CN108645116A - 一种带盘管蓄冷器的液化空气储能系统 - Google Patents

一种带盘管蓄冷器的液化空气储能系统 Download PDF

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CN108645116A
CN108645116A CN201810315702.7A CN201810315702A CN108645116A CN 108645116 A CN108645116 A CN 108645116A CN 201810315702 A CN201810315702 A CN 201810315702A CN 108645116 A CN108645116 A CN 108645116A
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air
regenerator
liquefied
storage
cold
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CN108645116B (zh
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苏苗印
汪慧
刘志
谢海龙
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HANGZHOU HANGYANG CHEMICAL AND PHARMACEUTICAL ENGINEERING CO LTD
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HANGZHOU HANGYANG CHEMICAL AND PHARMACEUTICAL ENGINEERING CO LTD
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0221Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using the cold stored in an external cryogenic component in an open refrigeration loop
    • F25J1/0222Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using the cold stored in an external cryogenic component in an open refrigeration loop in combination with an intermediate heat exchange fluid between the cryogenic component and the fluid to be liquefied
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    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0201Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using only internal refrigeration means, i.e. without external refrigeration
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    • F01DNON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
    • F01D15/00Adaptations of machines or engines for special use; Combinations of engines with devices driven thereby
    • F01D15/10Adaptations for driving, or combinations with, electric generators
