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    • 1. 发明申请
    • SYSTEM OF A DESALINATION PLANT DRIVEN BY A SOLAR POWER PLANT
    • 由太阳能发电厂驱动的脱盐设备系统
    • WO2016001369A1
    • 2016-01-07
    • PCT/EP2015/065119
    • 2015-07-02
    • AALBORG CSP A/S
    • BUNDGAARD, SvanteNIELSEN, Per JørnJENSEN, Peter BadstueWENDELBOE, Palle
    • B01D1/00B01D3/06C02F1/14F24J2/04F28D20/00
    • C02F1/14B01D1/0035B01D3/065F03G6/067F28D20/0034Y02A20/128Y02A20/129Y02A20/142Y02A20/212Y02E10/46Y02E60/142Y02E70/30Y02P70/34
    • A system is disclosed comprising a Concentrating Solar Power (CSP) plant (1), a first thermal energy storage (TES1), and a desalination plant (18), the solar power plant (1) having a receiver part for heating a heat transfer fluid (6) by means of sunlight and a first heat transfer system with at least one heat exchanger (3, 10) arranged for transfer of thermal power from said first fluid to a first storage liquid being water for storage of said thermal power in the first thermal energy storage (TES1), the first thermal energy storage (TES1) being arranged to operate with the first storage liquid substantially at atmospheric pressure and the volume of the first storage liquid contained in said first thermal energy storage (TES1) is in the range of 300 m 3 to 1,500 m 3 per megawatt [MW] nominal thermal capacity of said receiver part, and the desalination plant (18) being arranged to desalinate seawater (22) driven by thermal power provided from the first thermal energy storage (TES1) in order to produce a flow of fresh water (23).
    • 公开了一种包括集中太阳能发电(CSP)工厂(1),第一热能储存(TES1)和淡化设备(18)的系统,太阳能发电厂(1)具有用于加热传热 流体(6)和具有至少一个热交换器(3,10)的第一传热系统,所述热交换器设置成用于将热功率从所述第一流体转移到作为水的第一储存液体,以将所述热力储存在 第一热能存储器(TES1),第一热能储存器(TES1)被布置成基本上处于大气压下与第一储存液体一起操作,并且包含在所述第一热能储存器(TES1)中的第一储存液体的容积在 所述接收器部件的标称热容量为300m 3至1,500m 3 / m 3,并且所述脱盐设备(18)被布置为使由所述第一热能存储器(TES1)提供的热功率驱动的海水(22)脱盐 要么 以产生淡水流(23)。
    • 3. 发明申请
    • HEAT EXCHANGER WITH PIPE BUNDLE
    • WO2020253924A1
    • 2020-12-24
    • PCT/DK2020/050170
    • 2020-06-15
    • AALBORG CSP A/S
    • THOMSEN, PeterCHRISTENSEN, Ivan BoPELLE, Jens TaggartSØRENSEN, KeldBUNDGAARD, Svante
    • F28D1/047F28D1/02F22B1/00F22B15/00F28D7/08F28D20/00F28D21/00
    • A heat exchanger (10) is disclosed for providing heat exchange between fluids (24, 25), comprising a pipe bundle (17) extending between first and second pipe connectors (13, 14) and configured to guide a second fluid (25) between the first and second pipe connectors (13, 14), the pipes (17a-17n) being distributed in layers (22) of pipes (17a-17n), wherein a plurality of pipes (17a-17n) of each of said layers (22) of pipes each comprises two bends (B1, B2), so that the respective pipe provides three substantially parallel flow path sections (S1, S2, S3), wherein the length (L1) of a longer (S1) of said flow path sections of the respective pipe is at least 1.7 times greater than the length (L2) of the other two shorter flow path sections (S2, S3) of said pipe, wherein a first (B1) of said bends (B1, B2) is provided between the longer flow path section (S1) and a first of said shorter flow path section (S2), and wherein the other (B2) of said bends is provided between said first, shorter flow path section (S2) and the other shorter flow path section (S3), wherein each of said layers of pipes (17a-17n) comprises two pipe subgroups (SG1, SG2), wherein the longer (S1) of said flow path sections of one of said subgroups (SG1, SG2) is connected to a first of said pipe connectors (13, 14), and wherein the longer (S1) of said flow path sections of the other of said subgroups (SG1, SG2) is connected to the other of said pipe connectors (13, 14), and wherein the bend (B2) between the two shorter flow path sections (S2, S3) of the respective pipes in one of said pipe subgroups (SG1) in the pipe layer (22) is arranged substantially opposite to bends (B2) extending between the two shorter flow path sections (S2, S3) of pipes in the other pipe subgroup (SG2) of the same pipe layer (22).