CN203396784U - Seepage flow velocity monitoring test device for porous-medium structural body - Google Patents

Seepage flow velocity monitoring test device for porous-medium structural body Download PDF

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CN203396784U
CN203396784U CN201320430347.0U CN201320430347U CN203396784U CN 203396784 U CN203396784 U CN 203396784U CN 201320430347 U CN201320430347 U CN 201320430347U CN 203396784 U CN203396784 U CN 203396784U
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seepage
optical fiber
water
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苏怀智
崔书生
杨孟
欧斌
房彬
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Hohai University HHU
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Abstract

The utility model discloses a seepage flow velocity monitoring test device for a porous-medium structural body. The seepage flow velocity monitoring test device comprises a heating system (1), a distributed optical-fiber temperature sensing system (2), a porous-medium structural body model groove (3) with embedded optical fibers and a water outlet system (4). The heating system (1), the distributed optical-fiber temperature sensing system (2) and the water outlet system (4) are connected with the porous-medium structural body model groove (3). A monitoring period is a whole optical-cable heating temperature-rising period according to the unconventional optical-fiber seepage monitoring method, a linear correlation between seepage flow velocity and an average thermal conductivity is accurately pinpointed, and monitoring precision is reliably guaranteed.

Description

多孔介质结构体渗流流速监测试验装置Seepage velocity monitoring test device for porous media structure

技术领域 technical field

本发明涉及一种多孔介质结构体渗流流速监测试验装置及方法。  The invention relates to a porous medium structure body seepage flow velocity monitoring test device and method. the

背景技术 Background technique

中央关于水利建设的一号文件,加快了我国水利事业的建设步伐,我国的土石堤坝工程面临的主要问题有渗漏、管涌、坍塌、裂缝、滑坡、护坡破坏、冲刷空蚀等。渗漏是影响堤坝安全的一个重要因素,若渗漏隐患发现的不及时、渗控措施不到位,极有可能引起渗透破坏和坝坡失稳,严重影响工程安全,甚至导致堤坝溃决。据统计,土石坝工程中,超过三分之一的破坏是由于不同程度的渗漏以及渗漏衍生的各种问题所致;堤防溃决90%以上是由于渗漏破坏造成。  The No. 1 document of the central government on water conservancy construction has accelerated the pace of my country's water conservancy construction. The main problems faced by my country's earth-rock dam projects include leakage, piping, collapse, cracks, landslides, slope protection damage, and erosion cavitation. Seepage is an important factor affecting the safety of dams. If the hidden danger of leakage is not discovered in time and the seepage control measures are not in place, it is very likely to cause seepage damage and dam slope instability, which will seriously affect the safety of the project and even cause the dam to fail. According to statistics, more than one-third of the damage in earth-rock dam projects is caused by various degrees of leakage and various problems derived from leakage; more than 90% of embankment failures are caused by leakage damage. the

大量工程经验表明,加强土石堤坝渗漏与渗透变形的实时定位和定量监测,对保障工程的安全运行具有非常重要的意义,在对传统监测技术进行不断完善和发展的同时,越来越多的新型技术被引入堤坝安全监测领域,开展新技术在坝工领域中监测原理和实现方法、技术等的研究,已成为一个热点科研课题;相对于常规的点式监测仪器的监控盲区大、易造成测值的空间不连续及漏测,分布式光纤温度传感技术分布式、连续性地实时进行堤坝渗漏监测测量已引起了工程界和学术界的高度关注,但是该技术在渗漏监测应用方面的理论还不成熟,特别是目前尚未建立光纤加热温升同渗流流速、环境温度、加热功率之间定量关系模型,因此进行土石堤坝渗流流速光纤监测理论研究和模型试验具有重要的意义。  A large amount of engineering experience shows that strengthening the real-time positioning and quantitative monitoring of seepage and seepage deformation of earth-rock dams is of great significance to ensure the safe operation of the project. While the traditional monitoring technology is continuously improved and developed, more and more New technologies have been introduced into the field of dam safety monitoring, and research on the monitoring principles, implementation methods, and technologies of new technologies in the field of dam engineering has become a hot scientific research topic; The spatial discontinuity and missing measurement of the measured value, the distributed and continuous real-time monitoring and measurement of dam leakage by distributed optical fiber temperature sensing technology have attracted great attention from the engineering and academic circles, but the application of this technology in leakage monitoring The theory is not yet mature, especially the quantitative relationship model between the temperature rise of optical fiber heating and seepage flow velocity, ambient temperature, and heating power has not been established. Therefore, it is of great significance to carry out theoretical research and model tests on the seepage flow velocity monitoring of earth-rock dams. the