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    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K7/00Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating
    • F01K7/02Steam engine plants characterised by the use of specific types of engine; Plants or engines characterised by their use of special steam systems, cycles or processes; Control means specially adapted for such systems, cycles or processes; Use of withdrawn or exhaust steam for feed-water heating the engines being of multiple-expansion type
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  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
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  • Filling Or Discharging Of Gas Storage Vessels (AREA)
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Abstract

本发明公开了一种带盘管蓄冷器的液化空气储能系统,它包括空气压缩及液化储存机构、液化空气加热气化及蓄冷机构和空气加热膨胀及发电机构。本发明采用盘管蓄冷器同时作为空气液化系统的换热装置和冷能储存系统的蓄冷装置,即系统工作在冷能蓄积时,液化冷量通过蓄冷器的盘管蓄积在蓄冷器填料中;系统工作在冷能释放时,压缩空气经过蓄冷器填料获得冷量而被冷却。该系统有效整合液化环节和蓄冷环节,克服了传统液化储能工艺流程独立设置液化盘管蓄冷器和蓄冷器的缺点,从而简化了工艺流程,提高了系统热效率,减小了占地面积,并降低了工程费用。

Description

一种带盘管蓄冷器的液化空气储能系统
技术领域
本发明涉及液化空气的储能技术领域,具体涉及一种带盘管蓄冷器的液化空气储能系统。
背景技术
在能源供需矛盾日益突出的背景下,人们逐渐加大对绿色可再生能源如光能、风能和水能等领域的开发和利用。然而可再生能源具有随机性和间歇性等缺点,接入时会对电网产生冲击,甚至会引发大规模恶性事故。储能技术是实现可再生能源大规模接入、电力系统削峰填谷,以及分布式供能系统的关键技术,是目前实现可再生能源安全稳定的一个解决方案。液化空气储能不受场地限制,具有储能密度高和容量大等优点,是压缩空气能技术的发展趋势。
现有液化空气储能系统工艺主流程为,空气液化时,利用板式主盘管蓄冷器冷却压缩空气,冷量来自储存在蓄冷器的冷能介质;蓄冷时,冷能介质从液空汽化器获取冷量后传递给蓄冷器实现暂时储存。液化环节和蓄冷环节交替工作,实现一个周期内完整的传热循环。
目前的液化单元和蓄冷单元的工艺系统虽为成熟技术,但独立设置板式主换热和蓄冷器造成功能上的重复,且单元之间的联动操作较为复杂,冷能介质通过多次换热导致冷量损失很大,设备费用和占地面积都非常大。
发明内容
本发明主要解决的技术问题是提供一种带盘管蓄冷器的液化空气储能系统,克服传统液化储能工艺流程独立设置液化盘管蓄冷器和蓄冷器的缺点。
所述的一种带盘管蓄冷器的液化空气储能系统,其特征在于包括空气压缩及液化储存机构、液化空气加热气化及蓄冷机构和空气加热膨胀及发电机构,其中:
所述空气压缩及液化储存机构包括依次连接的空气过滤器和空气压缩机,空气压缩机出气口连接空气冷却塔的底部进气口:空气冷却塔顶部出口连接吸附器进气口,吸附器出气口通过膨胀增压机增压冷却后连接蓄冷器,蓄冷器出气口通过气液分离器连接液空贮槽,将液化空气储存在液空贮槽中,空气冷却塔上设有冷却水系统,吸附器上设有加热器;
所述液化空气加热气化及蓄冷机构包括蓄冷器、液空贮槽、汽化器及循环风机,冷媒介质通过循环风机驱动形成闭式循环,液空贮槽出料口经液空泵连接汽化器进料口,蓄冷器、循环风机及汽化器连接构成循环体系,冷媒介质经过汽化器获取液化空气汽化释放的冷量后进入蓄冷器并储存蓄冷器的填料中,待空气压缩及液化储存机构工作时,冷媒介质的冷量传递给纯化空气复热后回到循环风机中,蓄冷器顶部出口连接换热器;
