CN106885634A - Unsteady wall heating heat flux distribution measuring method based on infrared thermal imagery thermometry - Google Patents
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- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
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Abstract
Description
技术领域technical field
本发明涉及一种壁面受热热流分布测量方法,尤其涉及一种利用红外热像测温技术测量记录壁面在加热源(如火焰、电热器、热气体等)加热时的温度场变化来计算受热热流分布的方法。The invention relates to a method for measuring the heat flow distribution of a wall surface, in particular to a method for measuring and recording the temperature field change of the wall surface when it is heated by a heating source (such as a flame, an electric heater, hot gas, etc.) by using infrared thermal image temperature measurement technology to calculate the heat flow method of distribution.
背景技术Background technique
目前壁面热流测量的方法主要有三种:(1)采用电阻式温度传感器,通过输出的电信号得到已知电阻的温度梯度,利用傅里叶定律,计算壁面热流,例如柱塞式热流计;(2)采用热电偶式温度传感器,通过测量表面温差实现热流测量,例如薄膜热电偶;(3)是利用量热元件吸入热量,测量量热元件的平均温度变化率,再计算表面热流率,例如塞形铜箔量热计。At present, there are three main methods for measuring wall heat flow: (1) using a resistive temperature sensor, obtaining the temperature gradient of known resistance through the output electrical signal, and using Fourier's law to calculate the wall heat flow, such as a plunger heat flow meter; 2) Thermocouple temperature sensors are used to measure heat flow by measuring surface temperature differences, such as thin-film thermocouples; (3) calorimetric elements are used to absorb heat, and the average temperature change rate of calorimetric elements is measured, and then the surface heat flow rate is calculated, such as Plug-shaped copper foil calorimeter.
现有的壁面热流测量方法都是一次测量一个点的热流强度,不能解决整块区域内的实时热流分布问题;而且需要接触测量,其精度由热流传感器与被测物粘贴紧密程度、热流传感器厚度、热流传感器边长决定,对于某些复杂的结构来说传感器的安装较为不便。The existing wall heat flow measurement method is to measure the heat flow intensity of one point at a time, which cannot solve the problem of real-time heat flow distribution in the entire area; moreover, contact measurement is required, and its accuracy depends on the tightness of the heat flow sensor and the measured object, the thickness of the heat flow sensor 1. The side length of the heat flow sensor is determined. For some complex structures, the installation of the sensor is inconvenient.
发明内容Contents of the invention
本发明的目的在于针对目前技术的不足,提供一种非接触式基于红外热像测温技术的非定常壁面加热热流分布测量方法。The purpose of the present invention is to provide a non-contact method for measuring heat flow distribution of unsteady wall heating based on infrared thermal image temperature measurement technology in view of the deficiencies of the current technology.
本发明的目的是通过以下技术方案来实现的,一种非接触式基于红外热像测温技术的非定常壁面加热热流分布测量方法,具体步骤如下,The purpose of the present invention is achieved through the following technical solutions, a non-contact method for measuring the heat flow distribution of unsteady wall heating based on infrared thermal imaging temperature measurement technology, the specific steps are as follows,
(1)选择密度、比热容和热传导系数已知的物体,壁厚均匀,可近似成平板,其Bi数远小于1,利用红外测温技术记录随时间变化的加热壁面的温度场;(1) Select an object with known density, specific heat capacity and thermal conductivity. The wall thickness is uniform and can be approximated as a flat plate. The Bi number is much smaller than 1. Use infrared temperature measurement technology to record the temperature field of the heating wall surface that changes with time;
(2)由于Bi数远小于1,则忽略壁面厚度方向热阻,将物体加热问题简化成二维非定常传热问题,得到非定常热平衡方程;(2) Since the Bi number is much smaller than 1, the thermal resistance in the thickness direction of the wall is ignored, and the object heating problem is simplified into a two-dimensional unsteady heat transfer problem, and the unsteady heat balance equation is obtained;
(3)将步骤1)中测量得到的温度场对时间和空间分别求导,计算热温升非定常项和热传导项,忽略自然对流和热辐射,根据步骤2)的非定常热平衡方程计算加热热流。(3) Differentiate the temperature field measured in step 1) with respect to time and space, calculate the unsteady term of thermal temperature rise and the term of heat conduction, ignore natural convection and heat radiation, and calculate the heating according to the unsteady heat balance equation in step 2) heat flow.
