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公开(公告)号：US3818002A
公开(公告)日：1974-06-18
申请号：US19399771
申请日：1971-10-29
Applicant: BASF AG
Inventor： GOELZ H , STOCKBURGER D , SAEUBERLICH M , VON ERDEN K , MUELLER F , FUCHS H
IPC: C07D251/36 , C07D55/38
CPC classification number: C07D251/36
Abstract: Production of dry sodium dichloroisocyanurate by spray-drying and up to 50 percent w/w aqueous solution or sussion of the salt in a fluidized bed maintained by inert gases and consisting of finely divided dry sodium dichloroisocyanurate, at from 100* to 300*C.
Abstract translation: 在惰性气体保持的流化床中通过喷雾干燥和高达50％w / w的水溶液或盐的冲洗来生产干燥的二氯异氰脲酸钠，并由细分的干二氯异氰脲酸钠组成，在100-300℃下。
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公开(公告)号：US3813375A
公开(公告)日：1974-05-28
申请号：US23095872
申请日：1972-03-01
Applicant: BASF AG
Inventor： GIERTH V , ZEITLER G , KLOCKE H , STOCKBURGER D
CPC classification number: C08J3/14 , C08J2323/04
Abstract: METHOD OF MAKING POWDERS FROM ETHYLENE POLYMERS BY DISSOLVING THE ETHYLENE POLYMERS AT A TEMPERATURE ABOVE 60*C. IN A FLUORINATED CHLOROHYDROCARBON HAVING FROM 1 TO 4 CARBON STOMS AND 0 TO 2 HYDROGEN ATOMS, COOLING THE SOLUTION TO A TEMPERATURE BELOW 60*C. OR EVAPORATING THE SOLVENT AND COLLECTING THE PULVERIZED ETHYLENE POLYMERS.
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3.发明授权
公开(公告)号：US3805870A
公开(公告)日：1974-04-23
申请号：US24322972
申请日：1972-04-12
Applicant: BASF AG
Inventor： SCHENK W , STOCKBURGER D
IPC: B01D1/00 , B01D1/16 , C07C20060101 , C07C309/20 , C08F228/00 , C25D3/12 , F17C7/00 , C07C143/16
CPC classification number: C07C303/42 , Y10S159/10 , Y10S159/13 , Y10S422/901
Abstract: Process for the manufacture of highly concentrated sodium vinyl sulfonate solutions or dry sodium vinyl sulfonate by evaporation of water therefrom.
Abstract translation: 通过蒸发水从而制造高浓度乙烯基磺酸钠溶液或干乙烯基磺酸钠的方法。
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公开(公告)号：DK138548C
公开(公告)日：1979-02-26
申请号：DK700273
申请日：1973-12-21
Applicant: BASF AG
Inventor： WEISER D , STOCKBURGER D , THOMA P , KLOCKE H J , BEYSE H-J , THOMAE H
Abstract: A process for the manufacture of non-dusting dye granules from an aqueous formulation of highly dispersed water-insoluble dyes by spraying the formulation, which contains adhesive compounds, into a fluidized bed of pulverulent dispersing agent, dye or mixture thereof. The resulting granules possess excellent redispersibility, which is important in using them.
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公开(公告)号：BR7803386A
公开(公告)日：1979-01-02
申请号：BR7803386
申请日：1978-05-26
Applicant: BASF AG
Inventor： WEITZ H , BENDER D , VOLKAMER K , STOCKBURGER D , WAGNER U , SCHWENTKER H , SCHNEIDER K
Abstract: A process for separating, by means of a selective solvent, a mixture of C4-hydrocarbons which contains some hydrocarbons which are more soluble in the selective solvent and some which are less soluble therein, in which process the hydrocarbon mixture is separated, in an extractive distillation zone, into a top product which contains the less soluble hydrocarbons and an extract which contains the more soluble hydrocarbons and the selective solvent, the extract, taken off as the bottom product, is subjected to a flash evaporation and the resulting vapor component of the extract is recycled to the extractive distillation zone while the liquid phase remaining after the flash evaporation is fed to a solvent recovery zone, in which the liquid phase obtained from the flash evaporation is separated into a product containing the hydrocarbons and, as the bottom product, the selective solvent which has been freed from the hydrocarbons, the resulting selective solvent is recycled to the extractive distillation zone and the product which is obtained from the solvent recovery zone and contains the hydrocarbons is partially or completely recycled to the extractive distillation zone, after increasing the pressure in a compression zone, in which process the extract taken off the extractive distillation zone is brought, prior to the flash evaporation to a higher pressure than the pressure in the extractive distillation zone and thereafter the extract which is under this higher pressure is heated, in a heat exchange zone, by indirect heat exchange with the selective solvent obtained as the bottom product from the solvent recovery zone, and the heated extract is subsequently let down, in the flash evaporation, to a pressure which is at least equal to the pressure in the extractive distillation zone and is higher than the pressure in the solvent recovery zone.
