CN111537557B - Performance test method, system, medium and equipment of total heat exchange membrane - Google Patents
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Abstract
本发明提供一种全热交换膜的性能测试方法、系统、介质及设备,所述全热交换膜的性能测试方法包括:当已知热阻的全热交换膜放于全热交换膜性能测试装置时,获取预设时间段内的第一温度数据;根据所述第一温度数据确定误差传热值;当待测全热交换膜放于所述全热交换膜性能测试装置时,获取预设时间段内的第二温度数据和湿度数据;所述待测全热交换膜为未知热阻的全热交换膜;根据所述第二温度数据、湿度数据和误差传热值评价所述待测全热交换膜的性能。本发明能够对全热交换膜的传热、传湿性能进行单独测试以及耦合测试,用于全热交换膜材料筛选评价以及性能改进。
The invention provides a performance testing method, system, medium and equipment of a total heat exchange membrane. The performance testing method of the total heat exchange membrane includes: when a total heat exchange membrane with known thermal resistance is placed in a total heat exchange membrane performance test device, acquire the first temperature data within a preset time period; determine the error heat transfer value according to the first temperature data; Set the second temperature data and humidity data within the time period; the total heat exchange film to be tested is a total heat exchange film with unknown thermal resistance; evaluate the to-be-tested total heat exchange film according to the second temperature data, humidity data and error heat transfer value Measure the performance of the total heat exchange membrane. The invention can carry out independent test and coupling test on the heat transfer and moisture transfer performance of the total heat exchange membrane, and is used for the screening evaluation and performance improvement of the total heat exchange membrane material.
Description
技术领域technical field
本发明涉及全热交换膜性能评价技术领域,涉及一种性能评价方法,特别是涉及一种全热交换膜的性能测试方法、系统、介质及设备。The invention relates to the technical field of performance evaluation of total heat exchange membranes, and relates to a performance evaluation method, in particular to a performance test method, system, medium and equipment of a total heat exchange membrane.
背景技术Background technique
目前我国、美国、欧洲和日本均制定了相应的全热交换器规范,且各规范侧重点并不相同。由于标准制定区域的气候差异,导致相应规范中对全热交换器进行检测的测试工况存在差异。除此之外,ANRI 1060-2013并未考虑结露与噪声测试;EN308未对装置的全热效率提出检测要求;JISB8628缺少对箱体以及内部漏气度的测试;GB/T 21087-2007没有对潜热效率提出要求,但其在适用范围、装置类别、工况设定等方面更为完善。但各标准提出检测要求均针对整机而言,没有涉及全热交换膜热湿性能的测试指标与测试方法。At present, my country, the United States, Europe and Japan have formulated corresponding specifications for total heat exchangers, and the focus of each specification is different. Due to climate differences in standard-setting areas, there are differences in the test conditions for testing total heat exchangers in the corresponding specifications. In addition, ANRI 1060-2013 does not consider the condensation and noise test; EN308 does not put forward testing requirements for the total thermal efficiency of the device; JISB8628 lacks the test for the cabinet and internal air leakage; Latent heat efficiency puts forward requirements, but it is more perfect in terms of scope of application, device category, and working condition setting. However, the testing requirements of each standard are all for the whole machine, and there are no test indicators and test methods related to the thermal and humidity performance of the total heat exchange membrane.
全热交换器通过全热交换膜作为媒介进行显热与全热回收,因此要求材料具有良好的传热性能,且对水蒸气具有高透过性。针对上述两种性能,目前日本已制定相应的全热交换器材料评价指标,但我国尚未发布热湿交换材料性能评价标准。The total heat exchanger uses the total heat exchange membrane as a medium to recover sensible heat and total heat, so the material is required to have good heat transfer performance and high permeability to water vapor. In view of the above two properties, Japan has formulated corresponding evaluation indicators for total heat exchanger materials, but my country has not yet issued performance evaluation standards for heat and moisture exchange materials.
日本规范中只涉及材料透湿、透气与阻燃性能的测试方法,并未涉及材料传热性能的测试。由于全热交换膜传热过程中传热热阻主要为对流换热热阻,因此,根据全热交换膜两侧整体传热过程即传热系数判断材料传热性能优劣。测试室传热系数测试方法主要是静态热箱法,其一般分为标定热箱法和防护热箱法。热箱法一般用于测定建筑构件或围护结构的传热系数,其检测原理是将待测件放入冷、热箱之中,在稳定状态下,当冷热箱温度基本保持不变时,测量输入热箱的功率和冷、热箱空气温度,从而获得待测件传热系数。热箱法基本原理也应用于温室覆盖材料保温性能测试。在测定建筑构件与温室覆盖材料传热系数方面,热箱法的应用已经十分成熟,但全热交换器全热交换膜规格和传热特性与上述两者不同,且现有规范适用于测试室测量大尺寸试件。因此,不能使用规范中要求条件与设备测试全热交换膜传热系数。The Japanese standard only involves the test methods of material moisture permeability, air permeability and flame retardancy, and does not involve the test of material heat transfer performance. Since the heat transfer resistance in the heat transfer process of the total heat exchange membrane is mainly the convective heat transfer resistance, the heat transfer performance of the material is judged according to the overall heat transfer process on both sides of the total heat exchange membrane, that is, the heat transfer coefficient. The test method of heat transfer coefficient in the test chamber is mainly the static hot box method, which is generally divided into the calibration hot box method and the protective hot box method. The hot box method is generally used to measure the heat transfer coefficient of building components or enclosure structures. The detection principle is to put the test piece into the cold and hot boxes. , measure the power input into the hot box and the air temperature of the cold and hot boxes, so as to obtain the heat transfer coefficient of the DUT. The basic principle of the hot box method is also applied to the insulation performance testing of greenhouse covering materials. In terms of determining the heat transfer coefficient of building components and greenhouse covering materials, the application of the hot box method has been very mature, but the specifications and heat transfer characteristics of the total heat exchange film of the total heat exchanger are different from the above two, and the existing specifications are applicable to the test room Measure large size test pieces. Therefore, the conditions and equipment required in the specification cannot be used to test the heat transfer coefficient of the total heat exchange membrane.
对于材料透湿性的测试,测试方法可以按照原理分为称重法和传感器法。称重法利用透湿杯两侧存在的湿度差,对待测件的透湿性进行测试;传感器法主要有电解法和红外检定法,其中电解法利用该电解电流与水蒸气的关系计算通过待测件的水蒸气含量,从而获得待测件的透湿性能;红外检定法基本原理是待测件两侧分别流过湿度恒定的氮气与干燥氮气,水蒸气由于湿度差从潮湿侧流向干燥测,最终由载气传送到红外检测器产生电信号,通过电信号计算待测件水蒸气透过率。3种测试方法各有优劣,称重法测试时间长,易受外界因素干扰,精度不高;但其原理与测试设备简单。电解法和传感器法成本高,且仪器需要定期标定,但测试精度高。For the test of material moisture permeability, the test methods can be divided into weighing method and sensor method according to the principle. The weighing method uses the humidity difference between the two sides of the moisture-permeable cup to test the moisture permeability of the test piece; the sensor method mainly includes the electrolysis method and the infrared test method, and the electrolysis method uses the relationship between the electrolysis current and water vapor to calculate and pass the test. The water vapor content of the test piece can be obtained to obtain the moisture permeability of the test piece; the basic principle of the infrared test method is that nitrogen with constant humidity and dry nitrogen flow through both sides of the test piece respectively, and water vapor flows from the wet side to the dry test due to the humidity difference. Finally, the carrier gas is sent to the infrared detector to generate an electrical signal, and the water vapor transmission rate of the test piece is calculated through the electrical signal. The three test methods have their own advantages and disadvantages. The weighing method takes a long time to test, is easily disturbed by external factors, and has low accuracy; but its principle and test equipment are simple. The cost of electrolysis and sensor method is high, and the instrument needs to be calibrated regularly, but the test accuracy is high.
