CN104006540B - Heat chemistry energy storage testing arrangement and method of testing - Google Patents
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Abstract
本发明公开热化学储能测试装置及测试方法,测试装置包括太阳能集热器、热储罐、储能反应器、释能反应器、冷储罐、冷凝器、蒸发器、循环泵以及自动温控装置。太阳能集热器的出口管连接热储罐的进口,高温的传热流体从热储罐底部出口管流入储能反应器,进入不锈钢网筒包裹的CaO/Ca(OH)2颗粒床层中的换热盘管,换热盘管出口接冷储罐,循环泵位于冷储罐的出口管和太阳能集热器的进口管间。本装置能够有效利用太阳能驱动热化学储能反应,实现太阳热能的储存和化学能的释放,并对能量的储/释速率进行测试。本发明具有储能密度高,能量品质高,测试操作简便,成本低且分解产物储存容易的优点。
The invention discloses a thermochemical energy storage test device and a test method. The test device includes a solar heat collector, a heat storage tank, an energy storage reactor, an energy release reactor, a cold storage tank, a condenser, an evaporator, a circulation pump and an automatic temperature control system. control device. The outlet pipe of the solar collector is connected to the inlet of the heat storage tank, and the high-temperature heat transfer fluid flows into the energy storage reactor from the outlet pipe at the bottom of the heat storage tank, and enters the CaO/Ca(OH) 2 particle bed wrapped in a stainless steel mesh tube. The heat exchange coil, the outlet of the heat exchange coil is connected to the cold storage tank, and the circulation pump is located between the outlet pipe of the cold storage tank and the inlet pipe of the solar collector. The device can effectively use solar energy to drive thermochemical energy storage reactions, realize solar thermal energy storage and chemical energy release, and test the energy storage/release rate. The invention has the advantages of high energy storage density, high energy quality, simple test operation, low cost and easy storage of decomposition products.
Description
技术领域 technical field
本发明化学储能技术领域,具体涉及一种充分利用太阳能驱动(Ca(OH)2 (s)↔CaO (s)+ H2O (g)) 热化学反应的热化学储能测试装置及测试方法。 The technical field of chemical energy storage of the present invention, specifically relates to a thermochemical energy storage testing device and testing device that fully utilizes solar energy to drive (Ca(OH) 2 (s)↔CaO (s)+H 2 O (g)) thermochemical reaction method.
背景技术 Background technique
随着社会的飞速发展,有限的化石燃料显得更加匮乏,不能满足现代工业发展的需求,并且燃烧所产生的环境问题也日益突出。能源结构改革的新方向主要是开发新能源以及采用新型技术提高燃料的利用率。太阳能发电由于具有费用低、来源广、不污染环境以及不需远距离输送等优点而成为人类理想的替代能源。大力开发利用太阳能,将会有效缓解能源紧缺的问题,并改变我国不合理的能源结构,使能源供应多样化。然而,由于太阳能具有间歇性、低密度和不稳定性、难以持续供应的缺点,利用太阳能进行热发电目前仍有许多问题需要解决,其中如何实现太阳能高效、大规模的储存,保证太阳能一天24h持续供给是太阳能热发电技术的关键。在太阳能热发电中,高温储热的作用是调节负荷、降低设备容量和投资成本,进一步提高太阳能资源利用效率和设备可用率,提高热电系统的可靠性和经济性。目前,主要的热能储存方式包括显热储能、潜热储能和热化学储能。在选择储能方式时需要考虑很多因素,主要包括储存时间、经济性、储能密度、热损失、供能温度等。 With the rapid development of society, the limited fossil fuels are becoming more and more scarce, which cannot meet the needs of modern industrial development, and the environmental problems caused by combustion are becoming increasingly prominent. The new direction of energy structure reform is mainly to develop new energy sources and adopt new technologies to improve fuel utilization. Solar power generation has become an ideal alternative energy source due to its advantages of low cost, wide sources, no pollution to the environment, and no need for long-distance transmission. Vigorously developing and utilizing solar energy will effectively alleviate the problem of energy shortage, change my country's irrational energy structure, and diversify energy supply. However, due to the intermittent, low density and instability of solar energy, which makes it difficult to supply continuously, there are still many problems to be solved in the use of solar energy for thermal power generation. Among them, how to achieve efficient and large-scale storage of solar energy to ensure continuous solar energy 24 hours a day Supply is the key to solar thermal power technology. In solar thermal power generation, the role of high-temperature heat storage is to adjust the load, reduce equipment capacity and investment costs, further improve the utilization efficiency of solar resources and equipment availability, and improve the reliability and economy of thermal power systems. At present, the main thermal energy storage methods include sensible heat energy storage, latent heat energy storage and thermochemical energy storage. Many factors need to be considered when choosing an energy storage method, mainly including storage time, economy, energy storage density, heat loss, energy supply temperature, etc.
