[go: up one dir, main page]

CN102062507B - Flow ice making method and device based on lithium bromide absorption type refrigeration cycle - Google Patents

Flow ice making method and device based on lithium bromide absorption type refrigeration cycle Download PDF

Info

Publication number
CN102062507B
CN102062507B CN2011100237371A CN201110023737A CN102062507B CN 102062507 B CN102062507 B CN 102062507B CN 2011100237371 A CN2011100237371 A CN 2011100237371A CN 201110023737 A CN201110023737 A CN 201110023737A CN 102062507 B CN102062507 B CN 102062507B
Authority
CN
China
Prior art keywords
ice
water
evaporative
solution
freezing chamber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2011100237371A
Other languages
Chinese (zh)
Other versions
CN102062507A (en
Inventor
殷勇高
杜垲
张小松
査翔
张朋磊
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Southeast University
Original Assignee
Southeast University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Southeast University filed Critical Southeast University
Priority to CN2011100237371A priority Critical patent/CN102062507B/en
Publication of CN102062507A publication Critical patent/CN102062507A/en
Application granted granted Critical
Publication of CN102062507B publication Critical patent/CN102062507B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Abstract

本发明是利用溴化锂浓溶液在吸收器中不断吸收水蒸气,造成蒸发蒸发冷冻室的低压环境,使水在蒸发蒸发冷冻室的低压环境下不断蒸发吸收自身热量而部分冷冻结成流态冰。溴化锂溶液在吸收器中吸收来自蒸发蒸发冷冻室中的水蒸气被稀释后,通过溶液泵送到发生器中被加热再生,溶液浓度得到提升,重新具有吸湿能力,然后经过冷却送至吸收器,构成溶液吸收—再生往复循环。来自发生器的水蒸气在冷凝器中冷凝成过冷水,经过节流后送至蒸发冷冻室制冰。制冰系统由水箱根据蒸发冷冻室水位的高低自动补充。

Figure 201110023737

The invention utilizes concentrated lithium bromide solution to continuously absorb water vapor in the absorber to form a low-pressure environment in the evaporative freezing chamber, so that the water continuously evaporates and absorbs its own heat in the low-pressure environment of the evaporative freezing chamber, and partially freezes to form liquid ice. After the lithium bromide solution absorbs the water vapor from the evaporative freezer in the absorber and is diluted, it is pumped to the generator to be heated and regenerated. The concentration of the solution is increased, and it has moisture absorption capacity again, and then it is cooled and sent to the absorber. It constitutes a solution absorption-regeneration reciprocating cycle. The water vapor from the generator is condensed into supercooled water in the condenser, and then sent to the evaporative freezer to make ice after throttling. The ice making system is automatically replenished by the water tank according to the water level of the evaporative freezer.

Figure 201110023737

Description

基于溴化锂吸收式制冷循环的流态冰制取方法与装置Method and device for producing liquid ice based on lithium bromide absorption refrigeration cycle

技术领域 technical field

本发明涉及一种蒸发冷冻的制取流态冰新方法,是一种基于溴化锂溶液吸收式制冷循环的蒸发冷冻制取流态冰的方法和装置,属于热驱动制冷、制取流态冰的技术领域。 The present invention relates to a new method of producing liquid ice by evaporative freezing, which is a method and device for producing liquid ice by evaporative freezing based on lithium bromide solution absorption refrigeration cycle, and belongs to heat-driven refrigeration and liquid ice production. technology field.

背景技术 Background technique

随着能源紧张局面的凸现,制冷空调设备的广泛应用导致的空调系统能耗问题引起了当前社会的普遍关注,节能成为制冷领域内再新形势下的迫切要求,我国也提出可持续发展的建国战略。蓄冷作为一种节能和移峰填谷的重要手段,具有重要的实际意义和应用价值,其中冰蓄冷具有相变潜热大、成本低等优势受到重视。传统的冰蓄能存在着蒸发温度低、制取过程中存在传热温差大、制冷性能系数低等不足,流态冰以其良好的热物性以及流动特性成为冰蓄冷具有可观前景的应用形式,因此研究开发新型高效的制取流态冰的方法具有重要的意义。 With the emergence of energy shortages, the energy consumption of air-conditioning systems caused by the wide application of refrigeration and air-conditioning equipment has aroused widespread concern in the current society. Energy conservation has become an urgent requirement in the refrigeration field under the new situation. my country has also proposed the sustainable development of the country. strategy. As an important means of saving energy and shifting peaks and valleys, cold storage has important practical significance and application value. Among them, ice storage has the advantages of large latent heat of phase change and low cost. Traditional ice energy storage has disadvantages such as low evaporation temperature, large heat transfer temperature difference in the production process, and low refrigeration performance coefficient. Fluid ice has become a promising application form of ice storage due to its good thermophysical properties and flow characteristics. Therefore, it is of great significance to research and develop new and efficient methods for producing liquid ice.