由上述相关规范不难看出,上述针对全热交换器的相关规范关注点在于整机的性能评价,并未涉及全热交换膜的性能测试方法与条件。而全热交换膜性能好坏能够直接影响到静式全热交换器效率的高低。但目前针对薄片、纸等材料的传热与透湿性能测试规范中两种性能测试方法相互独立,分开进行。但在静式全热交换器实际工作中,全热交换膜同时进行传热与传质过程,两者相互作用,互相影响。根据单一指标对全热交换膜进行评价,往往会忽略耦合影响,也使得全热交换膜的优劣难以比较。It is not difficult to see from the above-mentioned relevant specifications that the above-mentioned relevant specifications for total heat exchangers focus on the performance evaluation of the whole machine, and do not involve the performance test methods and conditions of the total heat exchange membrane. The performance of the total heat exchange membrane can directly affect the efficiency of the static total heat exchanger. However, in the current heat transfer and moisture permeability test specifications for thin sheets, paper and other materials, the two performance test methods are independent of each other and are carried out separately. However, in the actual work of the static total heat exchanger, the total heat exchange membrane performs heat transfer and mass transfer at the same time, and the two interact and influence each other. The evaluation of total heat exchange membranes based on a single index often ignores the coupling effect, which also makes it difficult to compare the advantages and disadvantages of total heat exchange membranes.
因此,如何提供一种全热交换膜的性能测试方法、系统、介质及设备,以解决现有技术无法结合传热与传质的耦合影响对全热交换膜进行性能评价等缺陷,成为本领域技术人员亟待解决的技术问题。Therefore, how to provide a performance testing method, system, medium and equipment of a total heat exchange membrane, so as to solve the defects that the existing technology cannot combine the coupling influence of heat transfer and mass transfer to perform performance evaluation on the total heat exchange membrane, has become an important issue in this field. Technologists urgently need to solve technical problems.
发明内容Contents of the invention
鉴于以上所述现有技术的缺点,本发明的目的在于提供一种全热交换膜的性能测试方法、系统、介质及设备,用于解决现有技术无法结合传热与传质的耦合影响对全热交换膜进行性能评价的问题。In view of the shortcomings of the prior art described above, the purpose of the present invention is to provide a performance testing method, system, medium and equipment of a total heat exchange membrane, which is used to solve the problem that the prior art cannot combine the coupling influence of heat transfer and mass transfer. Performance evaluation of total heat exchange membranes.
为实现上述目的及其他相关目的,本发明一方面提供一种全热交换膜的性能测试方法,所述全热交换膜的性能测试方法包括:当已知热阻的全热交换膜放于全热交换膜性能测试装置时,获取预设时间段内的第一温度数据;根据所述第一温度数据确定误差传热值;当待测全热交换膜放于所述全热交换膜性能测试装置时,获取预设时间段内的第二温度数据和湿度数据;所述待测全热交换膜为未知热阻的全热交换膜;根据所述第二温度数据、湿度数据和误差传热值评价所述待测全热交换膜的性能。In order to achieve the above and other related purposes, the present invention provides a method for testing the performance of a total heat exchange membrane. The method for testing the performance of a total heat exchange membrane includes: when a total heat exchange membrane with known thermal resistance is placed When the heat exchange membrane performance testing device is used, the first temperature data within a preset time period is obtained; the error heat transfer value is determined according to the first temperature data; when the total heat exchange membrane to be tested is placed in the total heat exchange membrane performance test When the device is installed, the second temperature data and humidity data within a preset time period are acquired; the total heat exchange film to be tested is a total heat exchange film with unknown thermal resistance; according to the second temperature data, humidity data and error heat transfer value to evaluate the performance of the total heat exchange membrane to be tested.
于本发明的一实施例中,所述根据所述第一温度数据确定误差传热值的步骤包括:将所述第一温度数据作为已知量代入传热系数的表达式中;将所述误差传热值作为唯一未知量进行求解。In an embodiment of the present invention, the step of determining the error heat transfer value according to the first temperature data includes: substituting the first temperature data as a known quantity into the expression of the heat transfer coefficient; The error heat transfer value is solved for as the only unknown.
于本发明的一实施例中,所述传热系数的表达式为:所述第一温度数据包括第一初始温度和不同时刻对应的第一测定温度,所述温差为所述预设时间段内最后时刻的第一测定温度与所述初始温度的差值。In one embodiment of the present invention, the expression of the heat transfer coefficient is: The first temperature data includes a first initial temperature and corresponding first measured temperatures at different times, and the temperature difference is a difference between the first measured temperature at the last moment in the preset time period and the initial temperature.
于本发明的一实施例中,所述根据所述第二温度数据、湿度数据和误差传热值评价所述待测全热交换膜的性能的步骤包括:将所述第二温度数据和误差传热值作为已知量,根据所述传热系数的表达式确定所述待测全热交换膜的传热系数;将所述湿度数据作为已知量根据传质系数的表达式确定所述待测全热交换膜的传质系数;将所述第二温度数据和湿度数据作为已知量根据焓值的表达式确定所述待测全热交换膜的焓值变化曲线。In an embodiment of the present invention, the step of evaluating the performance of the total heat exchange membrane to be tested according to the second temperature data, humidity data and error heat transfer value includes: combining the second temperature data and error The heat transfer value is used as a known quantity, and the heat transfer coefficient of the total heat exchange film to be tested is determined according to the expression of the heat transfer coefficient; the humidity data is used as a known quantity to determine the described The mass transfer coefficient of the total heat exchange membrane to be tested; using the second temperature data and humidity data as known quantities to determine the enthalpy change curve of the total heat exchange membrane to be tested according to the expression of enthalpy.
于本发明的一实施例中,所述传质系数的表达式为:所述焓值的表达式为:焓值=1.01·第二温度数据+(2500+1.84·第二温度数据)·湿度数据。In one embodiment of the present invention, the expression of the mass transfer coefficient is: The expression of the enthalpy value is: enthalpy value=1.01·second temperature data+(2500+1.84·second temperature data)·humidity data.