显热储热指通过改变储能介质的温度来储能。储能材料可选用水、岩石、土壤等,方法简单、成本低,但其储能密度小和放热温度不恒定,且所需的储能系统结构庞大。潜热储能又称相变储能,如水受热气化,固体石蜡受热融化等,它是当今世界的研究热点。潜热储能的储能密度较显热高一个数量级,且放热温度恒定,但其储热介质一般有导热系数较小、易老化和过冷相分离等缺点。显热储能和潜热储能均具有高温下热损失过大的不足,不能长期储存高温热能。 Sensible heat storage refers to energy storage by changing the temperature of the energy storage medium. The energy storage materials can be water, rock, soil, etc. The method is simple and the cost is low, but the energy storage density is small and the heat release temperature is not constant, and the required energy storage system structure is huge. Latent heat energy storage, also known as phase change energy storage, is a research hotspot in the world today, such as water heating to gasification, solid paraffin heating to melting, etc. The energy storage density of latent heat energy storage is an order of magnitude higher than sensible heat, and the heat release temperature is constant, but its heat storage medium generally has disadvantages such as low thermal conductivity, easy aging, and supercooled phase separation. Sensible heat energy storage and latent heat energy storage both have the disadvantage of excessive heat loss at high temperature, and cannot store high temperature heat energy for a long time.
化学储能实际上就是利用储能材料相接触时发生化学反应而将储存的化学能释放出来。如C+热量↔ A+B,在这个反应中储能材料C吸收能量转化成A和B单独储存起来。当需要供能时,将A和B充分接触发生反应生成C,同时也完成了能量的释放过程。一般的,热化学储能过程可以分为三个步骤:储热、储存和热释放过程。 Chemical energy storage is actually to release the stored chemical energy by using the chemical reaction that occurs when the energy storage materials are in contact. Such as C + heat ↔ A + B, in this reaction, the energy storage material C absorbs energy and converts it into A and B for separate storage. When energy needs to be supplied, A and B are fully contacted to react to generate C, and the energy release process is also completed. Generally, the thermochemical energy storage process can be divided into three steps: heat storage, storage, and heat release process.
对比其他储热方式,热化学储能具有以下的优势:(1) 热化学储能方法能够实现在室温下长期无热损储存;(2) 储能密度高,分别相当于显热储热和潜热储热的10倍和5倍;(3) 适合长距离运输。这些特性为太阳能的高效转换、储存及传输提供了一种极具前景的方法,并能实现太阳能一天24h的连续供给,特别适用于电厂峰谷负荷调节,并于尖峰发电时释放出热能,推动汽轮机发电。目前已经研究过70多种热化学反应,但很理想的反应体系并不多。典型的热化学储能体系有无机氢氧化物热分解,主要是Ca(OH)2/CaO+H2O、Mg(OH)2/MgO+H2O,此外还有NH3的分解、碳酸化合物分解、硫酸盐分解、甲烷-二氧化碳催化重整、铵盐热分解、有机物的氢化和脱氢反应等,其中Ca(OH)2/CaO体系以及NH3的分解是研究的比较多的储能反应,也是最有前景的应用储能体系。选择化学储能材料时要考虑以下因素:(1) 反应温度适当;(2) 反应热效应大;(3) 反应不产生副反应,安全,循环寿命长;(4) 储能材料价格低廉,无毒,无腐蚀;(5) 反应时材料的体积变化要小;(6) 可逆化学反应速率要适当,以便于能量存储与释放;(7) 反应操作成熟,反应条件要求不苛刻。 Compared with other heat storage methods, thermochemical energy storage has the following advantages: (1) thermochemical energy storage method can realize long-term storage without heat loss at room temperature; (2) high energy storage density, which is equivalent to sensible heat storage and 10 times and 5 times of latent heat storage; (3) Suitable for long-distance transportation. These characteristics provide a promising method for the efficient conversion, storage and transmission of solar energy, and can realize the continuous supply of solar energy 24 hours a day, especially suitable for peak and valley load regulation of power plants, and release heat energy during peak power generation, promoting Steam turbines generate electricity. At present, more than 70 thermochemical reactions have been studied, but there are not many ideal reaction systems. Typical thermochemical energy storage systems include the thermal decomposition of inorganic hydroxides, mainly Ca(OH) 2 /CaO+H 2 O, Mg(OH) 2 /MgO+H 2 O, in addition to the decomposition of NH 3 , carbonic acid Decomposition of compounds, decomposition of sulfate, catalytic reforming of methane-carbon dioxide, thermal decomposition of ammonium salts, hydrogenation and dehydrogenation of organic matter, etc. Among them, the decomposition of Ca(OH) 2 /CaO system and NH 3 is more researched energy storage Reaction is also the most promising application for energy storage systems. The following factors should be considered when selecting chemical energy storage materials: (1) the reaction temperature is appropriate; (2) the thermal effect of the reaction is large; (3) the reaction does not produce side reactions, is safe, and has a long cycle life; (4) the energy storage material is cheap and has no (5) The volume change of the material during the reaction should be small; (6) The reversible chemical reaction rate should be appropriate to facilitate energy storage and release; (7) The reaction operation is mature and the reaction conditions are not harsh.