发明内容 Contents of the invention

技术问题:本发明提供一种节能、结构简单、易行的基于溴化锂吸收式制冷循 Technical problem: The present invention provides a lithium bromide-based absorption refrigeration cycle with energy saving, simple structure and easy operation.

环的流态冰制取方法与装置。 Ring liquid ice preparation method and device.

技术方案:为解决上述技术问题,本发明提供的技术方案为: Technical solution: In order to solve the above technical problems, the technical solution provided by the invention is:

本发明的技术方案是将传统的溴化锂吸收式制冷循环中的蒸发器加以变化和改造成流态冰制取模块,并辅以辅助功能部件即可实现。 The technical solution of the invention is to change and transform the evaporator in the traditional lithium bromide absorption refrigeration cycle into a flow ice production module, and realize it with auxiliary functional components.

本发明的基于溴化锂吸收式制冷循环的流态冰制取装置由溶液循环回路和蒸发冷冻制冰模块组成;溶液循环回路包括发生器、吸收器、溶液热交换器、冷却器、第一溶液泵、第二溶液泵、冷剂水泵;其中,吸收器的下部的浓溶液区分别通过第一溶液泵、第二溶液泵和溶液热交换器接发生器的下部,冷却器的输入端通过溶液热交换器接发生器的下部,冷却器的输出端接位于吸收器上部的喷淋器; The liquid ice preparation device based on the lithium bromide absorption refrigeration cycle of the present invention is composed of a solution circulation loop and an evaporative freezing ice-making module; the solution circulation loop includes a generator, an absorber, a solution heat exchanger, a cooler, and a first solution pump , the second solution pump, and the refrigerant water pump; wherein, the concentrated solution area in the lower part of the absorber is connected to the lower part of the generator through the first solution pump, the second solution pump and the solution heat exchanger respectively, and the input end of the cooler passes through the solution heat The exchanger is connected to the lower part of the generator, and the output end of the cooler is connected to the sprinkler on the upper part of the absorber;

蒸发冷冻制冰模块由冷凝器、补水装置、节流阀、蒸发冷冻室、成冰装置、冰水分离装置、单向阀门、中间储冰器、单向阀门、储冰槽构成;冷凝器下部的浓溶液区通过节流阀接蒸发冷冻室,蒸发冷冻室的输出端顺序通过单向阀门、中间储冰器、单向阀门接储冰槽;冷却塔底部的输出端顺序通过水泵、吸收器、冷凝器回到冷却塔上部的输入端。 The evaporative freezing ice-making module consists of a condenser, a water supply device, a throttle valve, an evaporative freezing chamber, an ice forming device, an ice-water separation device, a one-way valve, an intermediate ice storage device, a one-way valve, and an ice storage tank; the lower part of the condenser The concentrated solution area of the cooling tower is connected to the evaporative freezing chamber through a throttle valve, and the output end of the evaporative freezing chamber is connected to the ice storage tank through a one-way valve, an intermediate ice storage device, and a one-way valve in sequence; the output end at the bottom of the cooling tower is sequentially passed through a water pump and an absorber , The condenser returns to the input end of the upper part of the cooling tower.

在蒸发冷冻室中,蒸发冷冻室下部的浓溶液区通过冷剂水泵连接位于蒸发冷冻室上部的喷淋器,在喷淋器下部设有成冰装置,在成冰装置的下部设有冰水分离装置。 In the evaporative freezing chamber, the concentrated solution area in the lower part of the evaporative freezing chamber is connected to the sprinkler located in the upper part of the evaporative freezing chamber through a refrigerant water pump, and an ice-forming device is installed in the lower part of the sprayer, and ice water is installed in the lower part of the ice-forming device. separation device.