于本发明的一实施例中,所述全热交换膜性能测试装置包括冷箱和热箱;根据所述传热系数评价所述待测全热交换膜的传热性能;根据所述传质系数评价所述待测全热交换膜的传质性能;确定所述待测全热交换膜于冷箱或热箱的箱体中初始条件下空气焓值与所述预设时间段内最后时刻空气焓值的比值;在多个所述待测全热交换膜中,对于冷箱,所述比值越小,则判定所述待测全热交换膜热湿传递性能越好;对于热箱,所述比值越大,则判定所述待测全热交换膜热湿传递性能越好。In an embodiment of the present invention, the total heat exchange membrane performance testing device includes a cold box and a hot box; evaluate the heat transfer performance of the total heat exchange membrane to be tested according to the heat transfer coefficient; according to the mass transfer The coefficient evaluates the mass transfer performance of the total heat exchange membrane to be tested; determines the air enthalpy value under the initial condition of the total heat exchange membrane to be tested in the box of the cold box or the hot box and the last moment in the preset time period The ratio of the air enthalpy value; among the multiple total heat exchange membranes to be tested, for a cold box, the smaller the ratio, the better the heat and moisture transfer performance of the total heat exchange membrane to be tested; for a hot box, The larger the ratio, the better the heat and moisture transfer performance of the total heat exchange membrane to be tested.
于本发明的一实施例中,在所述误差传热值、传热系数、传质系数和焓值的确定过程中,对所述第一温度数据、第二温度数据和湿度数据进行多次测量取平均值。In an embodiment of the present invention, in the process of determining the error heat transfer value, heat transfer coefficient, mass transfer coefficient and enthalpy value, the first temperature data, the second temperature data and the humidity data are performed multiple times The measurements are averaged.
本发明又一方面提供一种全热交换膜的性能测试系统,所述全热交换膜的性能测试系统包括:第一获取模块,用于当已知热阻的全热交换膜放于全热交换膜性能测试装置时,获取预设时间段内的第一温度数据;误差模块,用于根据所述第一温度数据确定误差传热值;第二获取模块,用于当待测全热交换膜放于所述全热交换膜性能测试装置时,获取预设时间段内的第二温度数据和湿度数据;所述待测全热交换膜为未知热阻的全热交换膜;性能评价模块,用于根据所述第二温度数据、湿度数据和误差传热值评价所述待测全热交换膜的性能。Yet another aspect of the present invention provides a performance testing system for a total heat exchange membrane. The performance testing system for a total heat exchange membrane includes: a first acquisition module, used for when a total heat exchange membrane with known thermal resistance is placed in a total heat exchange When the exchange membrane performance testing device is used, the first temperature data within a preset time period is obtained; the error module is used to determine the error heat transfer value according to the first temperature data; the second acquisition module is used for when the total heat exchange to be tested When the film is placed in the total heat exchange membrane performance testing device, the second temperature data and humidity data within a preset time period are obtained; the total heat exchange film to be tested is a total heat exchange film with unknown thermal resistance; the performance evaluation module , for evaluating the performance of the total heat exchange membrane to be tested according to the second temperature data, humidity data and error heat transfer value.
本发明另一方面提供一种介质,其上存储有计算机程序,该计算机程序被处理器执行时实现所述的全热交换膜的性能测试方法。Another aspect of the present invention provides a medium on which a computer program is stored, and when the computer program is executed by a processor, the method for testing the performance of the total heat exchange membrane is realized.
本发明最后一方面提供一种设备,包括:处理器及存储器;所述存储器用于存储计算机程序,所述处理器用于执行所述存储器存储的计算机程序,以使所述设备执行所述的全热交换膜的性能测试方法。The last aspect of the present invention provides a device, including: a processor and a memory; the memory is used to store a computer program, and the processor is used to execute the computer program stored in the memory, so that the device executes the overall Performance test methods for heat exchange membranes.
如上所述,本发明所述的全热交换膜的性能测试方法、系统、介质及设备,具有以下有益效果:As mentioned above, the performance testing method, system, medium and equipment of the total heat exchange membrane according to the present invention have the following beneficial effects:
(1)解决了现有规范中关于材料传热传质性能耦合测试问题;(2)考虑了对流换热在内的全热交换膜试件的总传热效率,不仅局限于试件本身的导热系数;(3)测试时间短,测试流程简单,并且测试结果准确。(1) Solve the coupling test problem of material heat and mass transfer performance in the existing code; (2) The total heat transfer efficiency of the total heat exchange membrane specimen considering the convective heat transfer is not limited to the specimen itself Thermal conductivity; (3) The test time is short, the test process is simple, and the test results are accurate.
附图说明Description of drawings
图1显示为本发明所应用的全热交换膜性能测试装置的正视图。Fig. 1 shows the front view of the total heat exchange membrane performance testing device applied in the present invention.
图2显示为本发明所应用的全热交换膜性能测试装置的俯视图。Fig. 2 is a top view of the total heat exchange membrane performance testing device applied in the present invention.
图3显示为本发明的全热交换膜的性能测试方法于一实施例中的全热交换膜夹具示意图。FIG. 3 shows a schematic diagram of a total heat exchange membrane fixture in an embodiment of the performance test method of the total heat exchange membrane of the present invention.
图4显示为本发明所应用的全热交换膜性能测试装置的保温板示意图。Fig. 4 is a schematic diagram of a thermal insulation board of a total heat exchange membrane performance testing device applied in the present invention.
图5显示为本发明的全热交换膜的性能测试方法于一实施例中的原理流程图。FIG. 5 is a flow chart showing the principle of the performance testing method of the total heat exchange membrane in an embodiment of the present invention.
图6显示为本发明的全热交换膜的性能测试方法于一实施例中的性能评价流程图。FIG. 6 is a flow chart showing the performance evaluation of the total heat exchange membrane performance testing method in an embodiment of the present invention.
图7显示为本发明的全热交换膜的性能测试系统于一实施例中的结构原理图。FIG. 7 is a structural schematic diagram of an embodiment of a performance testing system for a total heat exchange membrane of the present invention.
图8显示为本发明的全热交换膜的性能测试设备于一实施例中的结构连接示意图。Fig. 8 is a schematic view showing the structural connection of the performance testing equipment of the total heat exchange membrane in an embodiment of the present invention.
元件标号说明Component designation description
1 第一轴流风机1 first axial fan
2 第一风阀2 first damper
3 循环风管3 circulating duct
4 第二风阀4 Second damper
5 第二轴流风机5 Second axial fan
6 输气管6 air pipe
7 第三风阀7 Third damper
8 第一湿度自记仪8 The first humidity recorder
9 试剂盒9 kits
10 加热装置10 heating device
11 温度自记仪11 Temperature self-recorder
12 第二湿度自记仪12 Second humidity recorder
13 进气管13 intake pipe
14 排气管14 exhaust pipe
15 全热交换膜固定夹15 Total heat exchange membrane fixing clip
16 全热交换膜夹具16 Full heat exchange membrane fixture
17 全热交换膜17 Total heat exchange membrane
18 保温板18 insulation board
71 第一获取模块71 First acquisition module
72 误差模块72 Error Module
73 第二获取模块73 The second acquisition module
74 性能评价模块74 performance evaluation module
81 处理器81 processors
82 存储器82 memory
83 收发器83 transceivers
84 通信接口84 communication interface
85 系统总线85 system bus
S51~S54 步骤S51~S54 steps
S541~S543 步骤S541~S543 steps
具体实施方式Detailed ways
以下通过特定的具体实例说明本发明的实施方式,本领域技术人员可由本说明书所揭露的内容轻易地了解本发明的其他优点与功效。本发明还可以通过另外不同的具体实施方式加以实施或应用,本说明书中的各项细节也可以基于不同观点与应用,在没有背离本发明的精神下进行各种修饰或改变。需说明的是,在不冲突的情况下,以下实施例及实施例中的特征可以相互组合。Embodiments of the present invention are described below through specific examples, and those skilled in the art can easily understand other advantages and effects of the present invention from the content disclosed in this specification. The present invention can also be implemented or applied through other different specific implementation modes, and various modifications or changes can be made to the details in this specification based on different viewpoints and applications without departing from the spirit of the present invention. It should be noted that, in the case of no conflict, the following embodiments and features in the embodiments can be combined with each other.