发明内容 Contents of the invention

发明目的:本发明的目的在于针对现有技术的不足,提供一种高效精确的多孔介质结构体渗流流速监测试验装置。  Purpose of the invention: The purpose of the present invention is to provide an efficient and accurate monitoring test device for seepage flow velocity of porous media structures in view of the deficiencies in the prior art. the

技术方案:本发明多孔介质结构体渗流流速监测试验装置,包括加热系统、分布式光纤温度传感系统、埋设有监测光纤的多孔介质结构体模型槽和出水系统;所述加热系统、分布式光纤温度传感系统和出水系统分别与所述多孔介质结构体模型槽连接。  Technical solution: The porous media structure seepage velocity monitoring test device of the present invention includes a heating system, a distributed optical fiber temperature sensing system, a porous media structure model tank embedded with a monitoring optical fiber, and a water outlet system; the heating system, distributed optical fiber The temperature sensing system and the water outlet system are respectively connected with the model tank of the porous medium structure. the

所述加热系统为主要由交流电源、调压器和负载发热电阻丝组成的并联电路,通过负载发热电阻丝对监测光纤加热,通过调压器控制电压从而控制加热功率。  The heating system is a parallel circuit mainly composed of an AC power supply, a voltage regulator and a load heating resistance wire. The monitoring optical fiber is heated through the load heating resistance wire, and the heating power is controlled by controlling the voltage through the voltage regulator. the

所述分布式光纤温度传感系统包括分布式光纤测温主机和线性多模感温光缆,所述分布式光纤测温主机通过脉冲激光设备与所述线性多模感温光缆相连并输出光脉冲;所述线性多模感温光缆的尾部与光纤连接器相连。  The distributed optical fiber temperature sensing system includes a distributed optical fiber temperature measurement host and a linear multi-mode temperature-sensing optical cable, and the distributed optical fiber temperature measurement host is connected to the linear multi-mode temperature-sensing optical cable through a pulse laser device and outputs optical pulses ; The tail of the linear multimode temperature-sensing optical cable is connected with the optical fiber connector. the

所述出水系统包括水箱、流速控制阀、水泵及循环水池;所述水箱的位置高于所述循环水池,所述水箱的水位线上部通过溢流管与所述循环水池连接;所述循环水池通过水泵将水输送到水箱中;所述水箱底部通过管道与所述多孔介质结构体模型槽连接;所述流速控制阀分别设置在水箱与所述多孔介质结构体模型槽和循环水池之间的管道上。  The water outlet system includes a water tank, a flow rate control valve, a water pump, and a circulating pool; the position of the water tank is higher than the circulating pool, and the upper water level of the water tank is connected to the circulating pool through an overflow pipe; the circulating pool Water is transported into the water tank by a water pump; the bottom of the water tank is connected with the porous medium structure model tank through a pipeline; the flow rate control valve is respectively arranged between the water tank and the porous medium structure model tank and the circulating pool on the pipe. the

多孔介质结构体渗流流速监测试验方法,包括如下步骤:  The test method for monitoring seepage flow rate of porous media structure includes the following steps:

(1)构建埋设有监测光纤的多孔介质结构体模型槽。基于不同试验要求,根据具体设计搭建带监测光纤的多孔介质结构体模型槽。  (1) Constructing a model groove of a porous medium structure embedded with a monitoring optical fiber. Based on different test requirements, a porous medium structure model tank with monitoring optical fiber is built according to the specific design. the

(2)调整出水系统以形成均匀稳定渗流场。将出水系统阀门调节到某一确定位置,后持续监测出水系统的出流量,待出流量稳定时,认为均匀稳定渗流场已经形成。  (2) Adjust the outlet system to form a uniform and stable seepage field. Adjust the valve of the water outlet system to a certain position, and then continuously monitor the outflow of the water outlet system. When the outflow is stable, it is considered that a uniform and stable seepage field has been formed. the

(3)基于分布式光纤温度传感系统对埋设于模型槽中的监测光纤进行温度监测;拉曼散射和布里渊散射对温度均有敏感性,可以用来测量温度,考虑到布里渊散射受应力等其他因素影响较大,故主要采用拉曼散射对温度进行测。通过斯托克斯光与反斯托克斯光计算出温度值:  (3) Based on the distributed optical fiber temperature sensing system, the temperature monitoring of the monitoring optical fiber buried in the model groove is carried out; both Raman scattering and Brillouin scattering are sensitive to temperature and can be used to measure temperature. Considering Brillouin scattering It is greatly affected by other factors such as stress, so Raman scattering is mainly used to measure temperature. The temperature value is calculated by Stokes light and anti-Stokes light:

TT == hCVwxya KK [[ lnln αα -- lnln (( ll asas ll sthe s )) ]] ,,

其中,式中:las为反斯托克斯光光强;ls为斯托克斯光光强;α为温度相关系数;h为普朗克系数;C为真空中的光速;V为拉曼平移量;K为鲍尔茨曼常数;T为绝对温度值。通过上述方法可以得到光缆温度值,技术上,还需要知道该温度值对应的位置值,光时域反射技术(OTDR)可以解决该问题。通过测量入射光与反射光的时间差Δt,就可以知道反射点距发射端的距离X:

Figure DEST_PATH_GDA0000417473680000022
式中:C为真空中的光速,n为光纤的折射率。  Among them, in the formula: l as is the anti-Stokes light intensity; l s is the Stokes light intensity; α is the temperature correlation coefficient; h is the Planck coefficient; C is the speed of light in vacuum; V is Raman translation; K is the Boltzmann constant; T is the absolute temperature value. The temperature value of the optical cable can be obtained through the above method. Technically, it is also necessary to know the position value corresponding to the temperature value. Optical time domain reflectometry (OTDR) can solve this problem. By measuring the time difference Δt between the incident light and the reflected light, the distance X between the reflection point and the transmitting end can be known:
Figure DEST_PATH_GDA0000417473680000022
In the formula: C is the speed of light in vacuum, and n is the refractive index of the fiber.

(4)经分布式光纤温度传感系统监测10分钟之后,通过加热系统对目标光纤 做通电加热操作。对监测光缆中固定用钢丝利用单线热源法通电加热,其中单线热源法中均匀稳恒渗流场影响下的温度场求解模型如下:  (4) After being monitored by the distributed optical fiber temperature sensing system for 10 minutes, the target optical fiber is energized and heated through the heating system. The fixed steel wire in the monitoring optical cable is heated by the single-line heat source method, and the solution model of the temperature field under the influence of the uniform and constant seepage field in the single-line heat source method is as follows:

∂ 2 T ∂ x 2 + ∂ 2 T ∂ y 2 - d ∂ T ∂ x = 0 ( x , y ) ∈ Ω - λ ∂ T ( x , y ) ∂ n = q ( x , y ) ∈ Γ 1 T ( x , y ) = T 0 ( x , y ) ∈ Γ 0 , 式中:Ω为模型区域;Γ1为模型内边界oabc;Γ0为模型外边界OABC;λ为介质导热系数;n代表边界面某处的外法线方向。同时不断监测目标光缆的分布式温度并记录下加热功率和起始加热时刻的监测文件名,为以后整理数据提供依据。在一次监测周期完成后,改变加热功率,测得在该渗流速度下不同加热功率的温升曲线。  ∂ 2 T ∂ x 2 + ∂ 2 T ∂ the y 2 - d ∂ T ∂ x = 0 ( x , the y ) ∈ Ω - λ ∂ T ( x , the y ) ∂ no = q ( x , the y ) ∈ Γ 1 T ( x , the y ) = T 0 ( x , the y ) ∈ Γ 0 , In the formula: Ω is the model area; Γ 1 is the inner boundary oabc of the model; Γ 0 is the outer boundary OABC of the model; λ is the thermal conductivity of the medium; n represents the outer normal direction somewhere on the boundary surface. At the same time, the distributed temperature of the target optical cable is continuously monitored and the heating power and the monitoring file name of the initial heating time are recorded, so as to provide a basis for data sorting in the future. After a monitoring period is completed, the heating power is changed, and the temperature rise curve of different heating powers at the seepage velocity is measured.