本发明的基于溴化锂吸收式制冷循环的流态冰制取装置的制取流态冰的方法,为,吸收器的浓溶液通过溶液泵经过溶液热交换器送至发生器中,发生器中发生终了的稀溶液在发生器和吸收器间的差压作用下经溶液热交换器和冷却器进入吸收器,组成溶液循环回路;蒸发制冰流程中,补水装置向冷凝器补水,冷凝器的水经节流阀进入蒸发蒸发冷冻室,蒸发蒸发冷冻室中成冰装置上形成的冰水混合物经冰水分离装置、单向阀门、中间储冰室、单向阀门进入储冰槽完成制冰流程。 The method for producing fluid ice based on the fluid ice producing device of the lithium bromide absorption refrigeration cycle of the present invention is that the concentrated solution of the absorber is sent to the generator through the solution heat exchanger through the solution pump, and the The final dilute solution enters the absorber through the solution heat exchanger and cooler under the action of the differential pressure between the generator and the absorber to form a solution circulation loop; in the process of evaporative ice making, the water supply device supplies water to the condenser, and the water in the condenser It enters the evaporative freezing chamber through the throttle valve, and the ice-water mixture formed on the ice-forming device in the evaporative freezing chamber passes through the ice-water separation device, one-way valve, intermediate ice storage room, and one-way valve into the ice storage tank to complete the ice-making process .

该方法利用吸收器中的浓溶液吸收蒸发蒸发冷冻室中的蒸汽 ,为蒸发蒸发冷冻室制造低压环境,水在其中蒸发吸收自身热量,在成冰装置上生长成流态冰。 This method uses the concentrated solution in the absorber to absorb the steam in the evaporative freezing chamber to create a low-pressure environment for the evaporative freezing chamber, in which water evaporates and absorbs its own heat, and grows into liquid ice on the ice-forming device.

该方法的冰水分离过程是在成冰装置上形成的冰晶经冰水分离装置分离出来,中间储冰器中保持与蒸发蒸发冷冻室中相同压力,打开单向阀门进入中间储冰室,然后关闭单向阀门,打开单向阀门冰晶进入储冰槽,完成冰水分离过程;完成冰水分离之后,通过真空泵将中间储冰室抽真空。 The ice-water separation process of this method is that the ice crystals formed on the ice-forming device are separated by the ice-water separation device, the intermediate ice storage is kept at the same pressure as that in the evaporative freezing chamber, and the one-way valve is opened to enter the intermediate ice storage chamber, and then Close the one-way valve, open the one-way valve and the ice crystals enter the ice storage tank to complete the ice-water separation process; after the ice-water separation is completed, the intermediate ice storage chamber is evacuated by a vacuum pump.

有益效果:Beneficial effect:

1、此方法可以利用工业余热、太阳能等温度为100℃左右的热源作为发生器的驱动能源,节省了大量的电能,实现了能源利用的可持续性发展。 1. This method can use industrial waste heat, solar energy and other heat sources with a temperature of about 100 ℃ as the driving energy of the generator, which saves a lot of electric energy and realizes the sustainable development of energy utilization.

2、本装置可以直接由溴化锂吸收制冷装置改造而成,构造简单,运行稳定,可以克服机械抽气制造真空磨损大、噪声大、连续运行困难的缺点。 2. This device can be directly transformed from a lithium bromide absorption refrigeration device. It has a simple structure and stable operation, and can overcome the shortcomings of mechanical exhaust manufacturing vacuum wear, high noise, and difficulty in continuous operation.

3、本方法和装置为流态冰的制取提供了一种可行的方法与方案,只需要将技术已经很成熟的吸收式制冷装置加以改造和升级即可实现。 3. The method and device provide a feasible method and solution for producing liquid ice, which can be realized only by modifying and upgrading the absorption refrigeration device with mature technology.

附图说明 Description of drawings

图1是本发明的结构示意图; Fig. 1 is a structural representation of the present invention;

其中有:发生器1,冷凝器2,水箱3,节流阀4,蒸发冷冻室5,成冰装置6,冰水分离器7,中间储冰器8,储冰槽9,吸收器10,溶液热交换器11,第一单向阀门12、第二单向阀门13,冷却塔14,冷却器15,第一溶液泵16、第二溶液泵17、冷剂水泵18,水泵19,真空泵20,热源加热流体21,补水节流阀22。 Among them: generator 1, condenser 2, water tank 3, throttle valve 4, evaporative freezing chamber 5, ice forming device 6, ice-water separator 7, intermediate ice storage device 8, ice storage tank 9, absorber 10, Solution heat exchanger 11, first one-way valve 12, second one-way valve 13, cooling tower 14, cooler 15, first solution pump 16, second solution pump 17, refrigerant water pump 18, water pump 19, vacuum pump 20 , the heat source heats the fluid 21, and the water replenishment throttle valve 22.