需要说明的是,以下实施例中所提供的图示仅以示意方式说明本发明的基本构想,遂图式中仅显示与本发明中有关的组件而非按照实际实施时的组件数目、形状及尺寸绘制,其实际实施时各组件的型态、数量及比例可为一种随意的改变,且其组件布局型态也可能更为复杂。It should be noted that the diagrams provided in the following embodiments are only schematically illustrating the basic ideas of the present invention, and only the components related to the present invention are shown in the diagrams rather than the number, shape and shape of the components in actual implementation. Dimensional drawing, the type, quantity and proportion of each component can be changed arbitrarily during actual implementation, and the component layout type may also be more complicated.
本发明提供了一种全热交换膜热湿性能测试方法,能够对全热交换膜的热湿性能进行快速评价,解决目前国内外规范中对于全热交换膜材料评价缺失,考虑空气流动对传热传湿影响,并实现全热交换膜热湿耦合测试。The invention provides a method for testing the heat and humidity performance of a total heat exchange membrane, which can quickly evaluate the heat and humidity performance of a total heat exchange membrane, and solves the lack of evaluation of total heat exchange membrane materials in the current domestic and foreign standards, considering the impact of air flow on heat transfer. The influence of heat and moisture transfer, and realize the heat and humidity coupling test of the total heat exchange membrane.
以下将结合图1至图8详细阐述本实施例的一种全热交换膜的性能测试方法、系统、介质及设备的原理及实施方式,使本领域技术人员不需要创造性劳动即可理解本实施例的全热交换膜的性能测试方法、系统、介质及设备。The principle and implementation of a performance testing method, system, medium and equipment of a total heat exchange membrane of this embodiment will be described in detail below in conjunction with FIGS. 1 to 8, so that those skilled in the art can understand this embodiment without creative work. The performance test method, system, medium and equipment of the total heat exchange membrane of the example.
请参阅图1至图3,分别显示为本发明所应用的全热交换膜性能测试装置的正视图、本发明所应用的全热交换膜性能测试装置的俯视图和本发明的全热交换膜的性能测试方法于一实施例中的全热交换膜夹具示意图。如图1至图3所示,整个装置的箱体包括冷箱和热箱,冷箱和热箱之间连接有全热交换膜夹具,全热交换膜在具体实施例中称为全热交换膜试件,全热交换膜试件采用相应测试装置进行热湿性能测试的准备工作如下:第一,打开测试装置盖板,将已知热阻的全热交换膜试件17放置在全热交换膜夹具16中,并用全热交换膜固定夹15进行固定。夹具两侧放置保温板18,盖上盖板,进行密封处理;第二,封闭全热交换膜性能测试装置后,关闭箱体上部循环风管3中的第一风阀2,打开箱体两侧输气管6上的第二风阀4与进气管13和排气管14上的第三风阀7;打开箱体上部温度自记仪11、第二湿度自记仪12;打开排气管14上的第一湿度自记仪8;检查试剂盒9中干燥剂与水是否充足;第三,启动输气管6中的第二轴流风机5,根据第一湿度自记仪8读数,调节进气管13插入试剂中深度,控制循环空气中含湿量,直至箱体中安装的第二湿度自记仪12显示箱体内空气湿度达到测试初始工况;第四,关闭第二轴流风机5、第二风阀4;打开箱体上部加热装置10开关,对箱体内部空气前行加热,直至箱体中安装温度自记仪11显示箱体内空气温度达到测试工况,关闭加热装置10;第五,将保温板18拉倒,打开循环风管3上的第一风阀2,启动第一轴流风机1。冷箱与热箱的箱体通过全热交换膜试件17开始传热传湿,温度自记仪11和第二湿度自记仪12实时记录两箱体温度变化;第六,测试周期结束后,根据温度自记仪11和湿度自记仪12记录数据。Please refer to Fig. 1 to Fig. 3, respectively show the front view of the total heat exchange membrane performance testing device applied in the present invention, the top view of the total heat exchange membrane performance testing device applied in the present invention and the total heat exchange membrane of the present invention The schematic diagram of the total heat exchange membrane fixture in an embodiment of the performance test method. As shown in Figures 1 to 3, the box body of the whole device includes a cold box and a hot box, and a total heat exchange film clamp is connected between the cold box and the hot box, and the full heat exchange film is called a total heat exchange film in a specific embodiment. Membrane specimens, total heat exchange membrane specimens are prepared for heat and humidity performance tests using corresponding test devices as follows: first, open the cover of the test device, and place the total heat
需要说明的是,图1至图3中未进行标号的部件若与已知标号的部件位置对称相似,则部件名称与所起的技术作用相同。It should be noted that if the unnumbered components in FIGS. 1 to 3 are symmetrically similar to the components with known numbers, the names of the components and the technical functions they perform are the same.
具体地,所述测试工况是指测试室夏季室内环境维持在24℃,相对湿度60%;冬季室内环境维持在20℃,相对湿度60%。将制冷工况与制热工况进行列表管理,形成表1测试工况表。Specifically, the test conditions refer to that the indoor environment of the test room is maintained at 24° C. and the relative humidity is 60% in summer; the indoor environment is maintained at 20° C. and the relative humidity is 60% in winter. Manage the cooling and heating working conditions in a list to form a test working condition table in Table 1.
