DEVICE FOR THE PYROLYSIS OF ORGANIC STARTING MATERIALS

The present invention relates to a device (1000) for the continuous pyrolysis of organic starting materials (10). The device (1000) comprises a pyrolysis reactor (100) with a tin bath as pyrolysis bath (120) at a temperature of approximately 480°C, a devolatilizer (200) for metal deposition and deso...

Ausführliche Beschreibung

Gespeichert in:

Bibliographische Detailangaben
Hauptverfasser:	LOEFFLER, MARTIN, SCHIMKO, RICHARD, ROEMER, SIEGFRIED, JAGAU, HERMANN
Format:	Patent
Sprache:	eng ; fre ; ger
Schlagworte:	CHEMISTRY CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION ORPROCESSING OF GOODS CRACKING HYDROCARBON OILS DESTRUCTIVE DISTILLATION OF CARBONAGEOUS MATERIALS FORPRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS FUELS GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS LUBRICANTS METALLURGY MINERAL WAXES PEAT PETROLEUM, GAS OR COKE INDUSTRIES PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVEHYDROGENATION, OLIGOMERISATION, POLYMERISATION RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, ORGASES REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS REFORMING OF NAPHTHA TECHNICAL GASES CONTAINING CARBON MONOXIDE TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE
Online-Zugang:	Volltext bestellen
Tags:	Tag hinzufügen Keine Tags, Fügen Sie den ersten Tag hinzu!

Beschreibung
Zusammenfassung:	The present invention relates to a device (1000) for the continuous pyrolysis of organic starting materials (10). The device (1000) comprises a pyrolysis reactor (100) with a tin bath as pyrolysis bath (120) at a temperature of approximately 480°C, a devolatilizer (200) for metal deposition and desorption of hydrocarbon residues, and a cooler (300) for cooling, comminuting and discharging the pyrolysis solids (910). The starting materials (10), such as comminuted used tyres, for example, are supplied to the pyrolysis reactor (100) via an entry lock (800). Arranged in the reactor (100) is a hood (152) which reduces the area that the pyrolysis vapours (130) can occupy and that has an inlet (154) for recycled pyrolysis gas (720). The introduction of a defined pyrolysis gas flow into the reactor space (180) ensures rapid and directed removal of the pyrolysis vapours (130) to a condensation device (500). The device (1000) of the invention is notable more particularly for a metal recycling facility (400) which conveys metal deposited in the devolatilizer (200) back into the pyrolysis bath (120).