具体实施方式 Detailed ways

该装置由溶液循环回路和蒸发冷冻制冰模块组成;溶液循环回路包括发生器1、吸收器10、溶液热交换器11、冷却器15、第一溶液泵16、第二溶液泵17、冷剂水泵18;蒸发冷冻制冰模块由冷凝器2、补水装置3、节流阀4、蒸发冷冻室5、连接补水装置3与蒸发冷冻室5的补水节流阀22、成冰装置6、冰水分离装置7、单向阀门12、中间储冰器8、单向阀门13、储冰槽9构成;冷凝器2中的冷凝水通过节流阀4接蒸发冷冻室5,蒸发冷冻室5的输出端顺序通过单向阀门12、中间储冰器8、单向阀门13接储冰槽9。 The device consists of a solution circulation loop and an evaporative freezing ice-making module; the solution circulation loop includes a generator 1, an absorber 10, a solution heat exchanger 11, a cooler 15, a first solution pump 16, a second solution pump 17, a refrigerant Water pump 18; evaporative freezing ice-making module consists of condenser 2, water supply device 3, throttle valve 4, evaporative freezing chamber 5, water supply throttle valve 22 connecting water replenishing device 3 and evaporative freezing chamber 5, ice forming device 6, ice water Separation device 7, one-way valve 12, intermediate ice storage 8, one-way valve 13, and ice storage tank 9; the condensed water in condenser 2 is connected to evaporative freezing chamber 5 through throttle valve 4, and the output of evaporative freezing chamber 5 The end sequence is connected to the ice storage tank 9 through the one-way valve 12, the intermediate ice storage container 8, and the one-way valve 13.

在蒸发冷冻室5中,蒸发冷冻室5下部的冷剂水区通过冷剂水泵18连接位于蒸发冷冻室5上部的喷淋器,在喷淋器下部设有成冰装置6,在成冰装置6的下部设有冰水分离装置7。 In the evaporative freezing chamber 5, the refrigerant water zone at the lower part of the evaporative freezing chamber 5 is connected to the shower located at the upper part of the evaporative freezing chamber 5 through a refrigerant water pump 18, and an ice forming device 6 is arranged at the lower part of the shower, and the ice forming device The bottom of 6 is provided with ice-water separator 7.

基于溴化锂溶液吸收式制冷循环的蒸发冷冻制取流态冰的方法,包括溶液循环和蒸发冷冻取流态冰两个过程。其具体方案如下: The method for producing fluid ice by evaporative freezing based on lithium bromide solution absorption refrigeration cycle comprises two processes of solution circulation and evaporative freezing to obtain fluid ice. The specific plan is as follows:

溴化锂溶液循环过程与传统的溴化锂吸收式制冷循环中的溶液循环类似,采用溶液在吸收器中吸收蒸发蒸发冷冻室中的水蒸气,以维持蒸发冷冻室中低水蒸汽压的状态,低于622.8Pa(0℃的水对应的饱和相变压力),溶液吸收水分后被稀释浓度降低,溴化锂稀溶液通过溶液泵,到发生器中被加热再生,浓度得到提高,重新恢复吸收水蒸气的能力。蒸发冷冻制取流态冰过程是吸收器中浓溶液不断吸收蒸发器出来的水蒸气造成蒸发冷冻室的低压环境(低于622.8Pa),冷凝器中的过冷水经过节流后进入蒸发冷冻室,由于蒸发冷冻室内压力低于0℃水对应的相变压力622.8Pa,蒸发冷冻室内的水就会不断地蒸发吸收自身的热量,温度逐渐降低至0℃,甚至低于0℃,在成冰装置上经过解冷而生成流态冰,并经过一定结构的冰水分离装置,分离出流态冰,蒸发冷冻室底部的冷冻水不断地喷洒到成冰装置上,逐渐形成冰晶或者冰粒。随着制冰循环中水分的不断减少,通过在蒸发冷冻室侧加设补水装置。 The lithium bromide solution circulation process is similar to the solution circulation in the traditional lithium bromide absorption refrigeration cycle. The solution is used in the absorber to absorb the water vapor in the evaporative freezer to maintain a low water vapor pressure in the evaporative freezer, which is lower than 622.8 Pa (the saturated phase transition pressure corresponding to water at 0°C), the solution is diluted after absorbing water and the concentration is reduced. The dilute lithium bromide solution passes through the solution pump and is heated and regenerated in the generator. The concentration is increased and the ability to absorb water vapor is restored. The process of producing liquid ice by evaporative freezing is that the concentrated solution in the absorber continuously absorbs the water vapor from the evaporator to create a low-pressure environment (less than 622.8Pa) in the evaporative freezing chamber, and the supercooled water in the condenser enters the evaporative freezing chamber after throttling , because the pressure in the evaporative freezing chamber is lower than the phase transition pressure 622.8Pa corresponding to 0°C water, the water in the evaporative freezing chamber will continue to evaporate and absorb its own heat, and the temperature will gradually drop to 0°C, or even lower than 0°C. The liquid ice is generated on the device through decooling, and the liquid ice is separated by an ice-water separation device with a certain structure. The frozen water at the bottom of the evaporation freezer is continuously sprayed on the ice forming device, and ice crystals or ice particles are gradually formed. With the continuous reduction of moisture in the ice-making cycle, a water replenishment device is added on the side of the evaporative freezer.