表1.冷、热箱初始工况表Table 1. Table of initial working conditions of cold and hot boxes
需要说明的是,当已知热阻的全热交换膜试件放于全热交换膜性能测试装置时,温度自记仪11测得的是第一温度数据,当待测全热交换膜试件放于所述全热交换膜性能测试装置时,温度自记仪11测得的是第二温度数据。已知热阻的全热交换膜试件和待测全热交换膜试件放置于全热交换膜性能测试装置上进行测试之前的准备过程相同。It should be noted that when the total heat exchange membrane test piece with known thermal resistance is placed in the total heat exchange membrane performance testing device, the temperature self-
请参阅图4,显示为本发明所应用的全热交换膜性能测试装置的保温板示意图。如图4所示,保温板18用于在测试开始前放置于全热交换膜夹具16的两侧,禁止在测试开始前全热交换膜进行传热传湿。Please refer to FIG. 4 , which shows a schematic diagram of the insulation board of the total heat exchange membrane performance testing device applied in the present invention. As shown in FIG. 4 , the
请参阅图5,显示为本发明的全热交换膜的性能测试方法于一实施例中的原理流程图。本发明是根据传热传质原理提出的,在静式全热交换器中,新、排风在不同通道中进行流动,通过全热交换膜完成传热传质过程。其中显热传递是通过膜的导热以及膜与两侧流体之间对流换热进行;潜热传递则通过两侧与膜之间对流传质以及膜内部分子扩散进行。Please refer to FIG. 5 , which shows a principle flow chart of an embodiment of the performance testing method of the total heat exchange membrane of the present invention. The present invention is proposed based on the principle of heat and mass transfer. In the static total heat exchanger, fresh air and exhaust air flow in different channels, and the heat and mass transfer process is completed through the total heat exchange membrane. Among them, the sensible heat transfer is carried out through the heat conduction of the membrane and the convective heat transfer between the membrane and the fluid on both sides; the latent heat transfer is carried out through the convective mass transfer between the two sides and the membrane and the molecular diffusion inside the membrane.
由于全热交换器的全热交换膜在传热过程中,热阻来源有对流换热热阻与材料导热热阻,依靠测试全热交换膜的导热系数不能反映其传热性能,并且传质过程会对传热过程造成影响。因此,测试装置通过测试全热交换器膜传热系数与传质系数来反映其传热传质性能。Since the total heat exchange film of the total heat exchanger is in the heat transfer process, the sources of thermal resistance include convective heat transfer thermal resistance and material heat conduction thermal resistance, and the thermal conductivity of the total heat exchange film cannot reflect its heat transfer performance, and the mass transfer The process will affect the heat transfer process. Therefore, the test device reflects the heat and mass transfer performance of the total heat exchanger film by testing the heat transfer coefficient and mass transfer coefficient.
如图5所示,所述全热交换膜的性能测试方法具体包括以下几个步骤:As shown in Figure 5, the performance testing method of the total heat exchange membrane specifically includes the following steps:
S51,当已知热阻的全热交换膜放于全热交换膜性能测试装置时,获取预设时间段内的第一温度数据。S51, when the total heat exchange film with known thermal resistance is placed in the total heat exchange film performance testing device, acquire first temperature data within a preset time period.
S52,根据所述第一温度数据确定误差传热值。S52. Determine an error heat transfer value according to the first temperature data.
在本实施例中,将所述第一温度数据作为已知量代入传热系数的表达式中;将所述误差传热值作为唯一未知量进行求解。In this embodiment, the first temperature data is substituted into the expression of the heat transfer coefficient as a known quantity; the error heat transfer value is used as the only unknown quantity for solution.
具体地,所述传热系数的表达式为: Specifically, the expression of the heat transfer coefficient is:
所述第一温度数据包括第一初始温度和不同时刻对应的第一测定温度,所述温差为所述预设时间段内最后时刻的第一测定温度与所述初始温度的差值。The first temperature data includes a first initial temperature and corresponding first measured temperatures at different times, and the temperature difference is a difference between the first measured temperature at the last moment in the preset time period and the initial temperature.
在理想状态下,传热计算过程为:In an ideal state, the heat transfer calculation process is:
假设箱体绝热,所有热量通过全热交换膜从热箱传递至冷箱,且传递热量全部用于冷箱空气加热。Assuming that the box is insulated, all heat is transferred from the hot box to the cold box through the total heat exchange membrane, and all the transferred heat is used for air heating of the cold box.
q=K·A·ΔT 公式(1)q=K·A·ΔT formula (1)
公式公式(1)中,q为全热交换膜换热量,单位是W;K为全热交换膜传热系数,单位是W/(m2·℃);A为全热交换膜表面积,单位是m2;ΔT为冷热箱温差,单位是℃;t为冷热箱换热时间,单位是s。In the formula formula (1), q is the total heat exchange membrane heat transfer capacity, the unit is W; K is the total heat exchange membrane heat transfer coefficient, the unit is W/(m 2 °C); A is the total heat exchange membrane surface area, The unit is m 2 ; ΔT is the temperature difference between the hot and cold boxes, and the unit is ℃; t is the heat exchange time of the hot and cold boxes, and the unit is s.
对公式公式(1)两侧进行时间积分:Perform time integration on both sides of the formula formula (1):
∫q·dt=∫K·A·ΔT·dt 公式(2)∫q·dt=∫K·A·ΔT·dt Formula (2)
冷热箱温差是时间t的函数:The temperature difference between the hot and cold boxes is a function of time t:
ΔT=f(t) 公式(3)ΔT=f(t) Formula (3)
因此,冷箱热量Q变化为:Therefore, the heat Q change of the cold box is:
Q=c·m·ΔTn=K·A·∫f(t)·dt 公式(4)Q=c·m·ΔT n =K·A·∫f(t)·dt Formula (4)
传热系数K:Heat transfer coefficient K:
公式(5)中,ΔTn为冷箱测定温度与初始温度差,单位是℃;t0为达到测定温度所需时间,单位是s;c为空气定容比热容,单位是J/(kg·℃);m为冷箱空气质量,单位是kg。In formula (5), ΔT n is the difference between the measured temperature and the initial temperature of the cold box, in °C; t 0 is the time required to reach the measured temperature, in s; c is the specific heat capacity of air at constant volume, in J/(kg· ℃); m is the air mass of the cold box, the unit is kg.
实际情况中,冷箱空气温度的变化不仅是由于通过全热交换膜的传热Q1,还与通过夹层的传热Q2以及箱体与外界之间传热Q3有关。因此,冷箱温度上升所需的热量为三者之和。In practice, the change of air temperature in the cold box is not only due to the heat transfer Q 1 through the total heat exchange membrane, but also related to the heat transfer Q 2 through the interlayer and the heat transfer Q 3 between the box and the outside world. Therefore, the heat required to raise the temperature of the cold box is the sum of the three.
Q=Q1+Q2+Q3=c·m·ΔTn 公式(6)Q=Q 1 +Q 2 +Q 3 =c·m·ΔT n Formula (6)
用已知均质试件以不同的箱体壁温进行稳态测定,获得箱体内壁电阻输出热量与Q3的关系。对于给定装置,Q2大体上是试件厚度、试件热阻和框架结构的函数。用已知均质试件在稳态下测试得到Q2标定系数。Use known homogeneous specimens to conduct steady-state measurements with different box wall temperatures, and obtain the relationship between the output heat of the box inner wall resistance and Q 3 . For a given setup, Q2 is roughly a function of specimen thickness, specimen thermal resistance, and frame construction. The Q 2 calibration coefficient is obtained by testing a known homogeneous specimen in a steady state.
S53,当待测全热交换膜放于所述全热交换膜性能测试装置时,获取预设时间段内的第二温度数据和湿度数据;所述待测全热交换膜为未知热阻的全热交换膜。S53, when the total heat exchange film to be tested is placed in the total heat exchange film performance testing device, acquire second temperature data and humidity data within a preset time period; the total heat exchange film to be tested is of unknown thermal resistance Full heat exchange membrane.