单线热源法同双线热源法最大的不同在于,单线法只需要一根热源光纤即可反演出渗流流速,而双线法需要一根热源光纤和一根温度场感温光纤。在土石坝及土石堤防的渗流监测中,单线热源法只需在渗流场区域布设一根测温光纤,利用DTS测温仪测出目标光纤稳定温度T1、起始温度(即加热时的环境温度)T0以及目标光纤的加热功率q。利用上述数据即可通过单线热源法反演出渗流流速v。假定光缆埋设方向同渗流方向垂直,单线热源法中目标光纤加热产生的温度场及模型示意图见附图3,图中,a表示温度等值线,b表示目标光纤,c表示加热功率P。将建模区域选为以光缆为轴线,r为半径的空间圆柱体。在1m长度范围内的空间圆柱体内,可以将渗流速度视为不随位置变化的常量。为了确定加热光纤加热后的影响范围,进行了饱和无渗流工况的试验,得到了热源光纤在不同加热功率下的起始温度和稳定温度,利用Marc有限元分析软件中稳定温度场的分析模块,反演圆柱体的半径r,最终确定光缆为中心、边长2r=15c的正方形二维区域作为建模区域,既符合数值计算的反演结果,又符合实际的试验结果,具体反演方法见附图4。  The biggest difference between the single-line heat source method and the double-line heat source method is that the single-line method only needs one heat source fiber to invert the seepage velocity, while the two-line method requires a heat source fiber and a temperature field temperature sensing fiber. In the seepage monitoring of earth-rock dams and embankments, the single-line heat source method only needs to arrange a temperature-measuring optical fiber in the seepage field area, and use the DTS thermometer to measure the stable temperature T 1 and initial temperature of the target optical fiber (that is, the environment during heating temperature) T 0 and the heating power q of the target fiber. Using the above data, the seepage flow velocity v can be inverted by the single-line heat source method. Assuming that the cable embedding direction is perpendicular to the seepage direction, the temperature field and model diagram generated by the heating of the target fiber in the single-line heat source method are shown in Figure 3. In the figure, a represents the temperature contour, b represents the target fiber, and c represents the heating power P. The modeling area is selected as a space cylinder with the optical cable as the axis and r as the radius. In a space cylinder with a length of 1m, the seepage velocity can be regarded as a constant that does not change with the position. In order to determine the influence range of the heating fiber after heating, the test of the saturated non-seepage condition was carried out, and the initial temperature and stable temperature of the heat source fiber under different heating power were obtained, and the analysis module of the stable temperature field in the Marc finite element analysis software was used , invert the radius r of the cylinder, and finally determine the square two-dimensional area with the optical cable as the center and side length 2r=15c as the modeling area, which not only conforms to the inversion results of numerical calculations, but also conforms to actual test results. The specific inversion method See attached drawing 4.

光纤流速反演模型示意图见附图6,其中光缆被简化为1cm×1cm的正方形区域,整个模型求解区间及其剖分形式符合有限差分法的要求,所以采用有限差分法求解单线法中均匀稳恒渗流场影响下的温度场求解模型,分别记网格内点和边界点的集合分别为Ωh

Figure DEST_PATH_GDA0000417473680000032
在点(xi,yj)上用差商表示二阶导数,即:  The schematic diagram of the optical fiber flow velocity inversion model is shown in Figure 6, in which the optical cable is simplified into a square area of 1 cm × 1 cm. The entire model solution interval and its subdivision form meet the requirements of the finite difference method. The solution model of the temperature field under the influence of the constant seepage field, respectively record the set of points in the grid and boundary points as Ω h and
Figure DEST_PATH_GDA0000417473680000032
Use the difference quotient to express the second order derivative on the point ( xi , y j ), namely:

∂∂ 22 TT ∂∂ xx 22 || (( xx ii ,, ythe y jj )) == 11 hh 22 [[ TT (( xx ii ++ 11 ,, ythe y jj )) -- 22 TT (( xx ii ,, ythe y jj )) ++ TT (( xx ii -- 11 ,, ythe y jj )) ]] ++ oo (( hh 22 )) ,,

∂∂ TT ∂∂ xx || (( xx ii ,, ythe y jj )) == TT (( xx ii ++ 11 ,, ythe y jj )) -- TT (( xx ii -- 11 ,, ythe y jj )) 22 hh ++ oo (( hh 22 )) ,,

将上述两式代入微分方程  Substitute the above two equations into the differential equation

∂∂ 22 TT ∂∂ xx 22 ++ ∂∂ 22 TT ∂∂ ythe y 22 -- dd ∂∂ TT ∂∂ xx == 00 ,,

可得到差分方程  The difference equation can be obtained

11 hh 22 [[ TT (( xx ii ++ 11 ,, ythe y jj )) -- 22 TT (( xx ii ,, ythe y jj )) ++ TT (( xx ii -- 11 ,, ythe y jj )) ]] ++ 11 hh 22 [[ TT (( xx ii ,, ythe y jj ++ 11 )) -- 22 TT (( xx ii ,, ythe y jj )) ++ TT (( xx ii ,, ythe y jj -- 11 )) ]] -- dd TT (( xx ii ++ 11 ,, ythe y jj )) -- TT (( xx ii -- 11 ,, ythe y jj )) 22 hh == 00

用Ti,j表示T(xi,yj)的,则上式可表示为  Using T i, j to represent T( xi , y j ), then the above formula can be expressed as

( 1 + ah 2 ) T i - 1 , j + T i , j - 1 - 4 T i , j + T i , j + 1 + ( 1 - ah 2 ) T i + 1 , j = 0 该式即为单线热源法中均匀稳恒渗流场影响下的温度场求解模型的五点差分格式,在求解域内有多少未知温度的节点,即会建立多少个差分方程,进而进行求解。  ( 1 + ah 2 ) T i - 1 , j + T i , j - 1 - 4 T i , j + T i , j + 1 + ( 1 - ah 2 ) T i + 1 , j = 0 This formula is the five-point difference scheme of the temperature field solution model under the influence of the uniform steady seepage field in the single-line heat source method. How many nodes with unknown temperature are in the solution domain, that is, how many difference equations will be established, and then solved.