世界范围内的能源日趋紧张与燃烧化石燃料所带来的环境污染问题以及我国目前的能源结构调整策略为热化学储能的应用带来了很大的契机,热化学储能由于自身具有的独特优势,在大规模千兆瓦级电力调峰、太阳能热力发电、工业和民用废热和余热的回收利用等领域具有广泛的应用前景。 The increasing energy shortage worldwide, the environmental pollution caused by the burning of fossil fuels, and my country's current energy structure adjustment strategy have brought great opportunities for the application of thermochemical energy storage. Due to its unique Advantages, it has broad application prospects in the fields of large-scale gigawatt-level power peak regulation, solar thermal power generation, industrial and civil waste heat and waste heat recovery and utilization.
热化学储能是一种高密度、高能量的储能方式,其储能密度较显热和潜热高,而且此种储能体系通过催化剂或产物分离方法极易用于长期能量储存,但在实用时存在的一次性投资大、技术复杂及整体效率低等缺点。目前热化学储能式太阳能热发电仍处于小试阶段,还没有建成大规模热电站,要想让热化学储能真正成为造福人类的实用技术,还必须解决好以下问题:(1) 储能材料的选择,附带的反应控制,反应的可逆性,催化剂寿命;(2) 反应器、热交换器的设计,各种化学床体的特性,气体、固体等介质的导热性;(3) 运行循环的描述,最佳循环效率;(4) 技术和经济分析,投资/收益研究,负载要求等;(5)储能材料腐蚀性、经济性。 Thermochemical energy storage is a high-density, high-energy energy storage method. Its energy storage density is higher than sensible heat and latent heat, and this energy storage system is very easy to use for long-term energy storage through catalysts or product separation methods, but in When practical, there are disadvantages such as large one-time investment, complex technology and low overall efficiency. At present, thermochemical energy storage solar thermal power generation is still in the small-scale test stage, and large-scale thermal power plants have not yet been built. To make thermochemical energy storage truly a practical technology for the benefit of mankind, the following problems must be solved: (1) Energy storage Selection of materials, incidental reaction control, reversibility of reaction, catalyst life; (2) design of reactors and heat exchangers, characteristics of various chemical beds, thermal conductivity of gases, solids and other media; (3) operation Cycle description, optimal cycle efficiency; (4) technical and economic analysis, investment/revenue research, load requirements, etc.; (5) energy storage material corrosiveness and economy.
发明内容 Contents of the invention
本发明是针对太阳能热化学储能实际应用中存在的技术问题,提供了热化学储能测试装置及测试方法,将太阳能转化成化学能储存起来并能在需要时及时释放出来,具体方案如下。 The present invention aims at the technical problems existing in the practical application of solar thermochemical energy storage, and provides a thermochemical energy storage testing device and testing method, which can convert solar energy into chemical energy and store it and release it in time when needed. The specific scheme is as follows.
