-
公开(公告)号:DE1179711B
公开(公告)日:1964-10-15
申请号:DEB0067267
申请日:1962-05-16
Applicant: BASF AG
Inventor: ROTZOLL DR RUDI-HEINZ , IMMEL DR WOLFGANG , KINKEL DR KLAUS , URBAN DR FRIEDRICH , ZACHER DR WIELAND
IPC: C08F10/00
-
公开(公告)号:DE1089759B
公开(公告)日:1960-09-29
申请号:DEB0050056
申请日:1958-08-22
Applicant: BASF AG
Inventor: SCHICKH DR OTTO V , ROTZOLL DR RUDI-HEINZ
Abstract: Saturated hydroxy carboxylic acid nitriles and/or unsaturated carboxylic acid nitriles are prepared by reacting a lactone or a C-alkylated lactone with gaseous ammonia in the presence of an acid dehydration catalyst at elevated temperature. The omega-hydroxy carboxylic acid amide may be obtained as by-products. Specified lactones are gamma-butyro-, deltavalero-, epsilon-capro-, zeta-oenantho-, etacaprylo-lactones and their alkyl derivatives. Suitable dehydration catalysts include phosphoric acid, acid phosphates, boron phosphates and sulphuric acid and its acid salts, as such or on carriers.
-
公开(公告)号:DE1236199B
公开(公告)日:1967-03-09
申请号:DEB0069403
申请日:1962-10-27
Applicant: BASF AG
Inventor: KINKEL DR KLAUS , PFANNMUELLER DR HELMUT , ROTZOLL DR RUDI-HEINZ , URBAN DR FRIEDRICH
IPC: C08F10/00
-
公开(公告)号:DE1131884B
公开(公告)日:1962-06-20
申请号:DEB0059855
申请日:1960-10-25
Applicant: BASF AG
Inventor: EILBRACHT DR HANS , PFANNMUELLER DR HELMUT , ROTZOLL DR RUDI-HEINZ , TRIESCHMANN DR HANS-GEORG , URBAN DR FRIEDRICH , ZACHER DR WIELAND
IPC: C08F10/00
-
公开(公告)号:DE1106895B
公开(公告)日:1961-05-18
申请号:DEB0051617
申请日:1958-12-31
Applicant: BASF AG
Inventor: DEHNERT DR JOHANNES , ROTZOLL DR RUDI-HEINZ
-
-
公开(公告)号:DE1208494B
公开(公告)日:1966-01-05
申请号:DEB0063794
申请日:1961-08-26
Applicant: BASF AG
Inventor: EILBRACHT DR HANS , ROTZOLL DR RUDI-HEINZ , TRIESCHMANN DR HANS-GEORG , URBAN DR FRIEDRICH
Abstract: Recycle ethylene in the high pressure polymerization of ethylene is purified by washing at least 25% of the ethylene, after any polyethylene having a molecular weight of more than 20,000 has been separated, with liquid ethylene at below 50.9 atmospheres. After the polythylene has been separated, a portion, e.g. 5-20%, of the recycle ethylene may be liquefied and the remainder of the recycle ethylene is washed with the liquefied ethylene. The washing may be carried out in a wash column with the liquid ethylene in counter-current to the gas at 25-40 atmospheres and -25 to 0 DEG C. The polyethylene may be used to form sheets.ALSO:Recycle ethylene in the high pressure polymerization of ethylene is purified by washing at least 25% of the ethylene, after any polyethylene having a molecular weight of more than 20,000 has been separated, with liquid ethylene at below 50.9 atm. After the polyethylene has been separated, a portion, e.g. 5-20% of the recycle ethylene may be liquefied and the remainder of the recycle ethylene is washed with the liquefied ethylene. The washing may be carried out in a wash column with the liquid ethylene in counter current to the gas at 25-40 atm. and - 25 DEG to 0 DEG C. The polyethylene may be used to form sheets.
-
-
-
-
-
-