(5)在测得该稳定渗流情况下的不同加热功率的温升曲线之后,改变出水系统的流速控制阀门开度,改变渗流场,待渗流场稳定之后,重复上述步骤,测得不同渗流场下不同加热功率的温升曲线。  (5) After measuring the temperature rise curves of different heating powers under the condition of stable seepage, change the flow rate control valve opening of the water outlet system to change the seepage field. After the seepage field is stable, repeat the above steps to measure different seepage fields The temperature rise curve of different heating power. the

(6)构建基于热线法的导热系数计算模型;瞬态热线法作为测量液体导热系数的主流方法,已经被公认为最好的导热系数测定方法,其理想模型为无限大介质中的径向一维非稳态导热问题,在初始温度均匀分布的无限介质中,对布设其中的热线加载恒定的加热功率,由于热线半径非常小,所以只要时间τ足够长,热线表面温升θ的表达式可简化为

Figure DEST_PATH_GDA0000417473680000046
式中:θ为光缆绝对温升,θ=T-T0,T为时间τ时光缆的温度,T0为加热初始光缆温度;q为单位长度加热功率,单位为W/m;λ为导热系数,单位为W·m-1·K-1;τ为加热时间;a为热扩散系数,单位为m2/s;r0为热线半径;C为比热容,单位J·kg-1·K-1,上式即为建立的瞬态热线法测量导热系数的基本方程。  (6) Construct a thermal conductivity calculation model based on the hot wire method; as the mainstream method for measuring the thermal conductivity of liquids, the transient hot wire method has been recognized as the best thermal conductivity measurement method, and its ideal model is a radial one in an infinite medium. dimensional unsteady heat conduction problem, in an infinite medium with uniform initial temperature distribution, a constant heating power is applied to the hot wire arranged in it, since the radius of the hot wire is very small, so as long as the time τ is long enough, the expression of the surface temperature rise θ of the hot wire can be expressed as Simplified to
Figure DEST_PATH_GDA0000417473680000046
In the formula: θ is the absolute temperature rise of the optical cable, θ=TT 0 , T is the temperature of the cable at the time τ, T 0 is the initial temperature of the cable during heating; q is the heating power per unit length, in W/m; λ is the thermal conductivity, The unit is W·m -1 ·K -1 ; τ is the heating time; a is the thermal diffusivity, the unit is m 2 /s; r 0 is the radius of the heating line; C is the specific heat capacity, the unit is J·kg -1 ·K -1 , the above formula is the basic equation for measuring the thermal conductivity established by the transient hot wire method.

(7)计算光缆所在介质的导热系数。根据瞬态热线法测量导热系数的基本方程,基于实验分析,绘制出θ~lnτ关系图,找出其中的直线段并求出其斜率,由该斜率值和加热功率q即可算出导热系数λ,其中λ的表达式为: 

Figure DEST_PATH_GDA0000417473680000051
通过前面推导的热线法计算模型进而可以计算出其导热系数。  (7) Calculate the thermal conductivity of the medium where the optical cable is located. According to the basic equation of measuring the thermal conductivity by the transient hot wire method, based on the experimental analysis, draw the relationship diagram of θ~lnτ, find out the straight line segment and calculate its slope, and calculate the thermal conductivity λ from the slope value and the heating power q , where the expression of λ is:
Figure DEST_PATH_GDA0000417473680000051
The thermal conductivity can be calculated through the calculation model of the hot wire method deduced above.

(8)通过温升过程线图,得到相应渗流场下的名义导热系数。名义导热系数由本申请中首次提出,分析处于渗流场中的热线(即通电加热的光缆)温升过程线,绘制θ~lnτ关系图。观察该温升过程线图即可发现,同传统热线法一样,图中同样存在着直线段,利用该直线段区间的数据可以拟合出一个斜率,进而可算出一个与之对应的导热系数。与传统热线法对比分析,首创提出了一种包含渗流对热线影响的导热系数,将其称为名义导热系数。  (8) The nominal thermal conductivity under the corresponding seepage field is obtained through the temperature rise process diagram. The nominal thermal conductivity is proposed for the first time in this application, and the temperature rise process line of the hot wire (that is, the optical cable heated by electricity) in the seepage field is analyzed, and the relationship between θ~lnτ is drawn. Observing the line diagram of the temperature rise process, it can be found that, like the traditional hot-line method, there is also a straight line segment in the figure, and a slope can be fitted by using the data in the line segment interval, and then a corresponding thermal conductivity can be calculated. Compared with the traditional hot wire method, a thermal conductivity coefficient including the influence of seepage on the hot wire is proposed for the first time, which is called the nominal thermal conductivity. the