热化学储能测试装置,其包括:太阳能集热器、温度控制器TC、温度测量变送器TT、热储罐、储能反应器、换热盘管、压力表、热电偶温度计、冷凝器、换热器、电阻丝加热器、冷储罐和循环泵;其中温度测量变送器TT用于测量太阳能集热器出口流体的温度,温度控制器TC用于控制太阳能集热器的入口管路上第一阀门V1的开度,温度控制器TC和温度测量变送器TT组成自动温控装置;太阳能集热器的出口管连接热储罐的进口,热流体经热储罐底部出口管进入储能反应器内部的换热盘管;储能反应器内设有第一热电偶温度计,储能反应器顶部蒸汽出口管连接着冷凝器,冷凝器内设置有液位传感计、电阻丝加热器、第二热电偶温度计及换热器;释能反应器出口管连接冷储罐,循环泵安装在冷储罐出口管及太阳能集热器的进口管路间。 Thermochemical energy storage test device, which includes: solar collector, temperature controller TC, temperature measurement transmitter TT, thermal storage tank, energy storage reactor, heat exchange coil, pressure gauge, thermocouple thermometer, condenser , heat exchanger, resistance wire heater, cold storage tank and circulating pump; the temperature measuring transmitter TT is used to measure the temperature of the outlet fluid of the solar collector, and the temperature controller TC is used to control the inlet pipe of the solar collector The opening degree of the first valve V1 on the road, the temperature controller TC and the temperature measuring transmitter TT form an automatic temperature control device; the outlet pipe of the solar collector is connected to the inlet of the thermal storage tank, and the thermal fluid enters through the outlet pipe at the bottom of the thermal storage tank The heat exchange coil inside the energy storage reactor; the first thermocouple thermometer is installed in the energy storage reactor, the steam outlet pipe on the top of the energy storage reactor is connected to the condenser, and the liquid level sensor, resistance wire A heater, a second thermocouple thermometer and a heat exchanger; the outlet pipe of the energy release reactor is connected to the cold storage tank, and the circulation pump is installed between the outlet pipe of the cold storage tank and the inlet pipe of the solar heat collector.
进一步优化的,所述储能反应器内部是包裹着CaO/Ca(OH)2颗粒床层的不锈钢网筒,换热盘管位于CaO/Ca(OH)2颗粒床层的中心处,CaO/Ca(OH)2颗粒床层中设有8个所述第一热电偶温度计;所述储能反应器在CaO/Ca(OH)2颗粒床层发生水合反应的过程中又用作释能反应器,释能反应器的内部构成同所述储能反应器,储能反应器和释能反应器外部包裹有绝热层。 Further optimized, the interior of the energy storage reactor is wrapped with CaO/Ca(OH) 2 stainless steel mesh tubes of the granular bed, the heat exchange coil is located at the center of the CaO/Ca(OH) 2 granular bed, and the CaO/ The Ca(OH) 2 particle bed is provided with 8 first thermocouple thermometers; the energy storage reactor is used as an energy release reaction during the hydration reaction of the CaO/Ca(OH) 2 particle bed The internal structure of the energy release reactor is the same as that of the energy storage reactor, and the exterior of the energy storage reactor and the energy release reactor is wrapped with an insulating layer.
进一步优化的,太阳能集热器由玻璃套封、不锈钢外壁、绝热层及吸热盘管组成,吸热盘管排布在玻璃套封的内部,吸热盘管外壁涂有选择性涂层,玻璃套封的不锈钢外壁包裹着绝热层。 Further optimized, the solar collector is composed of glass casing, stainless steel outer wall, heat insulation layer and heat-absorbing coil. The heat-absorbing coil is arranged inside the glass casing, and the outer wall of the heat-absorbing coil is coated with selective coating. A glass-encased stainless steel exterior wraps around the insulation.
为了克服太阳辐射的不稳定性,在太阳能集热器的出口设置了自动控温装置,由温度控制器TC和温度测量变送器TT组成;其中温度测量变送器TT测量太阳能集热器出口流体的温度,温度控制器TC控制太阳能集热器的入口管路上第一阀门V1的开度,通过调节流股1的流率来控制太阳能集热器出口流体的温度处于恒定状态。 In order to overcome the instability of solar radiation, an automatic temperature control device is installed at the outlet of the solar collector, which is composed of a temperature controller TC and a temperature measurement transmitter TT; where the temperature measurement transmitter TT measures the outlet of the solar collector The temperature of the fluid, the temperature controller TC controls the opening of the first valve V1 on the inlet pipeline of the solar collector, and controls the temperature of the outlet fluid of the solar collector to be in a constant state by adjusting the flow rate of the stream 1.
进一步优化的,储能反应器内部的不锈钢网筒被四个铜翅片两两呈90度布置等分成四个部分,每个部分从上到下等间距设置了3块不锈钢板,将整个不锈钢网筒分成4×4即16个小区域;所述第一热电偶温度计共有8个,分布在CaO/Ca(OH)2颗粒床层中相对的8个小区域内部。 Further optimization, the stainless steel mesh tube inside the energy storage reactor is divided into four parts by four copper fins arranged in pairs at 90 degrees. Each part is equipped with 3 stainless steel plates at equal intervals from top to bottom, and the whole stainless steel The grid cylinder is divided into 4×4, that is, 16 small areas; there are 8 first thermocouple thermometers, which are distributed in the relative 8 small areas in the CaO/Ca(OH) 2 particle bed.