上述技术方案中,进一步的,所述的步骤1)具体为:利用红外测温技术记录物体壁面随时间变化的温度场,记录过程从初始加热时刻开始到物体温度基本不变。In the above technical solution, further, the step 1) specifically includes: using infrared temperature measurement technology to record the temperature field of the wall surface of the object changing with time, and the recording process is basically unchanged from the initial heating moment to the temperature of the object.
进一步的,所述的步骤2)具体为:由于物体Bi数远小于1,可采用集中参数法,忽略沿厚度方向的热阻,认为物体两个表面沿厚度方向基本不存在温差,将物体加热问题简化成二维非定常传热问题,得到非定常热平衡方程,即Further, the step 2) is specifically: since the Bi number of the object is much smaller than 1, the lumped parameter method can be used, ignoring the thermal resistance along the thickness direction, considering that there is basically no temperature difference between the two surfaces of the object along the thickness direction, and heating the object The problem is simplified into a two-dimensional unsteady heat transfer problem, and the unsteady heat balance equation is obtained, namely
热温升非定常项=热传导项+热源项+自然对流项+辐射项Thermal temperature rise unsteady item = heat conduction item + heat source item + natural convection item + radiation item
方程包含有5个项,从左到右依次是壁面温度由于加热导致的随时间变化的非定常项,壁面自身的热传导项,加热热源项,自然对流项和辐射项。The equation contains 5 terms, from left to right are the time-varying unsteady term of the wall temperature due to heating, the heat conduction term of the wall itself, the heating heat source term, the natural convection term and the radiation term.
进一步的,所述的步骤3)具体为:将通过红外测温技术测量得到的壁面温度场对时间求导,再乘上已知的壁面材料的密度和比热容参数,计算得到非定常项;将壁面温度场对空间求导,乘以壁面的热传导系数,计算得到热传导项。经实验测试发现,往往在加热初期,壁面温度不高,自然对流项和辐射项都比较小,与平均加热热流强度值相差至少2个数量级,因此自然对流和辐射散热项可以忽略。Further, the step 3) is specifically: deriving the temperature field of the wall surface measured by infrared temperature measurement technology with respect to time, and then multiplying the known density and specific heat capacity parameters of the wall surface material to obtain the unsteady item; The temperature field of the wall surface is derived from the space, multiplied by the heat conduction coefficient of the wall surface, and the heat conduction term is calculated. Experimental tests have found that in the early stage of heating, the wall temperature is not high, and the natural convection and radiation items are relatively small, which are at least 2 orders of magnitude different from the average heating heat flux intensity value, so the natural convection and radiation heat dissipation items can be ignored.
本发明的有益效果是,本发明通过红外热像技术记录壁面整块区域内随时间变化的温度场,再将温度场对空间和时间求导,计算非定常热平衡方程,得到测量区域内的实时瞬态的加热热流分布。不同于现有的壁面热流传感器需要接触壁面,该方法实现非接触式测量,可适用于各种复杂壁面的热流测量。同时现有的壁面热流传感器在同一时刻只能测量壁面的一个点的热流值,本发明则可以同时测量一个二维区域的热流分布,极大的提高了测量效率,适用于更广泛的工程环境,具有很大的工程及生产实践意义,有很大的应用前景。The beneficial effect of the present invention is that the present invention records the temperature field changing with time in the entire area of the wall through infrared thermal imaging technology, and then derivates the temperature field with respect to space and time, calculates the unsteady heat balance equation, and obtains the real-time temperature in the measurement area. Transient heating heat flow distribution. Different from the existing wall heat flow sensor which needs to contact the wall, the method realizes non-contact measurement and is applicable to the heat flow measurement of various complex walls. At the same time, the existing wall heat flow sensor can only measure the heat flow value of one point on the wall at the same time, but the present invention can simultaneously measure the heat flow distribution in a two-dimensional area, which greatly improves the measurement efficiency and is applicable to a wider range of engineering environments , has great engineering and production practical significance, and has great application prospects.