该导热系数不是传统意义上无渗流状态下无限大均匀介质的导热系数,而是一种处于渗流场中,包含了渗流对热线影响的导热系数,该名义导热系数既包含了传统意义上的热传导部分,也包含了渗流对热线的影响。不同的渗流场,与之对应的名义导热系数必定不同,这两者之间存在某种关系,利用直线段区间的数据可以拟合出一个斜率,将该斜率代入导热系数计算模型中,即可算出一个与之对应的名义导热系数。  The thermal conductivity is not the thermal conductivity of an infinite homogeneous medium in the traditional sense without seepage, but a thermal conductivity in the seepage field that includes the influence of seepage on the hot line. The nominal thermal conductivity includes both the traditional thermal conductivity section, also covers the effect of percolation on the hot wire. For different seepage fields, the corresponding nominal thermal conductivity must be different. There is a certain relationship between the two. A slope can be fitted by using the data of the straight line interval, and the slope can be substituted into the thermal conductivity calculation model. Calculate a corresponding nominal thermal conductivity. the

(9)构建名义导热系数和渗流流速的关系数学模型,从而由不同渗流场的名义导热系数得到各种流速下的渗流流速值。  (9) Construct the mathematical model of the relationship between nominal thermal conductivity and seepage flow velocity, so that the seepage velocity values at various flow velocities can be obtained from the nominal thermal conductivity of different seepage fields. the

不同的渗流场,与之对应的名义导热系数必定不同,据此,可以将名义导热系数作为反映相应渗流场特性的一种新的物理参数;基于不同加热功率下的名义导热系数,得到各种流速下的其不同值;通过试验分析、理论研究得出了渗流流速与平均导热系数的关系,渗流流速和平均名义导热系数的线性相关关系非常明显,从而得到了渗流流速的经验计算公式,两者线性相关性非常明显。  For different seepage fields, the corresponding nominal thermal conductivity must be different. Accordingly, the nominal thermal conductivity can be used as a new physical parameter to reflect the characteristics of the corresponding seepage field; based on the nominal thermal conductivity under different heating powers, various The different values under the flow rate; through the experimental analysis and theoretical research, the relationship between the seepage flow rate and the average thermal conductivity is obtained. The linear correlation between the seepage flow rate and the average nominal thermal conductivity is very obvious, and thus the empirical calculation formula of the seepage flow rate is obtained. The linear correlation is very obvious. the

当假设多孔介质各向同性,即λxyz=常数;只考虑光纤定位精度范围内(即1m光纤长度范围)光纤及以光纤为中心的一定半径内的场分布情况;渗流场为稳定渗流场,即渗流速度不随时间和位置而变化,是一个常量。在三维坐标中,可以分解为Vx、Vy、Vz(常量);无源汇项即QT=0;只考虑稳定温度场, 即

Figure DEST_PATH_GDA0000417473680000061
渗流场影响下的三维导热方程可以写为下列形式:  ▿ 2 T - c w ρ w λ [ v x ∂ T ∂ x + v y ∂ T ∂ y + v z ∂ T ∂ z ] = 0 , - c w ρ w λ v x = a 1 , - c w ρ w λ v y = a 2 , - c w ρ w λ v z = a 3 . 则可以化简为 ▿ 2 T + a 1 ∂ T ∂ x + a 2 ∂ T ∂ y + a 3 ∂ T ∂ z = 0 , 该式即为只考虑渗流对温度影响、渗流流速为常数的监测模型方程式。可以看出,对于给定的边值条件,温度场的分布只与系数a1、a2、a3有关,而对于某一特定介质,
Figure DEST_PATH_GDA0000417473680000066
为常数,所以温度场的分布只与渗流流速v有关系,流速v会和温度场形成一一对应关系。  When assuming that the porous medium is isotropic, that is, λ x = λ y = λ z = constant; only consider the fiber within the range of positioning accuracy of the fiber (that is, the range of 1m fiber length) and the field distribution within a certain radius centered on the fiber; seepage The field is a stable seepage field, that is, the seepage velocity does not change with time and position, and is a constant. In three-dimensional coordinates, it can be decomposed into V x , V y , V z (constant); the passive sink term is Q T =0; only the stable temperature field is considered, namely
Figure DEST_PATH_GDA0000417473680000061
The three-dimensional heat conduction equation under the influence of the seepage field can be written in the following form: ▿ 2 T - c w ρ w λ [ v x ∂ T ∂ x + v the y ∂ T ∂ the y + v z ∂ T ∂ z ] = 0 , make - c w ρ w λ v x = a 1 , - c w ρ w λ v the y = a 2 , - c w ρ w λ v z = a 3 . can be simplified to ▿ 2 T + a 1 ∂ T ∂ x + a 2 ∂ T ∂ the y + a 3 ∂ T ∂ z = 0 , This formula is a monitoring model equation that only considers the influence of seepage on temperature and the seepage velocity is constant. It can be seen that for a given boundary value condition, the distribution of the temperature field is only related to the coefficients a1, a2, a3, and for a specific medium,
Figure DEST_PATH_GDA0000417473680000066
is a constant, so the distribution of the temperature field is only related to the seepage flow velocity v, and the flow velocity v will form a one-to-one correspondence with the temperature field.