进一步优化的,冷凝器底部设置有电阻丝加热器,故冷凝器又作为蒸发器;电阻丝加热器位于冷凝器的底部,第二热电偶温度计用于测量冷凝器内部冷凝水或蒸发器内部水蒸汽的温度,所述冷凝器和蒸发器的外部包裹有绝热层,冷水能由位于蒸发器底部的第五阀门经入口管流入蒸发器。 Further optimization, the bottom of the condenser is equipped with a resistance wire heater, so the condenser is used as an evaporator; the resistance wire heater is located at the bottom of the condenser, and the second thermocouple thermometer is used to measure the condensed water inside the condenser or the water inside the evaporator The temperature of the steam, the condenser and the evaporator are wrapped with a thermal insulation layer, and the cold water can flow into the evaporator through the inlet pipe through the fifth valve located at the bottom of the evaporator.
进一步优化的,换热盘管出口冷流体由第七阀门流入冷储罐中。 Further optimized, the cold fluid at the outlet of the heat exchange coil flows into the cold storage tank through the seventh valve.
上述热化学储能测试装置的储能测试方法具体是:热水从热储罐底部出口管流入储能反应器,并将热量传递给CaO/Ca(OH)2颗粒床层,驱动热化学反应(Ca(OH)2(s)↔CaO(s)+H2O(g))发生,吸收的太阳能转化为CaO和水蒸气的化学能储存起来,水蒸气经冷凝器冷凝形成液态水和CaO自动分开储存;当水蒸气再次进入到释能反应器中,和CaO相接触时发生水合反应并放出大量的热,实现化学能的释放过程;CaO/Ca(OH)2颗粒床层中的热电偶温度计显示出床层中不同位置处温度,记录每个时刻的温度,根据热释放速率获得储能和释能速率。 The energy storage test method of the above thermochemical energy storage test device is specifically: hot water flows into the energy storage reactor from the outlet pipe at the bottom of the thermal storage tank, and transfers heat to the CaO/Ca(OH) 2 particle bed to drive the thermochemical reaction (Ca(OH) 2 (s)↔CaO(s)+H 2 O(g)) occurs, the absorbed solar energy is converted into CaO and the chemical energy of water vapor is stored, and the water vapor is condensed by the condenser to form liquid water and CaO Automatic separate storage; when the water vapor enters the energy release reactor again, a hydration reaction occurs when it contacts with CaO and a large amount of heat is released, realizing the release process of chemical energy; the thermoelectricity in the CaO/Ca(OH) 2 particle bed The dual thermometer shows the temperature at different positions in the bed, records the temperature at each moment, and obtains the energy storage and energy release rate according to the heat release rate.
热流体从太阳能集热器出口进入热储罐中暂存,然后由热储罐底部出口管经第二阀门V2流入储反应器内的换热盘管中,换热后的冷流体从储能反应器底部出口管经第七阀门V7流入冷储罐中暂存。循环泵位于冷储罐的出口管和太阳能集热器的进口管路间,用来实现储热、释热过程换热流体的循环。 The hot fluid enters the heat storage tank from the outlet of the solar collector for temporary storage, and then flows into the heat exchange coil in the storage reactor through the second valve V2 from the outlet pipe at the bottom of the heat storage tank, and the cold fluid after heat exchange flows from the energy storage The outlet pipe at the bottom of the reactor flows into the cold storage tank through the seventh valve V7 for temporary storage. The circulation pump is located between the outlet pipe of the cold storage tank and the inlet pipe of the solar collector, and is used to realize the circulation of the heat exchange fluid in the process of heat storage and heat release.
储能反应器右侧顶部出口管连接着冷凝器,储能反应器底部出口管经第七阀门V7连接冷储罐的进口。发生放热反应时,低温的传热流体可由释能反应器底部入口管经第六阀门V6流入换热盘管内部,换热后的高温传热流体再经第三阀门V3由顶部出口管流出。 The top outlet pipe on the right side of the energy storage reactor is connected to the condenser, and the bottom outlet pipe of the energy storage reactor is connected to the inlet of the cold storage tank through the seventh valve V7. When an exothermic reaction occurs, the low-temperature heat transfer fluid can flow into the heat exchange coil from the bottom inlet pipe of the energy release reactor through the sixth valve V6, and the high-temperature heat transfer fluid after heat exchange flows out from the top outlet pipe through the third valve V3 .
