发明名称 Verdampfungsanlage
摘要 1,171,072. Evaporators, vapour-compression type. AQUA-CHEM, Inc. 12 Jan., 1968 [30 Jan., 1967], No. 1989/68. Heading B1B. Liquid, e.g. salt water, is partly evaporated in chamber 31, the vapours are withdrawn from the chamber through pipe 49 by compressor 50, the compressed vapour is supplied through pipe 51 to the tube-bundle 55 wherein most of the vapour condenses and boils the salt water flowing over the outer surface of the tube-bundle, the residual vapour and non-condensable gases flow, together with the condensate, into a vent condenser 22, mounted in the manifold on the end of the tube-bundle, where the residual vapour is condensed by heat-exchange with salt water which passes through the tubes of condenser 22 before entering chamber 31. The manifold on the end of tube-bundle 55 is divided by a partition into an upper half and a lower half; the upper half is connected by pipe 51 to the compressor, and the lower half houses the vent-condenser. Non-condensable gases are discharged from the condenser through pipe 57. Hot distillate, i.e. fresh water, is withdrawn from condenser 22 through pipe 56. Compressor 50 is driven by a diesel engine 14. Within chamber 31 is a supplementary boiler 70 comprising an open tank in which fresh water, circulated from and to the cooling jacket of engine 14 by pipes 78 and 76 respectively, is partly evaporated by means of exhaust gases from the engine which flow via pipe 74 through tubes in the open tank. The exhaust gases are then discharged through outlet 75. Some of the hot distillate flows from pipe 56 to the tank of boiler 70 whenever float 68 falls below a predetermined setting. Salt water is drawn into the system through strainer 12, and passes through heat exchanger 13 where it is preheated by lubricating oil circulated from engine 14. The water is then pumped through pipe 19 through plate-type heat exchanger 21 wherein it is heated by blow-down from sump 32 and by hot distillate from pipe 56. The salt water next flows through the tubes of condenser 22, and then through pipe 25 to pipe 27 where it mixes with some of the brine from sump 32. The mixture is then sprayed, through nozzles in tube 29, over tube bundle 55 in chamber 31. The pressure in chamber 31 is maintained constant by diaphragm valve 44 which admits cool salt water from pipe 20 into the chamber whenever the pressure rises above a predetermined value. Cool distillate is withdrawn from the system through valve 64.
申请公布号 DE1642435(A1) 申请公布日期 1971.06.03
申请号 DE1968A057951 申请日期 1968.01.16
申请人 AQUA-CHEM INC. 发明人 A. LOEBEL,FREDERICK
分类号 B01D1/28;C02F1/04;C02F1/18 主分类号 B01D1/28
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