本发明与现有技术相比,其有益效果是:1、本发明方法突破常规的光纤渗流监测方法中监测周期为整个光缆加热的温升周期,准确定位了渗流流速同平均导热系数的线性相关性,监测精度得到可靠保证。2、该发明通过了理论研究、试验验证,首创提出了一种包含渗流对热线影响的名义导热系数,本发明结果真实可靠,对于亟待研究的实际工程中埋设光缆的渗流流速监测具有重大意义。3、本发明解决了分布式光纤温度传感技术中渗流流速的监测问题,使其工程实际应用提供了可能。  Compared with the prior art, the present invention has the beneficial effects as follows: 1. The method of the present invention breaks through the conventional optical fiber seepage monitoring method in which the monitoring period is the temperature rise period of the entire optical cable heating, and accurately locates the linear correlation between the seepage velocity and the average thermal conductivity performance, and the monitoring accuracy is reliably guaranteed. 2. The invention has passed theoretical research and experimental verification. It is the first to propose a nominal thermal conductivity that includes the influence of seepage on the hot wire. The results of the invention are true and reliable, and it is of great significance for the monitoring of the seepage velocity of buried optical cables in practical projects that need to be studied urgently. 3. The present invention solves the problem of monitoring the seepage velocity in the distributed optical fiber temperature sensing technology, and provides the possibility for its practical engineering application. the

附图说明 Description of drawings

图1为本发明多孔介质结构体渗流流速监测试验装置示意图;  Fig. 1 is a schematic diagram of the porous media structure seepage velocity monitoring test device of the present invention;

图2为多孔介质结构体渗流流速监测试验装置的供水系统示意图;  Fig. 2 is the schematic diagram of the water supply system of the porous media structure seepage velocity monitoring test device;

图3为单线热源法中目标光纤加热产生的温度场及模型示意图;  Figure 3 is a schematic diagram of the temperature field and model generated by the heating of the target optical fiber in the single-line heat source method;

图4为单线法反演流速示意图;  Figure 4 is a schematic diagram of the single-line method inversion flow velocity;

图5为多孔介质结构体渗流流速监测试验装置的加热系统示意图;  Figure 5 is a schematic diagram of the heating system of the porous media structure seepage velocity monitoring test device;

图6为光纤流速反演模型示意图;  Figure 6 is a schematic diagram of the optical fiber flow velocity inversion model;

图7为多孔介质结构体渗流流速监测试验装置模型槽前视图;  Fig. 7 is the front view of the model tank of the porous media structure seepage velocity monitoring test device;

图8为多孔介质结构体渗流流速监测试验装置模型槽左视断面图;  Fig. 8 is a left view sectional view of the model tank of the porous media structure seepage velocity monitoring test device;

图9为v=0.0571×10-3m/s下不同加热功率下的θ~lnτ图;  Figure 9 is the graph of θ~lnτ under different heating powers under v=0.0571×10-3m/s;

图10为v=0.0730×10-3m/s下不同加热功率下的θ~lnτ图;  Figure 10 is the graph of θ~lnτ under different heating powers at v=0.0730×10 -3 m/s;

图11为0.1515×10-3m/s下不同加热功率下的θ~lnτ图;  Figure 11 is the graph of θ~lnτ under different heating powers at 0.1515×10 -3 m/s;

图12为v=0.0974ⅹ10-3m/s下不同加热功率下的θ~lnτ图;  Figure 12 is the graph of θ~lnτ under different heating powers under v=0.0974ⅹ10 -3 m/s;

图13为v=0.1964ⅹ10-3m/s下不同加热功率下的θ~lnτ图;  Figure 13 is the graph of θ~lnτ under different heating powers under v=0.1964ⅹ10 -3 m/s;

图14为渗流流速和导热系数关系图。  Figure 14 is a graph showing the relationship between seepage velocity and thermal conductivity. the

具体实施方式 Detailed ways

下面对本发明技术方案进行详细说明,但是本发明的保护范围不局限于所述实施例。  The technical solutions of the present invention will be described in detail below, but the protection scope of the present invention is not limited to the embodiments. the

