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公开(公告)号:DE59607970D1
公开(公告)日:2001-11-29
申请号:DE59607970
申请日:1996-03-27
Applicant: BASF AG
Inventor: SCHMIDT DR , SENS DR
IPC: C09B23/16 , B41M5/30 , B41M5/39 , C07C245/12 , C07D413/12 , C09B53/00 , C09B53/02 , C09B55/00 , D06P5/13 , B41M5/38
Abstract: Azamethine dyes of formula (I) are new, wherein K = a carboxylic or heterocyclic residue; X = N or C-Q and Q , Q and Q = H, 1-6 C alkyl which may be interrupted by 1 or 2 ether O atoms, benzyl, 3-8 C cycloalkyl, 1-4 C fluoroalkyl, opt. substd. phenyl, 1-6 C alkoxy, benzyloxy, opt. substd. phenoxy, 1-6 C alkylthio, halogen, CN, formylamino or a residue of formula R , -CO-OR , -CO-NHR , -CO-NH-CO-R , -CO-NH-CO-R , -CO-NH-SO2R , -NH-CO-R , -NH-CO-NR R , -NH-CS-OR , -NH-CS-NR R , -NH-CO-R , -NH-SO -R , -NH-SO -R or -NH-SO2-NR R in which R and R = 1-3 C alkyl which is opt. substd., 3-8 C cycloalkyl, opt. substd. phenyl or -NR R including amino; R = 5- or 6- membered non-aromatic heterocyclic residue which may be benzoanellated and which contains one or more heteroatoms chosen from N, O and S; and R4 = a 5- or 6- membered heterocyclic residue which is opt. benzoanellated and which contains one or more heteroatoms chosen from N, O and S, or Q and Q together may complete a 5- or 6-membered carboxylic or heterocyclic ring, with the proviso that at least one of Q , Q and Q = a gp. R .
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公开(公告)号:DE59806794D1
公开(公告)日:2003-02-06
申请号:DE59806794
申请日:1998-08-14
Applicant: BASF AG
Inventor: HUEBINGER DR , WUNDER DR , BAUER DR , DOBBELAAR DR , LAWRENZ SVEN , MUESELER DR , NAHSTOLL DR , RUPANER DR , SCHMIDT DR
Abstract: A method for cooling dispersions or liquids (D/L) after a deodorising process comprising (a) passing steam through the D/L in a boiler (1), causing it to foam, (b) taking the foam from the top of the boiler into an evacuated separator (4) through a jet (5) and thus breaking the foam, (c) condensing the water vapour from the foam in a heat exchanger (8) and removing organic volatiles, and (d) returning the broken foam to (1). This process is continued until the D/L is deodorised to the required extent, then the hot D/L is cooled by transferring it from the bottom of (1) to the evacuated separator (4) via jet (5), the water vapour produced is condensed in (8) as before, and the cooled D/L is taken off at the bottom of (4).
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