本发明与现有技术相比,具有如下优点: Compared with the prior art, the present invention has the following advantages:
可充分利用太阳能来驱动化学反应(Ca(OH)2(s)↔CaO(s)+H2O(g)的发生,且储能过程中Ca(OH)2所释放的水蒸气可透过不锈钢网孔进入储能反应器中,沿储能反应器顶部蒸汽出口管进入到冷凝器中冷凝成液态水,实现了水蒸气和固体CaO的自动分开储存。当需要供能时,可利用外界余热通过换热器和冷凝器中冷凝水换热或加热器底部的电阻丝加热器来加热液态水生成水蒸气。水蒸气进入到释能反应器中和固体CaO重新接触而反应,反应放出的大量热可通过CaO/Ca(OH)2颗粒床层中心处的换热盘管收集。由于CaO/Ca(OH)2颗粒床层存在着导入热性能差的缺陷,故将整个CaO/Ca(OH)2颗粒床层用4个铜翅片和三块不锈钢板分成16个小区域。太阳能集热器出口管路上安装了自动温控装置,通过调节冷储罐出口流体流率来控制太阳能集热器出口流体温度。本装置能够有效实现太阳能向化学能的转化,且为固、气反应,储能介质的存储及运输简单,具有容易控制、能量利用效率高、储能密度高的优点。 Can make full use of solar energy to drive chemical reactions (Ca(OH) 2 (s)↔CaO(s)+H 2 O(g), and the water vapor released by Ca(OH) 2 during energy storage is permeable The stainless steel mesh enters the energy storage reactor, and enters the condenser along the steam outlet pipe at the top of the energy storage reactor to condense into liquid water, realizing the automatic separate storage of water vapor and solid CaO. When energy supply is required, external The waste heat is heated by the condensed water heat exchange in the heat exchanger and the condenser or the resistance wire heater at the bottom of the heater to heat the liquid water to generate water vapor. The water vapor enters the energy release reactor and re-contacts with solid CaO to react, and the released A large amount of heat can be collected by the heat exchange coil at the center of the CaO/ Ca (OH) particle bed. Because the CaO/ Ca (OH) particle bed has the defect of poor thermal performance, the entire CaO/Ca( OH) The 2 particle bed is divided into 16 small areas with 4 copper fins and three stainless steel plates. An automatic temperature control device is installed on the outlet pipeline of the solar collector, and the solar collector is controlled by adjusting the fluid flow rate at the outlet of the cold storage tank. Heater outlet fluid temperature. This device can effectively realize the conversion of solar energy into chemical energy, and it is a solid-gas reaction. The storage and transportation of the energy storage medium are simple, and it has the advantages of easy control, high energy utilization efficiency, and high energy storage density.
附图说明 Description of drawings
图1是热化学储能装置整体示意图。 Figure 1 is an overall schematic diagram of a thermochemical energy storage device.
图2是储能反应器的内部结构图。 Figure 2 is a diagram of the internal structure of the energy storage reactor.
图3是CaO/Ca(OH)2颗粒床层中热电偶温度计布置图。 Fig. 3 is the arrangement diagram of the thermocouple thermometer in the CaO/Ca(OH) 2 particle bed.
图4是太阳能集热器正视图。 Figure 4 is a front view of the solar collector.
图5是太阳能集热器侧视图。 Figure 5 is a side view of the solar collector.
具体实施方式 detailed description
下面结合附图,对本发明的结构和具体工作过程作详细描述,但本发明的实施和保护不限于此。 The structure and specific working process of the present invention will be described in detail below in conjunction with the accompanying drawings, but the implementation and protection of the present invention are not limited thereto.
如图1,热化学储能测试装置,包括太阳能集热器1、第一阀门V1 2、温度控制器TC 3、温度测量变送器TT 4、热储罐5、储能反应器 6、换热盘管 7、压力表11、释能反应器13、第一热电偶温度计15、冷凝器17、蒸发器20、换热器21、电阻丝加热器22、冷储罐23、循环泵24。如图4、图5所示,太阳能集热器1主要由玻璃套封25以及导热性能良好的吸热盘管28组成。太阳能集热器1出口热流体流入热储罐5暂存,热流体由热储罐5出口管经第二阀门V2进入储能反应器6内部的换热盘管7内。自动控温装置由温度控制器TC 3和温度测量变送器TT 4组成,温度控制器TC 3可控制太阳能集热器的入口管路上第一阀门V1的开度,通过调节流股1的流率来控制太阳能集热器出口流体温度处于恒定状态。 As shown in Figure 1, the thermochemical energy storage test device includes a solar collector 1, a first valve V1 2, a temperature controller TC 3, a temperature measurement transmitter TT 4, a heat storage tank 5, an energy storage reactor 6, a heat exchanger Heat coil 7, pressure gauge 11, energy release reactor 13, first thermocouple thermometer 15, condenser 17, evaporator 20, heat exchanger 21, resistance wire heater 22, cold storage tank 23, circulation pump 24. As shown in FIG. 4 and FIG. 5 , the solar heat collector 1 is mainly composed of a glass envelope 25 and a heat-absorbing coil 28 with good thermal conductivity. The thermal fluid at the outlet of the solar collector 1 flows into the thermal storage tank 5 for temporary storage, and the thermal fluid enters the heat exchange coil 7 inside the energy storage reactor 6 through the second valve V2 through the outlet pipe of the thermal storage tank 5 . The automatic temperature control device is composed of a temperature controller TC 3 and a temperature measuring transmitter TT 4. The temperature controller TC 3 can control the opening of the first valve V1 on the inlet pipeline of the solar collector, by adjusting the flow of the stream 1 rate to control the outlet fluid temperature of the solar collector in a constant state.