所述空气加热膨胀及发电机构包括与汽化器依次连接的加热器和膨胀发电机单元,膨胀发电机单元出口端分三路,一路连接放空口,一路连接冷却水系统,一路连接换热器,液化空气从液空贮槽经液空泵加压并经过汽化器蒸发后成为高压气态空气,高压空气通过膨胀发电机单元入口前经加热器加温后进行多级膨胀,膨胀发电机单元通过输出轴带动发电机高速转动输出电能。
所述的一种带盘管蓄冷器的液化空气储能系统,其特征在于冷却水系统包括水冷却塔,水冷却塔侧面进口连接膨胀发电机单元一个出口,水冷却塔上部进水口与冷却水槽一个出水口连接,水冷却塔底部出水口通过冷冻水泵连接空气冷却塔上部,冷却水槽另一个出水口通过冷却水泵连接空气冷却塔中部,冷却水与冷冻水分别从空气冷却塔中部、上部进入,对空气进行冷却。
所述的一种带盘管蓄冷器的液化空气储能系统,其特征在于蓄冷器为盘管式蓄冷器,由若干台并联或串联工作,满足冷却周期内的蓄冷和加热周期的换热要求。
所述的一种带盘管蓄冷器的液化空气储能系统,其特征在于蓄冷器的管道进出口设置温度探头和差压探头;蓄冷器中部设有空气出口,所述空气出口通过管道连接膨胀增压机,用于经蓄冷器中部抽出部分空气去膨胀增压机。
所述的一种带盘管蓄冷器的液化空气储能系统,其特在于所述吸附器与膨胀增压机之间设有高压压缩机。
所述的一种带盘管蓄冷器的液化空气储能系统,所述蓄冷器内的填料为石头、铝带或高分子材料。
所述的一种带盘管蓄冷器的液化空气储能系统,所述蓄冷器的填料内部嵌入多根蛇管,利于为多股换热介质提供换热通道,所述蛇管材料为铜管、铝管或不锈钢管。
所述的一种带盘管蓄冷器的液化空气储能系统,所述蓄冷器的进出口管道接头处设有过滤网,保护蓄冷器的筒口不被堵塞;所述蓄冷器采用真空粉末绝热,外真空夹层充填珠光砂。
所述的一种带盘管蓄冷器的液化空气储能系统,膨胀发电机单元采用四级膨胀机串联工作,相邻两级膨胀机之间设有余热加热器,每级膨胀机出口的空气通过余热加热器加温至120℃后再进入下一级膨胀机。
所述的一种带盘管蓄冷器的液化空气储能系统,所述吸附器为两台,且并联设置,交替工作。
通过采用上述技术,与现有技术相比,本发明的有益效果如下:
本发明提供的一种带盘管蓄冷器的液化空气储能系统,将空气压缩及液化储存机构、液化空气加热气化及蓄冷机构和空气加热膨胀及发电机构相互配合使用,使得液化空气储能系统中液化单元的换热设备和蓄冷单元的蓄冷设备合二为一,简化了设备,且联动操作简便,从而简化了工艺流程;另外,换热设备的整合有利于提高系统热效率,将冷能介质的冷量重复利用,不但减小工程占地面积,减少了设备费用,而且大大降低工程费用,提高了经济效益。
附图说明
图1是本发明一种带盘管蓄冷器的液化空气储能系统工艺流程示意图;
图2是本发明的蓄冷器工作流程示意图。
图中:1、空气过滤器;2、空气压缩机;3、空气冷却塔;4、冷却水系统,401、水冷却塔,402、冷却水槽,403、冷冻水泵,404、冷却水泵;5、分子筛吸附器;6、高压压缩机;7、后冷却器;8、蓄冷器;9、气液分离器;10、液空泵;11、液空贮槽;12、汽化器;13、循环风机;14、膨胀发电机单元;15、换热器;16、放空口;17、加热器;18、余热加热器;19、低温节流阀;
a、第一阀门;b、第二阀门;c、第三阀门;d、第四阀门;e、第五阀门e;f、第六阀门;g、第七阀门。
具体实施方式
下面结合说明书附图对本发明的较佳实施例进行详细阐述,以使本发明的优点和特征能更易于被本领域技术人员理解,从而对本发明的保护范围做出更为清楚明确的界定。
如图1和图2所示,本发明的一种带盘管蓄冷器的液化空气储能系统,包括空气压缩及液化储存机构、液化空气加热气化及蓄冷机构和空气加热膨胀及发电机构,其中:
所述空气压缩及液化储存机构包括依次连接的空气过滤器1和空气压缩机2,空气压缩机2出气口连接空气冷却塔3的底部进气口:空气冷却塔3顶部出口连接吸附器5进气口,吸附器5出气口通过高压压缩机6和膨胀增压机7增压冷却后连接蓄冷器8,蓄冷器8出气口通过气液分离器9连接液空贮槽11,将液化空气储存在液空贮槽11中,空气冷却塔3上设有冷却水系统4,吸附器5上设有加热器15,冷却水系统4包括水冷却塔401,水冷却塔401侧面进口连接膨胀发电机单元14一个出口,水冷却塔401上部进水口与冷却水槽402一个出水口连接,水冷却塔401底部出水口通过冷冻水泵403连接空气冷却塔3上部,冷却水槽402另一个出水口通过冷却水泵404连接空气冷却塔3中部,冷却水与冷冻水分别从空气冷却塔3中部、上部进入,对空气进行冷却;
