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公开(公告)号:AT253094B
公开(公告)日:1967-03-28
申请号:AT1074564
申请日:1964-12-18
Applicant: BASF AG
Inventor: MEYER HERMANN DR , MARKERT FERDINAND , SCHMIDT EMIL
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公开(公告)号:CA735515A
公开(公告)日:1966-05-31
申请号:CA735515D
Applicant: BASF AG
Inventor: FREY OTTO , DANZ WILLI , MARKERT FERDINAND , TELTSCHIK WALTER , KITTEL ERICH
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公开(公告)号:FR1432866A
公开(公告)日:1966-03-25
申请号:FR8273
申请日:1965-03-08
Applicant: BASF AG , SCHMIDT SCHE HEISSDAMPF
Inventor: BUSCHMANN KARL , MARKERT FERDINAND , MEYER HERMANN , VOLLHARDT FROHMUT
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公开(公告)号:GB942436A
公开(公告)日:1963-11-20
申请号:GB1393362
申请日:1962-04-11
Applicant: BASF AG
Inventor: DANZ WILLI , FREY OTTO , KITTEL ERICH , MARKERT FERDINAND , TELTSCHIK WALTER
Abstract: In the production of acetylene by subjecting hydrocarbons to high temperatures, the hot gas is quenched in a single stage by injecting a hydrocarbon oil boiling above 150 DEG C. in a volume ratio to gas (measured under standard conditions) of at least 1 : 100 without any appreciable cracking of the oil and separating the hot oil containing carbon black from the gas. The oil is preferably an aromatic oil and useful heat is extracted from it before its reuse; the carbon black content is preferably reduced to below 35% by weight e.g. by removing part of the oil and replacing this by fresh oil. The gas is preferably also later washed with an oil boiling in the range 80-450 DEG C. having a specific gravity below 0.95. The examples relate to the partial combustion of gasoline and of methane; reference is also made to heating hydrocarbons by electric discharge and exposure to hot flame gases. Specification 893,504 is referred to.
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15.
公开(公告)号:YU33820B
公开(公告)日:1978-05-15
申请号:YU73769
申请日:1969-03-26
Applicant: BASF AG
Inventor: FERDINAND MARKERT , MARKERT FERDINAND , MICHAEL SCHUNCK , SCHUNCK MICHAEL
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公开(公告)号:GB1087512A
公开(公告)日:1967-10-18
申请号:GB859366
申请日:1966-02-28
Applicant: BASF AG
Inventor: BUSCHMANN KARL , MARKERT FERDINAND , MEYER HERMANN , RICHTER GOTTFRIED , SCHWEITZER ARMIN
Abstract: Low molecular weight olefins, particularly ethylene, are obtained by thermal cracking in a cracking tube at above 750 DEG C. of aliphatic hydrocarbons having a final b.p. below 300 DEG C., e.g. light naphtha, followed by cooling to below 400 DEG C. in a cooling unit comprising either a single-tube cooler or a single-tube cooler followed by a multi-tube cooler, the single-tube cooler in either case being connected to the cracking tube by a connecting-piece so short that the residence time of the cracked gas in the connecting-piece is less than 0.01 sec. The connecting piece is preferably installed in the brickwork of the furnace casing, and is usually conical, the internal diameter of the cooling tube being greater than that of the cracking tube. More than one cracking tube may be connected to the same cooling unit. The process is stated to reduce undesirable side-reactions in the cracked gas, e.g. deposition of coke and production of methane and hydrogen.
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公开(公告)号:GB1032690A
公开(公告)日:1966-06-15
申请号:GB940565
申请日:1965-03-05
Applicant: BASF AG , SCHMIDT SCHE HEISSDAMPF
Inventor: BUSCHMANN KARL , MARKERT FERDINAND , MEYER HERMANN , VOLLHARDT FROHMUT
Abstract: In the production of ethylene by thermal cracking of hydrocarbons at above 750 DEG C., followed by indirect cooling in quench boilers, the gases are passed through the cooling tubes at a speed above 50 kg./m.2/sec., e.g. 60-70 kg./m.2/sec. The temperature of the cooling tubes is preferably above 310 DEG C. maintained by a steam pressure of at least 100 atmospheres. The velocity of the gas in the inlet cone of the boiler should be above 20 kg./cu.m./sec.
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公开(公告)号:FR1432867A
公开(公告)日:1966-03-25
申请号:FR8274
申请日:1965-03-08
Applicant: BASF AG , SCHMIDT SCHE HEISSDAMPF
Inventor: BUSCHMANN KARL , MARKERT FERDINAND , MEYER HERMANN , VOLLHARDT FROHMUT
Abstract: In the production of ethylene by thermal cracking of hydrocarbons at above 750 DEG C., followed by indirect cooling in quench boilers, the gases are passed through the cooling tubes at a speed above 50 kg./m.2/sec., e.g. 60-70 kg./m.2/sec. The temperature of the cooling tubes is preferably above 310 DEG C. maintained by a steam pressure of at least 100 atmospheres. The velocity of the gas in the inlet cone of the boiler should be above 20 kg./cu.m./sec.
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公开(公告)号:FR1239499A
公开(公告)日:1960-08-26
申请号:FR805883
申请日:1959-09-24
Applicant: BASF AG
Inventor: MARKERT FERDINAND , NONNENMACHER HELMUT , FUNK WILLIBALD , BIEBER HERMANN
IPC: C07C4/04
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