储能反应器6顶部安装有压力表11。如图2所示,储能反应器6内部是包裹有CaO/Ca(OH)2颗粒床层9的不锈钢网筒12,四个铜翅片8两两相邻呈90度布置将不锈钢网筒12等分成四个部分,每个部分从上到下等间距设置了3块不锈钢板10,如图3所示,整个CaO/Ca(OH)2颗粒床层被分成4×4即16个小区域。换热盘管7位于CaO/Ca(OH)2颗粒床层9的中心处,冷流体经换热盘管由第七阀门V7流入冷储罐23中。8个第一热电偶温度计15分别布置在CaO/Ca(OH)2颗粒床层中处于对顶角位置的8个小区域内。循环泵24位于冷储罐23出口管路和太阳能集热器1进口管路间。储能反应器6顶部蒸汽出口管连接着冷凝器17,冷凝器17内设置了液位传感器16、换热器21和第二热电偶温度计18,蒸发器20内设置了电阻丝加热器22。 A pressure gauge 11 is installed on the top of the energy storage reactor 6 . As shown in Figure 2, the interior of the energy storage reactor 6 is a stainless steel mesh cylinder 12 wrapped with a CaO/Ca(OH) 2 particle bed 9, and four copper fins 8 are arranged adjacent to each other at 90 degrees to connect the stainless steel mesh cylinder 12 is equally divided into four parts, and each part is provided with three stainless steel plates 10 at equal intervals from top to bottom, as shown in Fig. area. The heat exchange coil 7 is located at the center of the CaO/Ca(OH) 2 particle bed 9, and the cold fluid flows into the cold storage tank 23 through the seventh valve V7 through the heat exchange coil. The 8 first thermocouple thermometers 15 are respectively arranged in 8 small areas in the opposite corner positions in the CaO/Ca(OH) 2 particle bed. The circulation pump 24 is located between the outlet pipeline of the cold storage tank 23 and the inlet pipeline of the solar heat collector 1 . The steam outlet pipe at the top of the energy storage reactor 6 is connected to the condenser 17, the liquid level sensor 16, the heat exchanger 21 and the second thermocouple thermometer 18 are arranged in the condenser 17, and the resistance wire heater 22 is arranged in the evaporator 20.
储能反应器6顶端连接蒸汽出口管道,打开第四阀门V4,水蒸气进入到冷凝器17后冷凝为液态水储存起来,其顶端的压力计可随时监测容器中的压力,底部安装的第二热电偶温度计18可监测出冷凝器17内凝结水或蒸发器20中水蒸气的温度。通过液位传感器16可读出冷凝器17或加热器20中的液位变化,蒸发器底部安装有电阻丝加热器22,冷水也可由第五阀门V5补充到蒸发器20中。 The top of the energy storage reactor 6 is connected to the steam outlet pipe, and the fourth valve V4 is opened. The water vapor enters the condenser 17 and is condensed into liquid water for storage. The pressure gauge at the top can monitor the pressure in the container at any time, and the second valve installed at the bottom The thermocouple thermometer 18 can monitor the temperature of the condensed water in the condenser 17 or the water vapor in the evaporator 20 . The liquid level change in the condenser 17 or the heater 20 can be read through the liquid level sensor 16, and a resistance wire heater 22 is installed at the bottom of the evaporator, and cold water can also be added to the evaporator 20 through the fifth valve V5.
