysatoren ist meist umständlich und die Wirkung nicht vollauf befriedigend, da trotz einer gewissen Selel- tivität auch noch Doppelbindungen hydriert werden.
Nach dem Verfahren des Patentes Nr. 2804616 wird ein Katalysator von hoher Selektivität dadurch gewonnen, dass man die Aktivität von, gegebenenfalls auf einemTräger aufgezogenem, Palladium durch Blei herabsetzt.
Es wurde nun gefunden, dass ebenfalls ein sehr selektiver Katalysator, bei dessen Anwendung Dreifaehbindungen zu Doppelbin dungen unter Schonung vorhandener oder entstehender Doppelbindungen sich hydrieren lassen, erhalten wird, wenn die Aktivität eines Palladiumkatalysators in Form von Palladiummetall ohne und mit Trägern, zum Beispiel mit Bariumsulfat, Ton, Calciumsulfat, Calciumearbonat, Magnesiumoxyd, Kohle als Träger, mit Wismut herabgesetzt wird. Wismut wird in Form eines Salzes in wässeriger Losung bzw. als Suspension angewandt, indem die Suspension des Katalysators mit einem Salz des betreffenden Metalles gerührt und während kurzer Zeit erhitzt wird.
Gegenstand des vorliegenden Patentes ist ein Palladiumkatalysator für selektive Hy drierungen, welcher gekennzeichnet ist durch einen Gehalt an Wismut. Es wird angenommen, dass sich das'Wismut mit dem Palladium legiert und sich vor allem in den oberflächennahen Bezirken der einzelnen Katalysatorteilchen befindet, während das Innere der Teilchen wismutfrei bleibt.
Das Patent betrifft ferner ein Verfahren zur Herstellung eines selektiven Palladiumkatalysators gemäss der Erfindung, welches dadurch gekennzeichnet ist, dass ein nicht- selektiver Palladiumkatalysator in wässerigem Milieu mit einem Wismutsalz in Kontakt gebracht wird.
Der Katalysator ist leicht herstellbar, leicht zu reproduzieren, nicht pyrophor und kann überall da angewandt werden, wo Dreifachbindungen in Doppelbindungen verwandelt werden sollen. In gewissen Fällen empfiehlt sich die Zugabe von etwas Chinolin hauptsächlich bei der Hydrierung von Molekülen, in denen schon mehrere Doppelbindungen neben der Dreifachbindung vorhanden sind. Der Katalysator eignet sich vor züglich zur partiellen Hydrierung von Acetylenkohlenwasserstoffen und Acetylenearbinolen. Beispielsweise wird Acetylen in Aceton- lasung in guter Ausbeute zu Äthylen hydriert.
In analoger Weise gelingt die Partialhydrierung von Vinylacetylen, eines Zwischenpro- duktes des synthetischen Kautschuks. Aeety- lencarbinole, zum Beispiel 1-Oxy-äthinyl1, 5, 9, 13-tetramethyltetradecan werden in vor züglicher Ausbeute zu den entsprechenden Äthylencarbinolen reduziert.
Mit Wismut desaktiviertem Katalysator-gelingt es, 1, 6-Dioxy 3, 7-dimethyl-9- [trimethyl-eyclohexen- (1')-yl]- nonadien- (2, 7)-in- (4) vom Schmelzpunkt 54 bis 56¯ C in PetrolÏther bei Gegenwart von Chinolin mit einer Ausbeute von 85 /o i 1, 6-Dioxy - 3,7 - dimethyl - 9 - [trimethyl-cyclohexen-(l')-yl]-nonatrien-(2,4,7) vom Schmelzpunkt 73 bis 74¯ C berzuf hren.
Beispiel :
20 Teile einer 5prozentigen Palladiumchlorürlösung werden mit heissem Wasser auf 200 Raumteile verdünnt, dann wird so lange eine 5prozentige Sodalösung zugefügt, bis alles Palladium gefällt ist. Zur heissen Suspension lässt man vorsichtig eine Natriumformiat I¯sung, welche aus 1 Teil Ameisensäure und 30 Teilen 5prozentiger Sodalosung hergestellt wird, zutropfen. Nachdem alles reduziert ist, wird das Wasser vom Palladiummetall dekantiert und dieses durch wiederholtes Dekan- tieren gründlich ausgewaschen. Nun wird das Palladium in 20 Teilen Wasser suspendiert und mit 1 Teil Wismutnitrat versetzt und ger hrt.
