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    • 5. 发明授权
    • Method and apparatus for simultaneous heat and mass transfer utilizing a carrier-gas
    • 使用载气同时传热传质的方法和装置
    • US06911121B1
    • 2005-06-28
    • US10031534
    • 2000-07-26
    • James R. Beckman
    • James R. Beckman
    • B01D1/22B01D3/34B01D3/42C02F1/04
    • B01D1/22B01D3/346B01D3/42Y02W10/37Y10S165/162Y10S165/914
    • The present application is directed to a continuous contacting apparatus for separating a liquid component from a liquid mixture. The apparatus comprises: (i) an evaporation chamber (15) having first and second ends, an inlet (50) and an outlet (55) for a carrier gas, and an inlet (30) and an outlet (40) for a liquid mixture, wherein the inlet (30) for the liquid mixture and the outlet (55) of the carrier gas are located on the first end of the evaporation chamber (15); (ii) a dew-formation chamber (20) having an inlet (60) and an outlet (65) for a carrier gas and an outlet for the separable liquid component (80), wherein the inlet for the carrier gas (60) of the dew-formation chamber (20) is situated in a countercurrent manner to the inlet for the carrier gas of the evaporation chamber; (iii) a common heat transfer wall (10) providing thermal communication between the evaporation chamber (15) and the dew-formation chamber (20); (iv) a feeding device for providing the liquid mixture onto the evaporation side of the heat transfer wall; (v) an air mover for controlling a flow of a carrier gas through the chambers, wherein the gas flow in the evaporation chamber is countercurrent to the gas flow in the dew-formation chamber; and (vi) a heating apparatus for heating the carrier gas from the outlet of the evaporation chamber, wherein the heated carrier gas is directed to flow into the inlet of the dew-formation chamber. Also described is a process for separating a liquid component from a liquid mixture in a continuous contacting manner comprising employing such an apparatus for such separation.
    • 本申请涉及用于从液体混合物中分离液体组分的连续接触装置。 该设备包括:(i)具有第一和第二端的蒸发室(15),用于载气的入口(50)和出口(55),以及用于液体的入口(30)和出口(40) 混合物,其中用于液体混合物的入口(30)和载气的出口(55)位于蒸发室(15)的第一端上; (ii)具有用于载气的入口(60)和出口(65)和用于可分离液体组分(80)的出口的露水室(20),其中用于载气(60)的入口 露水室(20)以与蒸发室的载气的入口逆流的方式设置; (iii)在蒸发室(15)和露水形成室(20)之间提供热连通的公共传热壁(10); (iv)用于将液体混合物提供到传热壁的蒸发侧的进料装置; (v)用于控制通过所述室的载气流动的鼓风机,其中所述蒸发室中的气流与所述露水室中的气流逆流; 和(vi)用于从蒸发室的出口加热载气的加热装置,其中加热的载气被引导流入露水室的入口。 还描述了一种以连续接触方式从液体混合物中分离液体组分的方法,包括采用这种用于这种分离的装置。
    • 6. 发明授权
    • Apparatus for producing power using concentrated brine
    • 使用浓缩盐水生产电力的设备
    • US4704993A
    • 1987-11-10
    • US894902
    • 1986-08-08
    • Gad Assaf
    • Gad Assaf
    • B01D1/22B01D5/00F01K9/00F01K19/10F01K25/06F22B1/00F22B1/20
    • F01K9/00B01D1/22B01D5/0012B01D5/0039B01D5/0045F01K19/10F01K25/065F22B1/00Y10S165/914
    • A power plant includes a source of water, a heat exchanger having an evaporator side maintained below atmospheric pressure for converting the water to steam, and a turbine responsive to said steam for producing work and heat depleted steam. The heat exchanger also has a condenser side for receiving and condensing the heat depleted steam. The evaporator side of the heat exchanger is separated by a barrier from the condenser side. Concentrated brine from a source thereof is caused to fall in a film on the condenser side of the barrier, and water from the water source is caused to fall in a film on the evaporator side of the barrier. The heat of dilution of the film of concentrated brine, as it is directly contacted by the heat depleted steam in the condenser side of the heat exchanger, is transferred through the barrier from the condenser side to the evaporator side raising the temperature of the film of water on the evaporator side which evaporates in the reduced pressure in the evaporator. The cooled and diluted brine withdrawn from the condenser is reconcentrated in a constant enthalpy brine evaporator.
    • 发电厂包括水源,具有蒸发器侧保持低于大气压以将水转换成蒸汽的热交换器,以及响应于所述蒸汽产生工作和热耗尽蒸汽的涡轮机。 热交换器还具有用于接收和冷凝耗尽热量的蒸汽的冷凝器侧。 热交换器的蒸发器侧与冷凝器侧隔开隔离。 使来自其源的浓缩盐水落在阻挡层的冷凝器侧的膜中,使来自水源的水落在阻挡层的蒸发器侧的膜上。 浓缩的盐水的薄膜的稀释热由于热交换器的冷凝器侧的热耗尽蒸汽直接接触,通过阻挡层从冷凝器侧传递到蒸发器侧,从而提高膜的温度 蒸发器侧的水在蒸发器中减压蒸发。 从冷凝器中取出的冷却和稀释的盐水在恒定的焓盐水蒸发器中再浓缩。
    • 7. 发明申请
    • LIQUID DISTRIBUTOR FOR EVAPORATOR
    • 蒸发器用液体分配器
    • WO1997007867A1
    • 1997-03-06
    • PCT/FI1996000449
    • 1996-08-21
    • HADWACO LTD OYRAMM-SCHMIDT, LeifTIAINEN, VeliKOISTINEN, PeterERIKSSON, Hemmo
    • HADWACO LTD OY
    • B01D01/30
    • F28F9/028B01D1/22B01D3/008B01F5/0601B01F15/0264D21C11/10Y10S165/914
    • The invention relates to a liquid distributor for an evaporator, particularly meant for a film evaporator treating liquid suspensions containing solids. The distributor comprises a channel array (3, 4) that distributes the liquid (8) fed in at the sides of the evaporator to the top of the heat transfer surface (5), over the whole width thereof. The channel array is formed of at least one transversal supply channel (3) and of a number of distribution channels (4) departing downwards from the supply channel and leading to the heat transfer surface (5). The invention is characterized in that each distribution channel (4) is provided, on its side located downstream with respect to the supply channel flow (8, 11), with a step-shaped expansion (14) bordered by a sharp point (15), the purpose of said expansion being to prevent liquid suction created in the channel due to the effect of siphonage. The junctions (9) of the supply channel (3) and the distribution channels (4) can be provided with rounded division surfaces (12), on which the liquid is distributed into the channels at each instant, and under which the step-shaped expansions (14) start.
    • 本发明涉及一种用于蒸发器的液体分配器,特别适用于处理含有固体的液体悬浮液的薄膜蒸发器。 分配器包括通道阵列(3,4),其将在蒸发器侧面馈送的液体(8)在整个宽度上分配到传热表面(5)的顶部。 通道阵列由至少一个横向供应通道(3)和多个分配通道(4)形成,分配通道(4)从供应通道向下离开并通向传热表面(5)。 本发明的特征在于,每个分配通道(4)在其相对于供应通道流(8,11)的下游侧设置有由尖锐点(15)界定的阶梯形膨胀(14) 所述膨胀的目的是为了防止由于虹吸效应而在通道中产生的液体吸入。 供应通道(3)和分配通道(4)的接头(9)可以设置有圆形分隔表面(12),液体在每个时刻分配到通道中,在其下方形成阶梯形 扩展(14)开始。