AT80708B - Process for hydrogenating naphthalene. Process for hydrogenating naphthalene. - Google Patents
Process for hydrogenating naphthalene. Process for hydrogenating naphthalene.Info
- Publication number
- AT80708B AT80708B AT80708DA AT80708B AT 80708 B AT80708 B AT 80708B AT 80708D A AT80708D A AT 80708DA AT 80708 B AT80708 B AT 80708B
- Authority
- AT
- Austria
- Prior art keywords
- naphthalene
- hydrogenating
- nickel
- hydrogenating naphthalene
- hydrogenation
- Prior art date
Links
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 title claims description 24
- 238000000034 method Methods 0.000 title claims description 6
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 7
- 238000005984 hydrogenation reaction Methods 0.000 claims description 7
- 229910052739 hydrogen Inorganic materials 0.000 claims description 5
- 239000001257 hydrogen Substances 0.000 claims description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 4
- 229910000008 nickel(II) carbonate Inorganic materials 0.000 claims description 4
- ZULUUIKRFGGGTL-UHFFFAOYSA-L nickel(ii) carbonate Chemical compound [Ni+2].[O-]C([O-])=O ZULUUIKRFGGGTL-UHFFFAOYSA-L 0.000 claims description 4
- 239000003054 catalyst Substances 0.000 claims description 2
- 239000002184 metal Substances 0.000 description 7
- 229910052751 metal Inorganic materials 0.000 description 7
- 229910052759 nickel Inorganic materials 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 150000002790 naphthalenes Chemical class 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910000480 nickel oxide Inorganic materials 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
<Desc/Clms Page number 1>
Verfahren zum Hydrieren von Naphtalin.
Die Erfindung besteht darin. dass Naphtalin unter Zusatz von Nickelcarbonat bei einer zwischen 200 und 280"liegenden Temperatur mit Wasserstoff behandelt wird. Das Nicke ! carbonat wird dabei zu Metall reduziert, das die Wasserstoffübertragung bewirkt.
Der Vorteil des Verfahrens gegenüber der bisher bekannten Methode der Hydrierung von Naphtalin mit einem, durch trockene Reduktion von Nickeloxyd hergestellten Metall besteht in der viel feineren Verteilung des Metalles.
EMI1.1
aus sehr kleinen, amorphen Teilchen. Durch die bei der Reduktion abgespaltene Kohlensäure wird jedes Teilchen noch weiter in allerfeinste Elemente zerrissen und das entstehende Metall hat daher von Anfang an eine besonders grosse Oberflächenentwicklung. Es hat sich gezeigt, dass ein solches Metall befähigt ist, sich in naphthalin kolloidal zu verteilen und in dieser Form eine besonders rasche Hydrierung des Naphtatins zu bewirken.
Der technische Effekt äussert
EMI1.2
reduziertem Nickel'', dass kein Träger verwendet werden muss und dass die umständliche.. trockene Reduktion" wegfällt.
Die Fähigkeit des naphtalines mit Nickel haltbare, kolloidale Lösungen zu bilden, war bisher nicht bekannt. Da das nicht auf Trägern befindliche Nickel sehr zum Zusammenballen und jAusflocken"neigt, so ist dieses Resultat überraschend.
EMI1.3
Xickelcarbonat versetzt und bei 220 bis 2500 mit einem kräftigen Wasserstoffstrom behandelt. Der Druck wird dabei auf solcher Höhe erhalten, dass die Flüssigkeit noch nicht siedet. Die mit dem Wasserstoff mitgehenden Naphtalindämpfe können in einem Rückflusskühler kondensiert werden. Durch passende Einstellung der Kühlertemperatur kann man dafür sorgen, dass die niedriger siedenden Hydrierungsprodukte des Naphtalins überdestillieren, während das noch nicht hydrierte Naphtalin nach dem Reduktionsgefäss zurückkehrt.
Es tritt rasche Reduktion des Carbonats, kolloidale Verteilung des Metalls und gleichzeitig rasche Hydrierung des Naphtalins ein. Die Operation kann in jedem beliebigen Stadium der Hydrierung unterbrochen werden. Der gebrauchte Katalysator wird durch Filtration oder durch Abdestillieren von dem hydrierten Naphtalin getrennt und kann, soferne seine Reduktion zu Metall noch nicht zu weit ins Innere fortgeschritten ist, bzw. soferne er noch ausreichende Schwimmfähigkeit und katalytische Wirk- samkeit besitzt, zu weiteren Hydrierungen verwendet werden.
**WARNUNG** Ende DESC Feld kannt Anfang CLMS uberlappen**.
<Desc / Clms Page number 1>
Process for hydrogenating naphthalene.
The invention consists in this. that naphthalene is treated with hydrogen with the addition of nickel carbonate at a temperature between 200 and 280 ". The nickel carbonate is reduced to metal, which causes the hydrogen transfer.
The advantage of the process over the previously known method of hydrogenating naphthalene with a metal produced by dry reduction of nickel oxide is the much finer distribution of the metal.
EMI1.1
from very small, amorphous particles. Due to the carbon dioxide split off during the reduction, each particle is torn even further into the finest elements and the resulting metal therefore has a particularly large surface development from the start. It has been shown that such a metal is able to distribute itself colloidally in naphthalene and, in this form, to bring about a particularly rapid hydrogenation of the naphthalene.
The technical effect is evident
EMI1.2
reduced nickel '' that no carrier has to be used and that the cumbersome "dry reduction" is no longer necessary.
The ability of naphthalene to form stable colloidal solutions with nickel was not previously known. Since the nickel which is not located on a carrier tends to agglomerate and flocculate very much, this result is surprising.
EMI1.3
Added nickel carbonate and treated at 220 to 2500 with a vigorous stream of hydrogen. The pressure is maintained at such a level that the liquid does not yet boil. The naphthalene vapors entrained with the hydrogen can be condensed in a reflux condenser. By setting the cooler temperature appropriately, you can ensure that the lower-boiling hydrogenation products of the naphthalene distill over, while the not yet hydrogenated naphthalene returns to the reduction vessel.
Rapid reduction of the carbonate, colloidal distribution of the metal and, at the same time, rapid hydrogenation of the naphthalene occur. The operation can be interrupted at any stage of the hydrogenation. The used catalyst is separated from the hydrogenated naphthalene by filtration or by distilling off and can be used for further hydrogenations if its reduction to metal has not progressed too far into the interior or if it still has sufficient buoyancy and catalytic effectiveness .
** WARNING ** End of DESC field may overlap beginning of CLMS **.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT80708T | 1916-10-05 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT80708B true AT80708B (en) | 1920-05-25 |
Family
ID=3602253
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT80708D AT80708B (en) | 1916-10-05 | 1916-10-05 | Process for hydrogenating naphthalene. Process for hydrogenating naphthalene. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT80708B (en) |
-
1916
- 1916-10-05 AT AT80708D patent/AT80708B/en active
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