Durch Zugabe von Salzsäure erhält man das WismutsalzinLosung.Nachdem 1/2 Stunde bei 90 C gerührt worden ist, wird abfiltriert, gewaschen, getrocknet und fein gesiebt.
Method of making a catalyst.
Many catalysts for the selective hydrogenation of triple bonds to double bonds are described in the literature. The preparation of these catalysts is usually cumbersome and the effect is not entirely satisfactory, since double bonds are also hydrogenated despite a certain selectivity.
According to the process of patent no. 2804616, a catalyst of high selectivity is obtained by reducing the activity of palladium, possibly supported on a support, with lead.
It has now been found that a very selective catalyst, with the use of which triple bonds to double bonds can be hydrogenated while protecting existing or emerging double bonds, is obtained if the activity of a palladium catalyst in the form of palladium metal with and without supports, for example with barium sulfate , Clay, calcium sulfate, calcium carbonate, magnesium oxide, carbon as a carrier, is lowered with bismuth. Bismuth is used in the form of a salt in aqueous solution or as a suspension by stirring the suspension of the catalyst with a salt of the metal in question and heating it for a short time.
The subject of the present patent is a palladium catalyst for selective Hy drations, which is characterized by a content of bismuth. It is assumed that the bismuth is alloyed with the palladium and is mainly located in the areas of the individual catalyst particles close to the surface, while the interior of the particles remains free of bismuth.
The patent also relates to a method for producing a selective palladium catalyst according to the invention, which is characterized in that a non-selective palladium catalyst is brought into contact with a bismuth salt in an aqueous medium.
The catalyst is easy to prepare, easy to reproduce, not pyrophoric and can be used wherever triple bonds are to be converted into double bonds. In certain cases it is advisable to add a little quinoline mainly when hydrogenating molecules in which there are already several double bonds in addition to the triple bond. The catalyst is particularly suitable for the partial hydrogenation of acetylenic hydrocarbons and acetylenearbinols. For example, acetylene is hydrogenated to ethylene in good yield in acetone solution.
The partial hydrogenation of vinyl acetylene, an intermediate product of synthetic rubber, is carried out in an analogous manner. Ethylene carbinols, for example 1-oxyethinyl1, 5, 9, 13-tetramethyltetradecane, are reduced to the corresponding ethylene carbinols in an excellent yield.
With bismuth deactivated catalyst it is possible to obtain 1,6-dioxy 3, 7-dimethyl-9- [trimethyl-eyclohexen- (1 ') -yl] -nonadiene- (2, 7) -yne- (4) with a melting point of 54 up to 56¯ C in petroleum ether in the presence of quinoline with a yield of 85% 1,6-dioxy-3,7-dimethyl-9 - [trimethyl-cyclohexen- (l ') - yl] -nonatriene- (2,4 , 7) from melting point 73 to 74¯ C.
Example:
20 parts of a 5 percent palladium chloride solution are diluted to 200 parts by volume with hot water, then a 5 percent soda solution is added until all the palladium has precipitated. A sodium formate solution, which is prepared from 1 part of formic acid and 30 parts of 5 percent soda solution, is carefully added dropwise to the hot suspension. After everything has been reduced, the water is decanted from the palladium metal and this is thoroughly washed out by repeated decanting. The palladium is now suspended in 20 parts of water, 1 part of bismuth nitrate is added and the mixture is stirred.
The bismuth salt is obtained in solution by adding hydrochloric acid. After the mixture has been stirred at 90 ° C. for 1/2 hour, it is filtered off, washed, dried and finely sieved.
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH308889T | 1949-12-05 |
Publications (1)
Publication Number | Publication Date |
---|---|
CH308889A true CH308889A (en) | 1955-08-15 |
Family
ID=4493619
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CH308889D CH308889A (en) | 1949-12-05 | 1949-12-05 | Method of making a catalyst. |
Country Status (1)
Country | Link |
---|---|
CH (1) | CH308889A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4245942A (en) | 1977-10-05 | 1981-01-20 | Ab Nordstroms Linbanor | Bulk cargo ship hold arrangement |
-
1949
- 1949-12-05 CH CH308889D patent/CH308889A/en unknown
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4245942A (en) | 1977-10-05 | 1981-01-20 | Ab Nordstroms Linbanor | Bulk cargo ship hold arrangement |
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