所述液化空气加热气化及蓄冷机构包括蓄冷器8、液空贮槽11、汽化器12及循环风机13,冷媒介质通过循环风机13驱动形成闭式循环,液空贮槽11出料口经液空泵10连接汽化器12进料口,蓄冷器8、循环风机13及汽化器12连接构成循环体系,冷媒介质经过汽化器12获取液化空气汽化释放的冷量后进入蓄冷器8并储存蓄冷器8的填料中,待空气压缩及液化储存机构工作时,冷媒介质的冷量传递给纯化空气复热后回到循环风机13中,蓄冷器8顶部出口连接分子筛纯化系统15;
所述空气加热膨胀及发电机构包括与汽化器12依次连接的加热器17和膨胀发电机单元14,膨胀发电机单元14出口端分三路,一路连接放空口16,一路连接冷却水系统,一路连接分子筛纯化系统15,液化空气从液空贮槽11经液空泵10加压并经过汽化器12蒸发后成为高压气态空气,高压空气通过膨胀发电机单元14入口前经加热器17加温后进行多级膨胀,膨胀发电机单元14通过输出轴带动发电机高速转动输出电能。
本发明的空气过滤器1为自洁式空气过滤器,所采用的蓄冷器8为盘管式蓄冷器,为了提高其畜冷效果,本发明采用若干台蓄冷器8并联或串联工作,用于满足冷却周期内的蓄冷和加热周期的换热要求,每台蓄冷器8的管道进出口设置温度探头和差压探头,蓄冷器8中部设有空气出口,所述空气出口通过管道连接膨胀增压机7,用于经蓄冷器8中部抽出部分空气去膨胀增压机7,冷却后进入气液分离器9;且蓄冷器8采用真空粉末绝热,外真空夹层充填珠光砂。
本发明蓄冷器8内的填料为石头、铝带或高分子材料,为了便于多股换热介质提供换热通道,本发明在蓄冷器8的填料内部嵌入多根蛇管,利于为所述蛇管材料为铜管、铝管或不锈钢管。
为了提高其使用寿命,本发明在蓄冷器8的进出口管道接头处设有过滤网,保护蓄冷器8的筒口不被堵塞;
本发明实施例中的吸附器5为两台,且并联设置,所述吸附器5为两只切换使用,其中一只工作时,另一只再生,定时自动切换;保正交替连续工作。
实施例1 本发明实结合实施例具体阐释一种带盘管蓄冷器的液化空气储能系统流程工艺的原理。
常压原料空气经空气过滤器1除去灰尘和机械杂质后进入空气压缩机2加压至0.8Mpa,完成压缩后的105℃高温空气送入空气冷却塔3,由冷却水系统4中的冷却水槽402的水经冷却水泵404进入空气冷却塔3进行清洗,同时冷却水槽402中部分水进入水冷却塔401冷冻后通过冷冻水泵403进入空气冷却塔3对空气进行冷却,冷至20℃;
出空气冷却塔3的空气进入交替使用的吸附器5,空气中的二氧化碳、碳氢化合物和水分被吸附;净化后的空气进入膨胀增压机7的增压端增压至1.0Mpa,经膨胀增压机7的后冷却器冷却至常温后进入蓄冷器8;
进蓄冷器8的空气被分成两股,一股约30-40%的空气量从蓄冷器8中部抽出进入膨胀增压机7的膨胀端,预冷后-140℃的低温空气降至-170℃进入气液分离器9,另一股空气出蓄冷器8后经低温节流阀19至-172℃送入气液分离器9,进行分离,气液分离器9上部气体返回去蓄冷器8,冷凝后的液空输送至液空贮槽11中暂时储存,待膨胀发电14工作时,液空被液空泵10增压至10Mpa后得到高压常温气体输入汽化器12完成蒸发气化;
高压常温气体从汽化器12出来后经加热器17加温至120℃,再进入膨胀发电机单元14实现膨胀发电,为了充分利用输入系统的余热,每级膨胀机出口空气通过余热加热器18上的余热加温至120℃后再进入下一级膨胀机。
如图所示,本发明的膨胀发电机单元14工作时,蓄冷环节同时工作,所述冷媒介质选用0.7MPa的压缩空气。
循环风机13带动压缩空气实现闭式循环,常温空气获取气化器12低温液体蒸发冷量后冷却至-160℃得到低温空气,低温空气进入蓄冷器8将冷量传递给填料并暂时储存。
本实施例中蓄冷器8工作温度为-155℃,待下一个周期液化环节工作时,填料中的冷量被利用。
如图2所示,本发明的蓄冷器8工作流程如下:
液化系统工作时,第一阀门a、第二阀门b、第四阀门d、第五阀门e及第七阀门g处于打开状态,第三阀门c,第六阀门f处于关闭状态,压缩空气通过第一阀门a进入蓄冷器8被冷却,一股低温的中抽空气出第四阀门d进入膨胀增压机7,另一股低温空气通过第五阀门e去低温节流阀19。气液分离器9的低温回气通过第七阀门g去蓄冷器8回收冷量,常温回气从第二阀门b出去后作为吹扫气分两路,一路经加热器15后进入吸附器5,另一路经进入水冷却塔4。