本装置的具体使用方式为:太阳热能储存过程:低温的传热流体受热后经太阳能集热器出口管道流入保温性能良好的热储罐5中储存,顶部的压力表可显示出热储罐中的压力。打开热储罐底部出口管路上的第二阀门V2,热流体流入储能反应器6内CaO/Ca(OH)2颗粒床层中心处的换热盘管7,将热量传递给CaO/Ca(OH)2颗粒床层,Ca(OH)2受热分解生成CaO和水蒸气,实现太阳能以CaO和水蒸气的化学能储存。根据CaO/Ca(OH)2颗粒床层中第一热电偶温度计15的读数和Ca(OH)2热分解的温度 (510℃)可推测分解反应是否发生,即储能过程发生与否,根据热电偶温度计读数变化快慢可计算储能速率。打开第七阀门V7,保持第六阀门V6关闭,低温的传热流体流入冷储罐23中储存,循环泵24将冷流体再次泵入太阳能集热器1即开始下一轮的储热循环。根据温度测量变送器的读数通过温度控制器自动调节第一阀门V1的开度,保持太阳能集热器出口流体温度保持恒定。 The specific usage of this device is as follows: Solar thermal energy storage process: After being heated, the low-temperature heat transfer fluid flows into the heat storage tank 5 with good thermal insulation performance through the outlet pipe of the solar collector for storage. pressure. Open the second valve V2 on the outlet pipeline at the bottom of the thermal storage tank, and the thermal fluid flows into the energy storage reactor 6 in the CaO/Ca(OH) heat exchange coil 7 at the center of the particle bed, and transfers heat to CaO/Ca ( OH) 2 particle bed, Ca(OH) 2 is thermally decomposed to generate CaO and water vapor, realizing the chemical energy storage of solar energy with CaO and water vapor. According to the reading of the first thermocouple thermometer 15 in the CaO/ Ca (OH) particle bed and the temperature (510° C.) of Ca (OH) thermal decomposition, it can be inferred whether the decomposition reaction occurs, that is, whether the energy storage process occurs, according to The rate of energy storage can be calculated from the speed at which the thermocouple thermometer reading changes. Open the seventh valve V7, keep the sixth valve V6 closed, the low-temperature heat transfer fluid flows into the cold storage tank 23 for storage, and the circulation pump 24 pumps the cold fluid into the solar collector 1 again to start the next heat storage cycle. According to the reading of the temperature measuring transmitter, the opening degree of the first valve V1 is automatically adjusted through the temperature controller to keep the temperature of the fluid at the outlet of the solar collector constant.
储能介质的储存与分离过程:反应过程生成的水蒸气透过不锈钢网孔12沿着储能反应器顶部的蒸汽出口管道流出。打开第四阀门V4水蒸气经储能反应器顶部蒸汽出口管流入到冷凝器17内冷凝成为液态水,自动实现和固体CaO的分开储存,通过压力表和液位传感器可显示出冷凝器中的压力及液位。 Storage and separation process of energy storage medium: the water vapor generated in the reaction process flows out through the stainless steel mesh 12 along the steam outlet pipe at the top of the energy storage reactor. Open the fourth valve V4. The water vapor flows into the condenser 17 through the steam outlet pipe at the top of the energy storage reactor and condenses to become liquid water, which is automatically stored separately from solid CaO. The pressure gauge and liquid level sensor can display the water vapor in the condenser. pressure and level.
化学能的热释放过程:可利用外界余热通过换热器21和冷凝器中的冷凝水换热而产生水蒸气,也可利用蒸发器20内的电阻丝加热器22生成水蒸气。打开第四阀门V4,水蒸气沿管道进入到释能反应器13中,透过不锈钢网筒12和内部的CaO发生反应生成Ca(OH)2同时放出大量的热,同时保持第二阀门V2和第七阀门V7关闭,让冷流体经第六阀门V6流入释能反应器内的换热盘管7,换热后的热流体经第三阀门V3流出以供使用,从而实现化学能的释放。当CaO/Ca(OH)2颗粒床层中热电偶温度计的读数开始持续上升时,表示化学能热释放过程发生了,根据床层温度上升的快慢可计算出热释放速率。 The heat release process of chemical energy: the external waste heat can be used to exchange heat between the heat exchanger 21 and the condensed water in the condenser to generate water vapor, and the resistance wire heater 22 in the evaporator 20 can also be used to generate water vapor. Open the fourth valve V4, water vapor enters into the energy release reactor 13 along the pipeline, and reacts with the CaO inside the stainless steel mesh cylinder 12 to generate Ca(OH) 2 while releasing a large amount of heat, while maintaining the second valve V2 and The seventh valve V7 is closed, allowing the cold fluid to flow into the heat exchange coil 7 in the energy release reactor through the sixth valve V6, and the hot fluid after heat exchange flows out through the third valve V3 for use, thereby realizing the release of chemical energy. When the reading of the thermocouple thermometer in the CaO/Ca(OH) 2 particle bed begins to rise continuously, it means that the heat release process of chemical energy has occurred, and the heat release rate can be calculated according to the speed of the bed temperature rise.
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