附图说明Description of drawings
下面结合附图和实施例对本发明做进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.
图1为测量装置示意图;Figure 1 is a schematic diagram of the measuring device;
图2为本发明具体实例方法的流程图;Fig. 2 is the flowchart of specific example method of the present invention;
图3为不同加热源分别加热时的三个时刻的温度场分布;Fig. 3 is the temperature field distribution at three moments when different heating sources are heated separately;
图4为不同加热源分别加热时某一时刻对应的热流图;Figure 4 is a heat flow diagram corresponding to a certain moment when different heating sources are heated separately;
图中1.加热源 2.受热平板(半径为R,直径为d) 3.红外热像仪 4.图形处理器。In the figure 1. Heating source 2. Heating plate (radius R, diameter d) 3. Infrared thermal imaging camera 4. Graphics processor.
具体实施方式detailed description
本发明是基于红外热像测温技术的非定常壁面加热热流分布测量方法,具体步骤如下:The present invention is an unsteady wall surface heating heat flow distribution measurement method based on infrared thermal image temperature measurement technology, and the specific steps are as follows:
1、选择密度、比热容和热传导系数已知的物体,壁厚均匀,可近似成平板,其Bi数(毕渥数)远小于1,利用红外测温技术记录随时间变化的加热壁面的温度场:1. Select an object with known density, specific heat capacity and thermal conductivity. The wall thickness is uniform and can be approximated as a flat plate. :
利用红外测温技术记录物体壁面随时间变化的温度场,记录过程从初始加热时刻开始到物体温度基本不变。The infrared temperature measurement technology is used to record the temperature field of the wall surface of the object changing with time, and the recording process starts from the initial heating moment to the temperature of the object being basically unchanged.
2、由于Bi数远小于1,则忽略壁面厚度方向热阻,将物体加热问题简化成二维非定常传热问题,得到非定常热平衡方程;2. Since the Bi number is much smaller than 1, the thermal resistance in the thickness direction of the wall is ignored, and the heating problem of the object is simplified into a two-dimensional unsteady heat transfer problem, and the unsteady heat balance equation is obtained;
物体Bi数远小于1,则可采用集中参数法,忽略沿厚度方向的热阻,认为物体两个表面沿厚度方向基本不存在温差,将物体加热问题简化成二维非定常传热问题,得到非定常热平衡方程,即If the Bi number of the object is much smaller than 1, the lumped parameter method can be used, ignoring the thermal resistance along the thickness direction, and considering that there is basically no temperature difference between the two surfaces of the object along the thickness direction, and simplifying the object heating problem into a two-dimensional unsteady heat transfer problem, we get The unsteady heat balance equation, namely
热温升非定常项=热传导项+热源项+自然对流项+辐射项Thermal temperature rise unsteady item = heat conduction item + heat source item + natural convection item + radiation item
方程包含有5个项,从左到右依次是壁面温度由于加热导致的随时间变化的非定常项,壁面自身的热传导项,加热热源项,自然对流项和辐射项。The equation contains 5 terms, from left to right are the time-varying unsteady term of the wall temperature due to heating, the heat conduction term of the wall itself, the heating heat source term, the natural convection term and the radiation term.