如图所示,蓄冷系统或发电系统工作时,第三阀门c、第六阀门f处于打开状态,第一阀门a、第二阀门b、第四阀门d、第五阀门e及第七阀门g处于关闭状态,冷媒介质从汽化器12获取冷量后通过第六阀门f进入蓄冷器8储存冷量,常温冷媒由循环风机13驱动下从第三阀门c进入汽化器12,从而实现闭式循环。
以上所述仅为本发明的实施例,并非因此限制本发明的专利范围,凡是利用本发明说明书及附图内容所作的等效结构或等效流程变换,或直接或间接运用在其他相关的技术领域,均同理包括在本发明的专利保护范围内。

Claims (10)

1.一种带盘管蓄冷器的液化空气储能系统,其特征在于包括空气压缩及液化储存机构、液化空气加热气化及蓄冷机构和空气加热膨胀及发电机构,其中:
所述空气压缩及液化储存机构包括依次连接的空气过滤器(1)和空气压缩机(2),空气压缩机(2)出气口连接空气冷却塔(3)的底部进气口:空气冷却塔(3)顶部出口连接吸附器(5)进气口,吸附器(5)出气口通过膨胀增压机(7)增压冷却后连接蓄冷器(8),蓄冷器(8)出气口通过气液分离器(9)连接液空贮槽(11),将液化空气储存在液空贮槽(11)中,空气冷却塔(3)上设有冷却水系统(4),吸附器(5)上设有加热器(15);
所述液化空气加热气化及蓄冷机构包括蓄冷器(8)、液空贮槽(11)、汽化器(12)及循环风机(13),冷媒介质通过循环风机(13)驱动形成闭式循环,液空贮槽(11)出料口经液空泵(10)连接汽化器(12)进料口,蓄冷器(8)、循环风机(13)及汽化器(12)连接构成循环体系,冷媒介质经过汽化器(12)获取液化空气汽化释放的冷量后进入蓄冷器(8)并储存蓄冷器(8)的填料中,待空气压缩及液化储存机构工作时,冷媒介质的冷量传递给纯化空气复热后回到循环风机(13)中,蓄冷器(8)顶部出口连接换热器(15);
所述空气加热膨胀及发电机构包括与汽化器(12)依次连接的加热器(17)和膨胀发电机单元(14),膨胀发电机单元(14)出口端分三路,一路连接放空口(16),一路连接冷却水系统,一路连接换热器(15),液化空气从液空贮槽(11)经液空泵(10)加压并经过汽化器(12)蒸发后成为高压气态空气,高压空气通过膨胀发电机单元(14)入口前经加热器(17)加温后进行多级膨胀,膨胀发电机单元(14)通过输出轴带动发电机高速转动输出电能。
2.根据权利要求1所述的一种带盘管蓄冷器的液化空气储能系统,其特征在于冷却水系统(4)包括水冷却塔(401),水冷却塔(401)侧面进口连接膨胀发电机单元(14)一个出口,水冷却塔(401)上部进水口与冷却水槽(402)一个出水口连接,水冷却塔(401)底部出水口通过冷冻水泵(403)连接空气冷却塔(3)上部,冷却水槽(402)另一个出水口通过冷却水泵(404)连接空气冷却塔(3)中部,冷却水与冷冻水分别从空气冷却塔(3)中部、上部进入,对空气进行冷却。
3.根据权利要求1所述的一种带盘管蓄冷器的液化空气储能系统,其特征在于蓄冷器(8)为盘管式蓄冷器,由若干台并联或串联工作,满足冷却周期内的蓄冷和加热周期的换热要求。
4.根据权利要求1所述的一种带盘管蓄冷器的液化空气储能系统,其特征在于蓄冷器(8)的管道进出口设置温度探头和差压探头;蓄冷器(8)中部设有空气出口,所述空气出口通过管道连接膨胀增压机(7),用于经蓄冷器(8)中部抽出部分空气去膨胀增压机(7)。
5.根据权利要求1所述的一种带盘管蓄冷器的液化空气储能系统,其特在于所述吸附器(5)与膨胀增压机(7)之间设有高压压缩机(6)。
6.根据权利要求1所述的一种带盘管蓄冷器的液化空气储能系统,所述蓄冷器(8)内的填料为石头、铝带或高分子材料。
7.根据权利要求6所述的一种带盘管蓄冷器的液化空气储能系统,所述蓄冷器(8)的填料内部嵌入多根蛇管,利于为多股换热介质提供换热通道,所述蛇管材料为铜管、铝管或不锈钢管。
8.根据权利要求1所述的一种带盘管蓄冷器的液化空气储能系统,所述蓄冷器(8)的进出口管道接头处设有过滤网,保护蓄冷器(8)的筒口不被堵塞;所述蓄冷器(8)采用真空粉末绝热,外真空夹层充填珠光砂。
9.根据权利要求1-8任一所述的一种带盘管蓄冷器的液化空气储能系统,膨胀发电机单元(14)采用四级膨胀机串联工作,相邻两级膨胀机之间设有余热加热器(18),每级膨胀机出口的空气通过余热加热器(18)加温至120℃后再进入下一级膨胀机。
10.根据权利要求1-8任一所述的一种带盘管蓄冷器的液化空气储能系统,所述吸附器(5)为两台,且并联设置,交替工作。
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