蒸发制冰流程中,补水装置3根据蒸发冷冻室5中的最低水位要求向蒸发冷冻室5中自动补水,补水过程中补水装置3中的常温水经过补水节流阀22节流降压后进入蒸发冷冻室5中,冷凝器的水经节流阀4进入蒸发蒸发冷冻室5,蒸发蒸发冷冻室5中成冰装置6上形成的冰水混合物经冰水分离装置7、单向阀门12、中间储冰室8、单向阀门13进入储冰槽9完成制冰流程。 During the evaporative ice-making process, the water replenishment device 3 automatically replenishes water in the evaporative freezer 5 according to the minimum water level requirement in the evaporative freezer 5. In the evaporative freezing chamber 5, the water of the condenser enters the evaporative evaporative freezing chamber 5 through the throttle valve 4, and the ice-water mixture formed on the ice-forming device 6 in the evaporative evaporative freezing chamber 5 passes through the ice-water separation device 7, the one-way valve 12, The middle ice storage chamber 8 and the one-way valve 13 enter the ice storage tank 9 to complete the ice making process.

本发明将通过100℃以上热源驱动的发生器发生出的水蒸气进入冷凝器,发生后的溴化锂溶液浓度得到提升,经过换热器、冷却水冷却之后喷洒到吸收器中,吸收来自蒸发冷冻室中的水蒸气,吸收过程水蒸气变成液体释放的热量由来自冷却塔中的冷却水带走,吸收终了的溴化锂溶液浓度降低,然后通过溶液泵经过热交换器送至发生器中完成溶液发生过程。来自发生器中的水蒸气在冷凝器中经过来自冷却塔的冷却水冷却,冷凝成过冷水,然后经过节流装置节流后喷洒至蒸发冷冻室,在蒸发冷冻室中的成冰装置上蒸发并冷冻成冰晶,蒸发出的水蒸气被吸收器中浓溶液吸收,维持蒸发冷冻室内低压环境。为了防止该系统中水分不断地变成冰粒之后,循环中的水分减少,在适当的时候通过补水装置向冷凝器中补充水以保持系统循环中的水量。当蒸发冷冻室中冰水分离器中的冰晶聚集到一定量之后,打开蒸发冷冻室与中间储冰器间的单向阀门,冰晶在重力作用下进入中间储冰器,然后关闭该单向阀门。当中间储冰器中的冰晶达到一定量之后,打开中间储冰器与储冰槽之间的单向阀门,取走生成的冰晶或者冰粒,然后关闭单向阀门,开启真空泵保证中间储冰器一定的真空度。 In the present invention, the water vapor generated by the generator driven by a heat source above 100°C enters the condenser, and the concentration of the lithium bromide solution after generation is increased, and after being cooled by the heat exchanger and cooling water, it is sprayed into the absorber and absorbed from the evaporation and freezing chamber. The water vapor in the absorption process, the heat released by the water vapor into the liquid is taken away by the cooling water from the cooling tower, and the concentration of the lithium bromide solution after the absorption is reduced, and then sent to the generator through the heat exchanger through the solution pump to complete the solution generation. process. The water vapor from the generator is cooled by the cooling water from the cooling tower in the condenser, condensed into supercooled water, and then sprayed to the evaporative freezing chamber after being throttled by the throttling device, and evaporated on the ice forming device in the evaporative freezing chamber And freeze into ice crystals, the evaporated water vapor is absorbed by the concentrated solution in the absorber, maintaining the low pressure environment in the evaporation and freezing chamber. In order to prevent the water in the system from continuously turning into ice particles, the water in the circulation is reduced, and the water replenishment device is used to replenish water in the condenser at an appropriate time to maintain the amount of water in the system circulation. When the ice crystals in the ice-water separator in the evaporative freezing chamber accumulate to a certain amount, open the one-way valve between the evaporative freezing chamber and the intermediate ice storage, and the ice crystals enter the intermediate ice storage under the action of gravity, and then close the one-way valve . When the ice crystals in the intermediate ice storage reach a certain amount, open the one-way valve between the intermediate ice storage and the ice storage tank, remove the generated ice crystals or ice particles, then close the one-way valve, and turn on the vacuum pump to ensure the intermediate ice storage A certain degree of vacuum.

