Reactor arrangement for carrying out catalytic gas reactions

Reactor arrangement (I), for carrying out catalytic gaseous phase reactions, comprises a jacket tube reactor (2), a bundle of tubes and a separate, after cooler (3) directly connected to the side outlet, where the cross sectional area in the after cooler is essentially congruent with the cross secti...

Ausführliche Beschreibung

Gespeichert in:

Bibliographische Detailangaben
Hauptverfasser:	LEHR, MANFRED, GÜTLHUBER, FRIEDRICH
Format:	Patent
Sprache:	eng ; fre ; ger
Schlagworte:	APPARATUS THEREFOR BLASTING CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOIDCHEMISTRY CHEMISTRY DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OFGENERAL APPLICATION GENERAL METHODS OF ORGANIC CHEMISTRY HEAT EXCHANGE IN GENERAL HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS,IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT HEATING LIGHTING MECHANICAL ENGINEERING METALLURGY ORGANIC CHEMISTRY PERFORMING OPERATIONS PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL THEIR RELEVANT APPARATUS TRANSPORTING WEAPONS
Online-Zugang:	Volltext bestellen
Tags:	Tag hinzufügen Keine Tags, Fügen Sie den ersten Tag hinzu!

Beschreibung
Zusammenfassung:	Reactor arrangement (I), for carrying out catalytic gaseous phase reactions, comprises a jacket tube reactor (2), a bundle of tubes and a separate, after cooler (3) directly connected to the side outlet, where the cross sectional area in the after cooler is essentially congruent with the cross sectional area in the jacket and both the cross sectional areas are oppositely paired in large numbers. Reactor arrangement (I), for carrying out catalytic gaseous phase reactions, comprises a jacket tube reactor (2), a bundle of tubes with a number of catalyst-filled reaction tubes surrounded by the jacket, (where the reaction bundle of tubes lies in a cross sectional area perpendicularly to the longitudinal axis of the reaction tubes) and a separate, after cooler (3) directly connected to the side outlet (where the reaction tubes with the cooling tubes is surrounded by the envelope, the number of the cooling tubes is less than the reaction tube and the cooling tubes lies in a cross sectional area perpendicularly to the longitudinal axis of the cooling tubes (21)), where the cross sectional area (26, 27) in the after cooler is essentially congruent with the cross sectional area in the jacket tube reactor and both the cross sectional areas are oppositely paired in large numbers and in large parts with essentially same ratio of current cross-section of cooling tubes to the lower current cross section of the reaction tubes (7).