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    • 3. 发明公开
    • MECHANICAL VAPOR RECOMPRESSION SYSTEM AND METHOD THEREOF
    • 机械蒸气再循环系统及其方法
    • EP3238797A1
    • 2017-11-01
    • EP15871968.2
    • 2015-12-24
    • Gardner Denver Machinery (Shanghai) Co. Ltd.
    • YANG, ZhimingLIU, Mingtong
    • B01D1/00B01D1/30
    • B01D1/2887B01D1/00B01D1/284B01D1/30B01D3/10B01D5/006C02F1/041
    • A mechanical vapor recompression system and method thereof. The system comprises: an evaporator (20), a first cavity (30), a first fluid collection area (31), a second cavity (32) and a blowing type pump (33), the evaporator (20) having a high temperature fluid reception channel (21 a) and a low temperature fluid reception channel (21 b); the method comprises: enabling a first fluid to flow from a vapor source (10) to the high temperature fluid reception channel (21a) of the evaporator (20), enabling liquid water collected from a first fluid supply to flow to the low temperature reception channel (21b), and transferring heat of vaporous water in the high temperature reception channel (21 a) to the liquid water collected in the low temperature reception channel (21 b); converting at least a part of the liquid water collected in the low temperature reception channel (21 b) to vaporous water, and returning the further heated vaporous water to the vapor source (10).
    • 机械蒸气再压缩系统及其方法。 该系统包括:蒸发器(20),第一腔体(30),第一流体收集区域(31),第二腔体(32)和吹气式泵(33),蒸发器(20)具有高温 流体接收通道21a和低温流体接收通道21b; 该方法包括:使第一流体能够从蒸发源(10)流到蒸发器(20)的高温流体接收通道(21a),使得从第一流体供给源收集的液态水流动到低温接收器 将所述高温侧的接收流路21a内的蒸气水的热量传递给所述低温侧的接收流路21b内的液态水。 将收集在低温接收通道(21b)中的液态水的至少一部分转换成蒸汽水,并将进一步加热的蒸汽水返回蒸汽源(10)。
    • 5. 发明公开
    • PROCEDE ET APPAREIL DE DISTILLATION NOTAMMENT POUR PRODUIRE DE L'EAU DOUCE
    • 方法和装置DESTILLIATION特别适合制作淡水
    • EP1636138A2
    • 2006-03-22
    • EP04767241.5
    • 2004-06-03
    • The Third Millenium Water Company
    • DOMEN, Jean-PaulVIANNAY, Stéphane
    • C02F1/14
    • B01D1/007B01D1/0047B01D1/221B01D1/30B01D3/346C02F1/04C02F1/14C02F2103/08Y02A20/128Y02A20/129Y02A20/142Y02A20/211Y02A20/212Y02P70/34Y02W10/37
    • The inventive device is embodied in the form of a chamber-oven for diffusing vapour and saturated hot air which circulate in a closed circuit by natural convection. Said device is embodied in the form of a domestic-use solar energy collecting device provided with a greenhouse whose surface is equal to 1 m2 and produces from 50 to 100 litres/day of distilled water. The device comprises a distillation unit arranged between two furnaces (59', 79') in a temperature-controlled container (48'). Said distillation unit comprises 100 flat thin hollow plates having a surface of 20 dm2 by face and an active volume of 200 dm3 . The fine and tensioned walls (54') of said plates are provided with a hydrophilic coating (60') and internal (56') and inter-plate (58') spaces. The lower chimney (59') comprises a greenhouse (118', 119') whose bottom is embodied in the form of an impermeable black layer provided with a thin hydrophilic carpet on the rear part thereof. Saturated hot air at a temperature of 80 °C enters inside (56') hollow plates from bellow and exits from the top at a temperature of 50 °C. A high chimney (79') is provided with a monoblock heat exchanger (84') which is transversed by a non-potable water to be distilled which, afterwards is spread warm (40°C) over the hydrophilic coating (60'). During passage through the heat exchanger (84') the air is cooled to 30 °C and moved down by gravity to the inter-plate spaces (58') and exits therefrom at a temperature of 78 °C. The distilled water condensed in the plates and by the heat exchanger is collected and removed. Brine is received in the bottom of the inter-plate space and distributed along the thin hydrophilic carpet of the bottom (122') of the greenhouse. An air current passes along said hot carpet is heated and saturated and enters the plates. The brine liquor finally flows in an air-preheating tank (63') which is emptied each morning. The greenhouse can be substituted by a heating tube transversed by a heating fluid or associated with another steam-jet tube. The more powerful chamber-ovens can produce at least 200 m3/day of distilled water for collective consumption. Said invention can be used for salt removal from seawater, co-generating electricity and potable water and for producing food concentrates.
    • 9. 发明公开
    • WATER EVAPORATION APPARATUS
    • DEVICE蒸发水的
    • EP1017629A4
    • 2000-12-27
    • EP98925327
    • 1998-06-05
    • AQUAJET TECH LTD
    • GODDARD FENTON
    • B01D1/02B01D1/30B01D3/42C02F1/04
    • B01D1/0005B01D1/30B01D3/42C02F1/04C02F2209/42
    • A water evaporation apparatus (10) for evaporating water (12) contained in a drum (14) includes a thermally insulated float assembly (16) for floating in the water (12). The float assembly defines a space (18) which is in fluid communication with the water (12) via a hole (22) formed through a bottom wall (24) of the float assembly (16). The float assembly (16) also includes an exhaust stack (26) which extends from the space (18) and has a discharge end (28) located outside the drum (14). A volume of water (20) flows into space (18) through the hole (22). A heater (30) is located within the space (18) and below the level of the water (20) for causing evaporation thereof. This generates steam and other vapours which rise through the stack (26) and are vented through discharge end (28). As the water (20) is evaporated it is replenished by water (12) from the drum (14) flowing through the hole (22) into the space (18). In this way, the water (12) within the drum (14) is progressively evaporated. When the water level within the drum (14) drops to a lowest level (L) a switch (68) is operated by a stop (70) mounted on the stack (26) to cover power to the heater (30).