Claims (5)

1. 一种基于溴化锂吸收式制冷循环的流态冰制取装置,其特征在于该装置由溶液循环回路和蒸发冷冻制冰模块组成;溶液循环回路包括发生器(1)、吸收器(10)、溶液热交换器(11)、冷却器(15)、第一溶液泵(16)、第二溶液泵(17);其中,吸收器的下部的浓溶液区分别通过第一溶液泵、第二溶液泵和溶液热交换器接发生器的下部,冷却器的输入端通过溶液热交换器接发生器的下部,冷却器的输出端接位于吸收器上部的喷淋器;蒸发冷冻制冰模块由冷凝器(2)、补水装置(3)、节流阀(4)、蒸发冷冻室(5)、连接补水装置(3)与蒸发冷冻室(5)的补水节流阀(22)、成冰装置(6)、冰水分离装置(7)、第一单向阀门(12)、中间储冰器(8)、第二单向阀门(13)、储冰槽(9)、冷剂水泵(18)构成;冷凝器(2)中的冷凝水通过节流阀(4)接蒸发冷冻室(5),蒸发冷冻室(5)的输出端顺序通过第一单向阀门(12)、中间储冰器(8)、第二单向阀门(13)接储冰槽(9)。    1. A liquid ice production device based on a lithium bromide absorption refrigeration cycle, characterized in that the device is composed of a solution circulation loop and an evaporative freezing ice-making module; the solution circulation loop includes a generator (1), an absorber (10) , solution heat exchanger (11), cooler (15), first solution pump (16), second solution pump (17); wherein, the concentrated solution area in the lower part of the absorber passes through the first solution pump and the second solution pump respectively. The solution pump and the solution heat exchanger are connected to the lower part of the generator, the input end of the cooler is connected to the lower part of the generator through the solution heat exchanger, and the output end of the cooler is connected to the sprinkler on the upper part of the absorber; the evaporative freezing ice-making module is composed of Condenser (2), replenishing water device (3), throttle valve (4), evaporative freezing chamber (5), water replenishing throttle valve (22) connecting water replenishing device (3) and evaporative freezing chamber (5), ice forming Device (6), ice-water separation device (7), first one-way valve (12), intermediate ice storage (8), second one-way valve (13), ice storage tank (9), refrigerant water pump ( 18) composition; the condensed water in the condenser (2) is connected to the evaporative freezer (5) through the throttle valve (4), and the output end of the evaporative freezer (5) passes through the first one-way valve (12), intermediate storage The ice container (8) and the second one-way valve (13) are connected to the ice storage tank (9). the 2.根据权利要求1所述的基于溴化锂吸收式制冷循环的流态冰制取装置,其特征是,在蒸发冷冻室(5)中,蒸发冷冻室(5)下部的冷剂水区通过冷剂水泵(18)连接位于蒸发冷冻室(5)上部的喷淋器,在喷淋器下部设有成冰装置(6),在成冰装置(6)的下部设有冰水分离装置(7)。 2. The liquid ice production device based on lithium bromide absorption refrigeration cycle according to claim 1, characterized in that, in the evaporative freezing chamber (5), the refrigerant water zone at the lower part of the evaporative freezing chamber (5) passes through the cooling The agent water pump (18) is connected to the sprinkler located on the upper part of the evaporative freezing chamber (5), and the ice-forming device (6) is arranged at the lower part of the shower, and the ice-water separation device (7) is arranged at the lower part of the ice-forming device (6). ). 3.一种如权利要求1所述的基于溴化锂吸收式制冷循环的流态冰制取装置的制取流态冰的方法,其特征在于,蒸发制冰流程中,补水装置(3)根据蒸发冷冻室(5)中的最低水位要求向蒸发冷冻室(5)中自动补水,补水过程中补水装置(3)中的常温水经过补水节流阀(22)节流降压后进入蒸发冷冻室(5)中,冷凝器的水经节流阀(4)进入蒸发冷冻室(5),蒸发冷冻室(5)中成冰装置(6)上形成的冰水混合物经冰水分离装置(7)、第一单向阀门(12)、中间储冰室(8)、第二单向阀门(13)进入储冰槽(9)完成制冰流程。 