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Patent Agency Ranking
公开(公告)号：DK138548B
公开(公告)日：1978-09-25
申请号：DK700273
申请日：1973-12-21
Applicant: BASF AG
Abstract: A process for the manufacture of non-dusting dye granules from an aqueous formulation of highly dispersed water-insoluble dyes by spraying the formulation, which contains adhesive compounds, into a fluidized bed of pulverulent dispersing agent, dye or mixture thereof. The resulting granules possess excellent redispersibility, which is important in using them.
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公开(公告)号：BR7310174D0
公开(公告)日：1974-08-15
申请号：BR1017473
申请日：1973-12-27
Applicant: BASF AG
Abstract: A process for the manufacture of non-dusting dye granules from an aqueous formulation of highly dispersed water-insoluble dyes by spraying the formulation, which contains adhesive compounds, into a fluidized bed of pulverulent dispersing agent, dye or mixture thereof. The resulting granules possess excellent redispersibility, which is important in using them.
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公开(公告)号：BR7205348D0
公开(公告)日：1974-10-29
申请号：BR534872
申请日：1972-08-08
Applicant: BASF AG
Inventor： KAHRM K , SAEUBERLICH M , LEONHARD K , STOCKBURGER D
IPC: B01J2/02 , C07D201/02 , C07D201/16 , C07D41/06
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公开(公告)号：CA922465A
公开(公告)日：1973-03-13
申请号：CA80890
申请日：1970-04-22
Applicant: BASF AG
Inventor： GEHRING H , STOCKBURGER D , STEIGERWALD K , FAUTH K H , URBAN F , RICHARD SINN
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公开(公告)号：SE7806079L
公开(公告)日：1978-11-29
申请号：SE7806079
申请日：1978-05-26
Applicant: BASF AG
Inventor： STOCKBURGER D , VOLKAMER K , BENDER D , SCHNEIDER K-J , SCHWENTKER H , WAGNER U , WEITZ H-M
Abstract: A process for separating, by means of a selective solvent, a mixture of C4-hydrocarbons which contains some hydrocarbons which are more soluble in the selective solvent and some which are less soluble therein, in which process the hydrocarbon mixture is separated, in an extractive distillation zone, into a top product which contains the less soluble hydrocarbons and an extract which contains the more soluble hydrocarbons and the selective solvent, the extract, taken off as the bottom product, is subjected to a flash evaporation and the resulting vapor component of the extract is recycled to the extractive distillation zone while the liquid phase remaining after the flash evaporation is fed to a solvent recovery zone, in which the liquid phase obtained from the flash evaporation is separated into a product containing the hydrocarbons and, as the bottom product, the selective solvent which has been freed from the hydrocarbons, the resulting selective solvent is recycled to the extractive distillation zone and the product which is obtained from the solvent recovery zone and contains the hydrocarbons is partially or completely recycled to the extractive distillation zone, after increasing the pressure in a compression zone, in which process the extract taken off the extractive distillation zone is brought, prior to the flash evaporation to a higher pressure than the pressure in the extractive distillation zone and thereafter the extract which is under this higher pressure is heated, in a heat exchange zone, by indirect heat exchange with the selective solvent obtained as the bottom product from the solvent recovery zone, and the heated extract is subsequently let down, in the flash evaporation, to a pressure which is at least equal to the pressure in the extractive distillation zone and is higher than the pressure in the solvent recovery zone.
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