S54,根据所述第二温度数据、湿度数据和误差传热值评价所述待测全热交换膜的性能。S54. Evaluate the performance of the total heat exchange membrane to be tested according to the second temperature data, humidity data and error heat transfer value.
请参阅图6,显示为本发明的全热交换膜的性能测试方法于一实施例中的性能评价流程图。如图6所示,S54包括:Please refer to FIG. 6 , which shows a performance evaluation flow chart of an embodiment of the performance testing method of the total heat exchange membrane of the present invention. As shown in Figure 6, S54 includes:
S541,将所述第二温度数据和误差传热值作为已知量,根据所述传热系数的表达式确定所述待测全热交换膜的传热系数。S541. Using the second temperature data and the error heat transfer value as known quantities, determine the heat transfer coefficient of the total heat exchange film to be tested according to the expression of the heat transfer coefficient.
S542,将所述湿度数据作为已知量根据传质系数的表达式确定所述待测全热交换膜的传质系数。S542, using the humidity data as a known quantity to determine the mass transfer coefficient of the total heat exchange membrane to be tested according to the expression of the mass transfer coefficient.
在本实施例中,所述传质系数的表达式为: In this embodiment, the expression of the mass transfer coefficient is:
理想状态传质计算:Ideal state mass transfer calculation:
md=Km·A·Δd·ρair 公式(8)m d =K m ·A·Δd·ρ air formula (8)
冷热箱空气含湿量差是时间t的函数:The difference in humidity between the hot and cold box air is a function of time t:
Δd=g(t) 公式(9)Δd=g(t) Formula (9)
因此,冷箱空气含湿量M变化为:Therefore, the change of the humidity M of the air in the cold box is:
M=m·Δdn=Km·A·ρair·∫g(t)·dt 公式(10)M=m·Δd n =K m ·A·ρ air ·∫g(t)·dt Formula (10)
传质系数Km为:The mass transfer coefficient K m is:
公式公式(8)-(11)中,Km为全热交换膜传质系数,单位是m/s;m为冷箱空气质量,单位是kg;△d表示当前时间点与下一个时间点冷(热)箱空气湿度的差值,单位是g/kg(干空气);t0为达到测定湿度需时间,单位是s;Δdn为冷箱测定湿度与初始湿度差,单位是g/kg(干空气);A为全热交换膜表面积,单位是m2;ρair为干空气密度,单位是kg/m3。In the formula (8)-(11), K m is the mass transfer coefficient of the total heat exchange membrane, the unit is m/s; m is the air mass of the cold box, the unit is kg; △d represents the current time point and the next time point The difference between the air humidity of the cold (hot) box, the unit is g/kg (dry air); t 0 is the time required to reach the measured humidity, the unit is s; Δd n is the difference between the measured humidity and the initial humidity of the cold box, the unit is g/ kg (dry air); A is the surface area of the total heat exchange membrane, in m 2 ; ρ air is the density of dry air, in kg/m 3 .
需要说明的是,冷箱与热箱的空气质量存在细微差别,本发明中将冷箱空气质量与热箱空气质量视作相等,箱体的空气质量为空气密度与箱体体积的乘积,其中,空气密度由公知常识可查表得知,为已知量,箱体给定之后,箱体体积也为已知量。It should be noted that there is a slight difference between the air quality of the cold box and the hot box. In the present invention, the air quality of the cold box and the air quality of the hot box are regarded as equal, and the air quality of the box is the product of the air density and the volume of the box, where , the air density can be known from the common knowledge table, which is a known quantity. After the box is given, the volume of the box is also a known quantity.
S543,将所述第二温度数据和湿度数据作为已知量根据焓值的表达式确定所述待测全热交换膜的焓值变化曲线。S543. Using the second temperature data and humidity data as known quantities, determine an enthalpy change curve of the total heat exchange membrane to be tested according to an expression of enthalpy.
在本实施例中,所述焓值的表达式为:In this embodiment, the expression of the enthalpy value is:
焓值=1.01·第二温度数据+(2500+1.84·第二温度数据)·湿度数据。Enthalpy value=1.01·second temperature data+(2500+1.84·second temperature data)·humidity data.
读取冷、热箱中安装温湿度自记仪数据,在测试结束后,获得箱体中空气温湿度变化曲线。计算绘制得冷、热箱体空气焓值随时间变化曲线,计算公式如下:Read the data of the temperature and humidity self-recorder installed in the cold and hot boxes, and obtain the change curve of the air temperature and humidity in the box after the test. Calculate and draw the time-varying curve of the air enthalpy of the cold and hot box, the calculation formula is as follows:
i'=1.01T'+(2500+1.84T')·d' 公式(6)i'=1.01T'+(2500+1.84T')·d' formula (6)
公式(7)中,i'表示空气焓值,单位是kJ/kg;T'表示空气温度,单位是℃;d'表示空气含湿量,单位是kg/kg(干空气)。In the formula (7), i' represents the air enthalpy value, the unit is kJ/kg; T' represents the air temperature, the unit is ℃; d' represents the air moisture content, the unit is kg/kg (dry air).
具体地,在性能评价过程中,所述全热交换膜性能测试装置包括冷箱和热箱。Specifically, in the performance evaluation process, the total heat exchange membrane performance testing device includes a cold box and a hot box.
根据所述传热系数评价所述待测全热交换膜的传热性能。The heat transfer performance of the total heat exchange membrane to be tested is evaluated according to the heat transfer coefficient.
根据所述传质系数评价所述待测全热交换膜的传质性能。The mass transfer performance of the total heat exchange membrane to be tested is evaluated according to the mass transfer coefficient.
确定所述待测全热交换膜于冷箱或热箱的箱体中初始条件下空气焓值与所述预设时间段内最后时刻空气焓值的比值。Determine the ratio of the air enthalpy value at the initial condition of the total heat exchange film to be tested in the box of the cold box or the hot box to the air enthalpy value at the last moment in the preset time period.
在多个所述待测全热交换膜中,对于冷箱,所述比值越小,则判定所述待测全热交换膜热湿传递性能越好;对于热箱,所述比值越大,则判定所述待测全热交换膜热湿传递性能越好。Among the multiple total heat exchange membranes to be tested, for a cold box, the smaller the ratio, the better the heat and moisture transfer performance of the total heat exchange membrane to be tested; for a hot box, the larger the ratio, Then it is judged that the heat and moisture transfer performance of the total heat exchange membrane to be tested is better.
在本实施例中,所述预设时间段是指测试周期。测试周期的计算过程如下:In this embodiment, the preset time period refers to a test period. The calculation process of the test cycle is as follows:
根据传热时间来确定测试周期。假设在理想状态下,所有热量通过全热交换膜传递,冷、热箱空气温度均匀,热箱空气温度为T1,冷箱空气温度为T2。The test period is determined according to the heat transfer time. Assuming that in an ideal state, all heat is transferred through the total heat exchange membrane, the air temperature of the cold box and the hot box are uniform, the air temperature of the hot box is T 1 , and the air temperature of the cold box is T 2 .