3. A method for producing liquid ice based on a lithium bromide absorption refrigeration cycle based liquid ice production device as claimed in claim 1, characterized in that, in the evaporation ice making process, the water supply device (3) is based on the evaporation The minimum water level in the freezer (5) requires automatic replenishment of water into the evaporative freezer (5). During the replenishment process, the normal temperature water in the water replenishment device (3) enters the evaporative freezer after being throttled and reduced by the water replenishment throttle valve (22) In (5), the water in the condenser enters the evaporative freezing chamber (5) through the throttle valve (4), and the ice-water mixture formed on the ice-forming device (6) in the evaporative freezing chamber (5) passes through the ice-water separation device (7 ), the first one-way valve (12), the middle ice storage chamber (8), and the second one-way valve (13) enter the ice storage tank (9) to complete the ice making process. 4.根据权利要求3所述的基于溴化锂吸收式制冷循环的流态冰制取装置的制取流态冰的方法,其特征在于该方法利用吸收器(10)中的浓溶液吸收蒸发冷冻室(5)中的蒸汽 ,为蒸发冷冻室(5)制造低压环境,水在其中蒸发吸收自身热量,在成冰装置(6)上生长成流态冰。 4. The method for producing liquid ice based on the liquid ice production device of the lithium bromide absorption refrigeration cycle according to claim 3, characterized in that the method utilizes the concentrated solution in the absorber (10) to absorb and evaporate the freezing chamber The steam in (5) creates a low-pressure environment for the evaporative freezer (5), in which water evaporates to absorb its own heat, and grows into liquid ice on the ice-forming device (6). 5.根据权利要求3所述的基于溴化锂吸收式制冷循环的流态冰制取装置的制 5. according to claim 3 the manufacture of the liquid ice production device based on lithium bromide absorption refrigeration cycle 取流态冰的方法,其特征在于该方法的冰水分离过程是在成冰装置(6)上形成 The method for taking liquid ice is characterized in that the ice-water separation process of the method is formed on the ice-forming device (6). 的冰晶经冰水分离装置(7)分离出来,中间储冰器(8)中保持与蒸发冷冻室中 The ice crystals are separated by the ice-water separation device (7), and kept in the intermediate ice storage (8) and in the evaporative freezer 相同压力,打开单向阀门(12),在重力作用下所述的冰晶进入中间储冰器(8),然后关闭第一单向阀门(12),打开第二单向阀门(13)冰晶进入储冰槽,完成冰水分离过程;完成冰水分离之后,通过真空泵将中间储冰器(8)抽真空。 At the same pressure, open the one-way valve (12), the ice crystals enter the intermediate ice storage (8) under the action of gravity, then close the first one-way valve (12), open the second one-way valve (13) and the ice crystals enter The ice storage tank completes the ice-water separation process; after the ice-water separation is completed, the intermediate ice storage (8) is evacuated by a vacuum pump.
CN2011100237371A 2011-01-21 2011-01-21 Flow ice making method and device based on lithium bromide absorption type refrigeration cycle Expired - Fee Related CN102062507B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011100237371A CN102062507B (en) 2011-01-21 2011-01-21 Flow ice making method and device based on lithium bromide absorption type refrigeration cycle

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011100237371A CN102062507B (en) 2011-01-21 2011-01-21 Flow ice making method and device based on lithium bromide absorption type refrigeration cycle

