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...

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Hauptverfasser: LOEFFLER, MARTIN, SCHIMKO, RICHARD, ROEMER, SIEGFRIED, JAGAU, HERMANN
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Sprache:eng ; fre ; ger
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creator LOEFFLER, MARTIN
SCHIMKO, RICHARD
ROEMER, SIEGFRIED
JAGAU, HERMANN
description 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).
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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).</abstract><oa>free_for_read</oa></addata></record>
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subjects 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
title DEVICE FOR THE PYROLYSIS OF ORGANIC STARTING MATERIALS
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