全热交换膜单位时刻传递热量:Total heat exchange membrane transfers heat per unit time:
q=K·A·ΔT 公式(8)q=K·A·ΔT formula (8)
冷、热箱温度变化:Cold and hot box temperature change:
对公式(12)积分得:Integrate formula (12) to get:
公式(14)中,ΔT0为冷热箱初始温差,单位是℃;按照等温流体外掠平板层流换热经验公式,估算全热交换膜长度下的对流换热系数,从而估算得全热交换膜传热系数K,估算测试时间t。In formula (14), ΔT 0 is the initial temperature difference between the hot and cold tanks, in °C; according to the empirical formula of isothermal fluid laminar heat transfer in a sweeping flat plate, the convective heat transfer coefficient under the total heat exchange membrane length is estimated, and the total heat transfer coefficient is estimated. Exchange membrane heat transfer coefficient K, estimated test time t.
进一步地,在所述误差传热值、传热系数、传质系数和焓值的确定过程中,对所述第一温度数据、第二温度数据和湿度数据进行多次测量取平均值。Further, in the process of determining the error heat transfer value, heat transfer coefficient, mass transfer coefficient and enthalpy value, the first temperature data, the second temperature data and humidity data are measured multiple times to obtain an average value.
以下将结合图示对本实施例所提供的全热交换膜的性能测试系统进行详细描述。需要说明的是,应理解以下系统的各个模块的划分仅仅是一种逻辑功能的划分,实际实现时可以全部或部分集成到一个物理实体上,也可以物理上分开。且这些模块可以全部以软件通过处理元件调用的形式实现,也可以全部以硬件的形式实现,还可以部分模块通过处理元件调用软件的形式实现,部分模块通过硬件的形式实现。例如:某一模块可以为单独设立的处理元件,也可以集成在下述系统的某一个芯片中实现。此外,某一模块也可以以程序代码的形式存储于下述系统的存储器中,由下述系统的某一个处理元件调用并执行以下某一模块的功能。其它模块的实现与之类似。这些模块全部或部分可以集成在一起,也可以独立实现。这里所述的处理元件可以是一种集成电路,具有信号的处理能力。在实现过程中,上述方法的各步骤或以下各个模块可以通过处理器元件中的硬件的集成逻辑电路或者软件形式的指令完成。The performance testing system of the total heat exchange membrane provided by this embodiment will be described in detail below with reference to the diagrams. It should be noted that it should be understood that the division of the various modules of the following systems is only a division of logical functions, and may be fully or partially integrated into a physical entity or physically separated during actual implementation. Moreover, these modules can be implemented in the form of calling software through processing elements, or can be implemented in the form of hardware, or some modules can be implemented in the form of calling software through processing elements, and some modules can be implemented in the form of hardware. For example: a certain module may be a separate processing element, or it may be integrated into a certain chip of the following system. In addition, a certain module may also be stored in the memory of the system described below in the form of program code, and be called by a processing element of the system described below to execute the function of a certain module described below. The implementation of other modules is similar. All or part of these modules can be integrated together, and can also be implemented independently. The processing element mentioned here may be an integrated circuit with signal processing capability. In the implementation process, each step of the above method or the following modules can be completed by an integrated logic circuit of hardware in the processor element or an instruction in the form of software.
以下这些模块可以是被配置成实施以上方法的一个或多个集成电路,例如:一个或多个特定集成电路(Application Specific Integrated Circuit,简称ASIC),一个或多个数字信号处理器(Digital Singnal Processor,简称DSP),一个或者多个现场可编程门阵列(Field Programmable Gate Array,简称FPGA)等。当以下某个模块通过处理元件调用程序代码的形式实现时,该处理元件可以是通用处理器,如中央处理器(CentralProcessing Unit,简称CPU)或其它可以调用程序代码的处理器。这些模块可以集成在一起,以片上系统(System-on-a-chip,简称SOC)的形式实现。The following modules may be one or more integrated circuits configured to implement the above method, for example: one or more specific integrated circuits (Application Specific Integrated Circuit, referred to as ASIC), one or more digital signal processors (Digital Signal Processor , DSP for short), one or more Field Programmable Gate Arrays (Field Programmable Gate Array, FPGA for short), etc. When one of the following modules is implemented in the form of invoking program codes by a processing element, the processing element may be a general-purpose processor, such as a central processing unit (Central Processing Unit, CPU for short) or other processors that can invoke program codes. These modules can be integrated together and implemented in the form of a System-on-a-chip (SOC for short).
请参阅图7,显示为本发明的全热交换膜的性能测试系统于一实施例中的结构原理图。如图7所示,所述全热交换膜的性能测试系统7包括:第一获取模块71、误差模块72、第二获取模块73和性能评价模块74。Please refer to FIG. 7 , which is a structural principle diagram of an embodiment of a performance testing system for a total heat exchange membrane of the present invention. As shown in FIG. 7 , the performance testing system 7 of the total heat exchange membrane includes: a
所述第一获取模块71用于当已知热阻的全热交换膜放于全热交换膜性能测试装置时,获取预设时间段内的第一温度数据。The
所述误差模块72用于根据所述第一温度数据确定误差传热值。The
在本实施例中,所述误差模块72具体用于将所述第一温度数据作为已知量代入传热系数的表达式中;将所述误差传热值作为唯一未知量进行求解。In this embodiment, the
具体地,所述传热系数的表达式为:所述第一温度数据包括第一初始温度和不同时刻对应的第一测定温度,所述温差为所述预设时间段内最后时刻的第一测定温度与所述初始温度的差值。Specifically, the expression of the heat transfer coefficient is: The first temperature data includes a first initial temperature and corresponding first measured temperatures at different times, and the temperature difference is a difference between the first measured temperature at the last moment in the preset time period and the initial temperature.
所述第二获取模块73用于当待测全热交换膜放于所述全热交换膜性能测试装置时,获取预设时间段内的第二温度数据和湿度数据;所述待测全热交换膜为未知热阻的全热交换膜。The
所述性能评价模块74用于根据所述第二温度数据、湿度数据和误差传热值评价所述待测全热交换膜的性能。The
在本实施例中,所述性能评价模块74具体用于将所述第二温度数据和误差传热值作为已知量,根据所述传热系数的表达式确定所述待测全热交换膜的传热系数;将所述湿度数据作为已知量根据传质系数的表达式确定所述待测全热交换膜的传质系数;将所述第二温度数据和湿度数据作为已知量根据焓值的表达式确定所述待测全热交换膜的焓值变化曲线。In this embodiment, the
具体地,所述传质系数的表达式为:所述焓值的表达式为:焓值=1.01·第二温度数据+(2500+1.84·第二温度数据)·湿度数据。Specifically, the expression of the mass transfer coefficient is: The expression of the enthalpy value is: enthalpy value=1.01·second temperature data+(2500+1.84·second temperature data)·humidity data.