Publications (2)

Publication Number Publication Date
CN102062507A CN102062507A (en) 2011-05-18
CN102062507B true CN102062507B (en) 2012-07-18

Family

ID=43997894

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011100237371A Expired - Fee Related CN102062507B (en) 2011-01-21 2011-01-21 Flow ice making method and device based on lithium bromide absorption type refrigeration cycle

Country Status (1)

Country Link
CN (1) CN102062507B (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102538331B (en) * 2012-03-30 2013-12-18 常熟南师大发展研究院有限公司 Method and device for fetching out flow-state ices from vacuum process flow-state ice preparing room
CN107014124A (en) * 2017-04-21 2017-08-04 高志栋 A kind of ice making method and ice-making system
CN107162344B (en) * 2017-07-03 2020-10-02 苏州华商新能源有限公司 Sewage treatment method
CN107726684A (en) * 2017-11-01 2018-02-23 江苏高菱蓄能科技有限公司 A kind of droxtal slurry preparation system
CN108592444B (en) * 2018-02-06 2023-10-31 华北电力大学 A heat exchange unit combining an electric heat pump and an absorption heat pump
CN109282397B (en) * 2018-08-14 2020-06-19 浙江理工大学 Novel energy storage air conditioner and method based on air compression refrigeration cycle

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3094781B2 (en) * 1994-04-07 2000-10-03 日本鋼管株式会社 Vacuum ice making equipment
CN1117254C (en) * 2000-09-14 2003-08-06 东南大学 Environment protection type energy-saving efficient air conditioner using solution to accumualte energy
WO2008062438A2 (en) * 2006-08-31 2008-05-29 Thermax Limited Method and apparatus for generating ice slurry
CN200986354Y (en) * 2006-12-26 2007-12-05 上海海事大学 Vacuum freezing steam absorbing type binary ice preparing device
CN201589481U (en) * 2009-09-25 2010-09-22 天津商业大学 A system for producing fluidized ice from seawater
CN201992924U (en) * 2011-01-21 2011-09-28 东南大学 Ice-slurry preparing device based on lithium bromide absorption refrigeration cycle

Also Published As

Publication number Publication date
CN102062507A (en) 2011-05-18

Similar Documents

Publication Publication Date Title
CN104374025B (en) A kind of three-phase energy-storage method of solar airconditioning
CN100552323C (en) Solar-air source energy storage type solution heat pump device
CN102062507B (en) Flow ice making method and device based on lithium bromide absorption type refrigeration cycle
CN110118448B (en) Thermal storage and cold storage gas-assisted solar energy absorption ammonia water cooling system
CN112158903B (en) Seawater desalination device based on solution dehumidification
CN201382637Y (en) Hot fluorine once deicing plate ice machine
CN102305494B (en) An Absorption Chemical Energy Storage Device Containing Crystals
CN108106046A (en) A kind of solar energy double effect absorption type heat pump system of combination three-phase accumulation of energy
CN206514443U (en) Energy supplying system based on low valley power storage
CN202216448U (en) Diffusion absorption refrigeration and vapor compression refrigeration combined cycle device
CN102322705B (en) Diffusion absorption refrigeration and vapor compression refrigeration combined cycle device
CN203068863U (en) Boiling regeneration type heat source tower heat pump system
US20210222938A1 (en) Heat-source-tower heat pump system combined with ice maker
CN105222448A (en) Adsorption-type solar contact method preparing ice slurry device
CN202254475U (en) Absorption type chemical energy storage device including crystallization
CN102080898A (en) Lithium bromide absorbing evaporative condensing water chilling unit
CN102410675B (en) Over-cooling device and over-cooling method for evaporative condensation type refrigeration system
CN201992924U (en) Ice-slurry preparing device based on lithium bromide absorption refrigeration cycle
CN101216232A (en) Method and device for producing liquid ice with double-layer evaporative supercooled water
CN107200372B (en) Seawater desalination system and method
CN113915786A (en) Compression type heat pump device utilizing latent heat for energy storage
CN202328942U (en) Supercooling device for evaporative condensate type refrigeration system and method thereof
CN201973952U (en) Lithium bromide absorption evaporative condensation water chiller
CN109282397B (en) Novel energy storage air conditioner and method based on air compression refrigeration cycle
CN113531944B (en) Double-effect three-phase energy storage and absorption type refrigerating system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120718

Termination date: 20180121