3、将步骤1中测量得到的温度场对时间和空间分别求导,计算热温升非定常项和热传导项,忽略自然对流和热辐射,根据步骤2的非定常热平衡方程计算加热热流;3. Deriving the temperature field measured in step 1 with respect to time and space, calculating the unsteady item of thermal temperature rise and heat conduction item, ignoring natural convection and thermal radiation, and calculating the heating heat flow according to the unsteady heat balance equation in step 2;
将通过红外测温技术测量得到的壁面温度场对时间求导,再乘上已知的壁面材料的密度和比热容参数,计算得到非定常项;将壁面温度场对空间求导,乘以壁面的热传导系数,计算得到热传导项。经实验测试发现,往往在加热初期,壁面温度不高,自然对流项和辐射项都比较小,与平均加热热流强度值相差至少2个数量级,因此自然对流和辐射散热项可以忽略。The wall temperature field measured by infrared temperature measurement technology is derived with respect to time, and then multiplied by the known density and specific heat capacity parameters of the wall material to calculate the unsteady item; the wall temperature field is derived with respect to space, multiplied by the wall surface The heat transfer coefficient is calculated to obtain the heat conduction term. Experimental tests have found that in the early stage of heating, the wall temperature is not high, and the natural convection and radiation items are relatively small, which are at least 2 orders of magnitude different from the average heating heat flux intensity value, so the natural convection and radiation heat dissipation items can be ignored.
以下通过实施例对本发明内容做进一步解释。实验采用铝制圆形平板,厚度为2.5mm,半径为152mm,定压热容cp为880J/(kg·K),密度ρ为2700kg/m3,导热系数κp为237W/(m·K),由于壁厚只有2.5mm,而平板半径为152mm,其Bi数远小于1,沿厚度方向的热阻很小,可以忽略。平板正上方1m处放置红外成像仪,并连接图像处理器,整个实验装置如图1。加热源为电加热片,加热源1为方形加热片,而加热源2为圆形加热片,均为恒定热流加热片。按照图2所示的流程图进行实验和计算。图3是平板在不同加热器加热情况下分别在t=10s,t=15s,t=20s三个时刻的温度场分布。图4第一排是将温度场对时间求一阶导数所得到得壁面随时间变化的非定常项分布图。将温度场对二维空间求二阶导数,得到图4中间所示的空间热传导项的分布图。边界条件为均匀热流边界条件,根据自然对流经验公式和热辐射公式W=σ(ΔT)4,在加热初期,代入各项参数,计算自然对流项和热辐射项,发现其和非定常项或热传导项相差至少2个数量级,因此可以忽略自然对流项和热辐射项,从而计算得到图4最下排所示的非定常加热平板的热源分布图。The content of the present invention will be further explained below by way of examples. The experiment uses an aluminum circular plate with a thickness of 2.5mm and a radius of 152mm. The constant pressure heat capacity c p is 880J/(kg·K), the density ρ is 2700kg/m 3 , and the thermal conductivity κ p is 237W/(m· K), since the wall thickness is only 2.5mm, and the plate radius is 152mm, its Bi number is far less than 1, and the thermal resistance along the thickness direction is very small and can be ignored. An infrared imager is placed 1m above the plate and connected to an image processor. The entire experimental setup is shown in Figure 1. The heating source is an electric heating chip, the heating source 1 is a square heating chip, and the heating source 2 is a circular heating chip, all of which are constant heat flow heating chips. Experiments and calculations are carried out according to the flow chart shown in Figure 2. Fig. 3 is the distribution of the temperature field of the plate at three moments of t=10s, t=15s and t=20s under different heating conditions of the heater. The first row of Fig. 4 is the unsteady term distribution diagram of the wall surface changing with time obtained by calculating the first derivative of the temperature field with respect to time. Calculate the second order derivative of the temperature field with respect to the two-dimensional space, and obtain the distribution diagram of the space heat conduction item shown in the middle of Figure 4. The boundary condition is uniform heat flow boundary condition, according to the natural convection empirical formula and the thermal radiation formula W=σ(ΔT) 4 , in the initial stage of heating, various parameters are substituted to calculate the natural convection and thermal radiation items, and it is found that they differ from the unsteady or heat conduction items by at least 2 orders of magnitude, so the natural convection can be ignored term and heat radiation term, so as to calculate the heat source distribution diagram of the unsteady heating plate shown in the bottom row of Fig. 4.
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| CN109470363A (en) * | 2018-10-29 | 2019-03-15 | 浙江大学 | Method for measuring heat flow distribution of curved thin-wall heating based on infrared thermal imaging technology |
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