具体地,所述全热交换膜性能测试装置包括冷箱和热箱;所述性能评价模块74用于根据所述传热系数评价所述待测全热交换膜的传热性能;根据所述传质系数评价所述待测全热交换膜的传质性能;确定所述待测全热交换膜于冷箱或热箱的箱体中初始条件下空气焓值与所述预设时间段内最后时刻空气焓值的比值;在多个所述待测全热交换膜中,对于冷箱,所述比值越小,则判定所述待测全热交换膜热湿传递性能越好;对于热箱,所述比值越大,则判定所述待测全热交换膜热湿传递性能越好。Specifically, the total heat exchange membrane performance testing device includes a cold box and a hot box; the
本实施例提供一种计算机存储介质,其上存储有计算机程序,该计算机程序被处理器执行时实现所述全热交换膜的性能测试方法。This embodiment provides a computer storage medium, on which a computer program is stored, and when the computer program is executed by a processor, the method for testing the performance of the total heat exchange membrane is realized.
本领域普通技术人员可以理解:实现上述各方法实施例的全部或部分步骤可以通过计算机程序相关的硬件来完成。前述的计算机程序可以存储于一计算机可读存储介质中。该程序在执行时,执行包括上述各方法实施例的步骤;而前述的计算机可读存储介质包括:ROM、RAM、磁碟或者光盘等各种可以存储程序代码的计算机存储介质。Those of ordinary skill in the art can understand that all or part of the steps for implementing the above method embodiments can be completed by hardware related to computer programs. The aforementioned computer program can be stored in a computer-readable storage medium. When the program is executed, it executes the steps of the above-mentioned method embodiments; and the aforementioned computer-readable storage medium includes: ROM, RAM, magnetic disk or optical disk and other computer storage media that can store program codes.
请参阅图8,显示为本发明的全热交换膜的性能测试设备于一实施例中的结构连接示意图。如图8所示,本实施例提供一种设备8,所述设备8包括:处理器81、存储器82、收发器83、通信接口84或/和系统总线85;存储器82和通信接口84通过系统总线85与处理器81和收发器83连接并完成相互间的通信,存储器82用于存储计算机程序,通信接口84用于和其他设备进行通信,处理器81和收发器83用于运行计算机程序,使所述设备执行所述全热交换膜的性能测试方法的各个步骤。Please refer to FIG. 8 , which is a schematic structural connection diagram of an embodiment of the performance testing equipment of the total heat exchange membrane of the present invention. As shown in FIG. 8 , the present embodiment provides a
上述提到的系统总线85可以是外设部件互连标准(PeripheralComponentInterconnect,简称PCI)总线或扩展工业标准结构(ExtendedIndustryStandardArchitecture,简称EISA)总线等。该系统总线85可以分为地址总线、数据总线、控制总线等。通信接口用于实现数据库访问装置与其他设备(如客户端、读写库和只读库)之间的通信。存储器可能包含随机存取存储器(RandomAccessMemory,简称RAM),也可能还包括非易失性存储器(non-volatilememory),例如至少一个磁盘存储器。The system bus 85 mentioned above may be a Peripheral Component Interconnect (PCI for short) bus or an Extended Industry Standard Architecture (EISA for short) bus or the like. The system bus 85 can be divided into address bus, data bus, control bus and so on. The communication interface is used to realize the communication between the database access device and other devices (such as client, read-write library and read-only library). The memory may include a random access memory (Random Access Memory, RAM for short), and may also include a non-volatile memory (non-volatile memory), such as at least one disk memory.
上述的处理器81可以是通用处理器,包括中央处理器(CentralProcessingUnit,简称CPU)、网络处理器(NetworkProcessor,简称NP)等;还可以是数字信号处理器(DigitalSignalProcessing,简称DSP)、专用集成电路(扫描应用程序licationSpecificIntegratedCircuit,简称ASIC)、现场可编程门阵列(FieldProgrammableGateArray,简称FPGA)或者其他可编程逻辑器件、分立门或者晶体管逻辑器件、分立硬件组件。Above-mentioned
本发明所述的全热交换膜的性能测试方法的保护范围不限于本实施例列举的步骤执行顺序,凡是根据本发明的原理所做的现有技术的步骤增减、步骤替换所实现的方案都包括在本发明的保护范围内。The scope of protection of the performance test method of the total heat exchange membrane described in the present invention is not limited to the execution order of the steps listed in this embodiment, any scheme realized by adding or subtracting steps or replacing steps in the prior art according to the principle of the present invention All are included in the scope of protection of the present invention.
本发明还提供一种全热交换膜的性能测试系统,所述全热交换膜的性能测试系统可以实现本发明所述的全热交换膜的性能测试方法,但本发明所述的全热交换膜的性能测试方法的实现装置包括但不限于本实施例列举的全热交换膜的性能测试系统的结构,凡是根据本发明的原理所做的现有技术的结构变形和替换,都包括在本发明的保护范围内。The present invention also provides a performance testing system of a total heat exchange membrane, which can realize the performance testing method of a total heat exchange membrane described in the present invention, but the total heat exchange membrane described in the present invention The device for realizing the performance test method of the membrane includes but is not limited to the structure of the performance test system of the total heat exchange membrane listed in this embodiment. within the scope of protection of the invention.
综上所述,本发明所述全热交换膜的性能测试方法、系统、介质及设备提供了一种全热交换膜热湿性能测试方法,能够对全热交换膜的热湿性能进行快速评价,解决目前国内外规范中对于全热交换膜材料评价缺失,考虑空气流动对传热传湿影响,并实现全热交换膜热湿耦合测试。解决了现有规范中关于材料传热传质性能耦合测试问题;考虑了对流换热在内的全热交换膜试件的总传热效率,不仅局限于试件本身的导热系数;测试时间短,测试流程简单,并且测试结果准确。本发明有效克服了现有技术中的种种缺点而具高度产业利用价值。In summary, the performance testing method, system, medium and equipment of the total heat exchange membrane described in the present invention provide a method for testing the heat and humidity performance of the total heat exchange membrane, which can quickly evaluate the heat and humidity performance of the total heat exchange membrane , to solve the lack of evaluation of total heat exchange membrane materials in the current domestic and foreign standards, consider the influence of air flow on heat transfer and moisture transfer, and realize the heat and humidity coupling test of total heat exchange membranes. It solves the coupling test problem of heat and mass transfer performance of materials in the existing specifications; the total heat transfer efficiency of the total heat exchange membrane specimen, including convective heat transfer, is not limited to the thermal conductivity of the specimen itself; the test time is short , the test process is simple and the test results are accurate. The invention effectively overcomes various shortcomings in the prior art and has high industrial application value.
上述实施例仅例示性说明本发明的原理及其功效,而非用于限制本发明。任何熟悉此技术的人士皆可在不违背本发明的精神及范畴下,对上述实施例进行修饰或改变。因此,举凡所属技术领域中具有通常知识者在未脱离本发明所揭示的精神与技术思想下所完成的一切等效修饰或改变,仍应由本发明的权利要求所涵盖。The above-mentioned embodiments only illustrate the principles and effects of the present invention, but are not intended to limit the present invention. Anyone skilled in the art can modify or change the above-mentioned embodiments without departing from the spirit and scope of the present invention. Therefore, all equivalent modifications or changes made by those skilled in the art without departing from the spirit and technical ideas disclosed in the present invention should still be covered by the claims of the present invention.
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