PREVENTION OF COKING IN PYROLYSIS PLANTS

1,267,467. Preventing coking in pyrolysis plants. DEUTSCHE TEXACO A.G. 10 Nov., 1970 [28 Nov., 1969], No. 53450/70. Heading C5E. Coke obstructions are prevented in pyrolysis plants by causing the coke to deposit on a sieve in an easily accessible position in the flow path of the cracked gas stream b...

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Hauptverfasser: FISCHER R, SCHNEIDER H, HUSSNER R
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HUSSNER R
description 1,267,467. Preventing coking in pyrolysis plants. DEUTSCHE TEXACO A.G. 10 Nov., 1970 [28 Nov., 1969], No. 53450/70. Heading C5E. Coke obstructions are prevented in pyrolysis plants by causing the coke to deposit on a sieve in an easily accessible position in the flow path of the cracked gas stream between the pyrolysis furnace and the cooler. The sieve may comprise one or more wire mesh cages, preferably two disposed one within the other, the inner having a larger mesh size than the outer. In the example the cracked gases contain about 33 mole per cent ethylene obtained by pyrolysis of ethane. When the resistance of the sieve to the gas flow increases due to coke deposition the sieve is replaced.
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Coke obstructions are prevented in pyrolysis plants by causing the coke to deposit on a sieve in an easily accessible position in the flow path of the cracked gas stream between the pyrolysis furnace and the cooler. The sieve may comprise one or more wire mesh cages, preferably two disposed one within the other, the inner having a larger mesh size than the outer. In the example the cracked gases contain about 33 mole per cent ethylene obtained by pyrolysis of ethane. 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Preventing coking in pyrolysis plants. DEUTSCHE TEXACO A.G. 10 Nov., 1970 [28 Nov., 1969], No. 53450/70. Heading C5E. Coke obstructions are prevented in pyrolysis plants by causing the coke to deposit on a sieve in an easily accessible position in the flow path of the cracked gas stream between the pyrolysis furnace and the cooler. The sieve may comprise one or more wire mesh cages, preferably two disposed one within the other, the inner having a larger mesh size than the outer. In the example the cracked gases contain about 33 mole per cent ethylene obtained by pyrolysis of ethane. When the resistance of the sieve to the gas flow increases due to coke deposition the sieve is replaced.</abstract><oa>free_for_read</oa></addata></record>
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subjects ACYCLIC OR CARBOCYCLIC COMPOUNDS
BLASTING
CHEMISTRY
CRACKING HYDROCARBON OILS
DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OFGENERAL APPLICATION
FUELS
HEAT EXCHANGE IN GENERAL
HEATING
LIGHTING
LUBRICANTS
MECHANICAL ENGINEERING
METALLURGY
MINERAL WAXES
ORGANIC CHEMISTRY
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
WEAPONS
title PREVENTION OF COKING IN PYROLYSIS PLANTS
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