实施例1:本发明所述的多孔介质结构体渗流流速监测试验装置,其装置示意图如图1所示,包括加热系统1、分布式光纤温度传感系统2、埋设有监测光纤的多孔介质结构体模型槽3和出水系统4;所述加热系统1、分布式光纤温度传感系统2和出水系统4分别与所述多孔介质结构体模型槽3连接。  Embodiment 1: The porous medium structure seepage flow rate monitoring test device according to the present invention, the schematic diagram of which is shown in Figure 1, includes a heating system 1, a distributed optical fiber temperature sensing system 2, and a porous medium structure embedded with monitoring optical fibers Body model tank 3 and water outlet system 4; the heating system 1, distributed optical fiber temperature sensing system 2 and water outlet system 4 are respectively connected to the porous medium structure model tank 3. the

所述加热系统如图5所示,主要由交流电源9、调压器10和负载发热电阻丝11组成的并联电路,通过负载发热电阻丝11对监测光纤加热,通过调压器10控制电压从而控制加热功率;所述分布式光纤温度传感系统包括分布式光纤测温主机和线性多模感温光缆,所述分布式光纤测温主机通过脉冲激光设备与所述线性多模感温光缆相连并输出光脉冲;所述线性多模感温光缆的尾部与光纤连接器相连;所述出水系统如图2所示,包括水箱5、流速控制阀6、水泵7及循环水池8;所述水箱5的位置高于所述循环水池8,所述水箱5的水位线上部通过溢流管与所述循环水池8连接;所述循环水池8通过水泵7将水输送到水箱5中;所述水箱5底部通过管道与所述多孔介质结构体模型槽3连接;所述流速控制阀6分别设置在水箱5与所述多孔介质结构体模型槽3和循环水池8之间的管道上。  The heating system, as shown in Figure 5, is mainly composed of a parallel circuit consisting of an AC power supply 9, a voltage regulator 10, and a load heating resistance wire 11. The monitoring optical fiber is heated by the load heating resistance wire 11, and the voltage is controlled by the voltage regulator 10 so that Control the heating power; the distributed optical fiber temperature sensing system includes a distributed optical fiber temperature measurement host and a linear multi-mode temperature sensing optical cable, and the distributed optical fiber temperature measurement host is connected to the linear multimode temperature sensing optical cable through a pulse laser device And output optical pulses; the tail of the linear multimode temperature-sensing optical cable is connected with the optical fiber connector; the water outlet system as shown in Figure 2 includes a water tank 5, a flow control valve 6, a water pump 7 and a circulating pool 8; the water tank The position of 5 is higher than that of the circulating pool 8, and the upper part of the water level line of the water tank 5 is connected with the circulating pool 8 through an overflow pipe; the circulating pool 8 delivers water to the water tank 5 through the water pump 7; the water tank 5. The bottom is connected to the porous medium structure model tank 3 through a pipeline; the flow rate control valve 6 is respectively arranged on the pipeline between the water tank 5, the porous medium structure model tank 3 and the circulating water pool 8. the

本发明多孔介质结构体渗流流速监测试验方法,包括如下步骤:  The porous medium structure body seepage velocity monitoring test method of the present invention comprises the following steps:

(1)设计试验中不同流速及加热功率工况。通过控制出水系统来设计试验中不同的流速工况;通过控制加热系统来设计试验中不同的加热功率工况,由于加热电路相同,所以采用控制电压来控制不同的加热功率工况。本试验设计了六种不同流速工况:0m/s、0.0571×10-3m/s、0.0730×10-3m/s、0.1515×10-3m/s、0.0974×10-3m/s、0.1964×10-3m/s。由于加热电路相同,所以采用电压来控制加热功率,采用了6种不同的加热电压:7V、9V、11V、13V、15V、17V;  (1) Different flow rates and heating power conditions in the design test. Different flow rate conditions in the test are designed by controlling the water outlet system; different heating power conditions in the test are designed by controlling the heating system. Since the heating circuit is the same, the control voltage is used to control different heating power conditions. Six different flow velocity conditions were designed in this experiment: 0m/s, 0.0571×10-3m/s, 0.0730×10-3m/s, 0.1515×10-3m/s, 0.0974×10-3m/s, 0.1964×10 -3m/s. Since the heating circuit is the same, voltage is used to control the heating power, and 6 different heating voltages are used: 7V, 9V, 11V, 13V, 15V, 17V;

(2)构建埋设有监测光纤的多孔介质结构体模型槽。基于不同试验要求,根据具体设计搭建带光纤的多孔介质结构体的待监测模型槽,本实施例主要砌筑 一个长2.6m、宽1m、高1.15m的模型槽,并用M5水泥砂浆砌筑,M10砂浆抹面;水池内壁铺设塑料薄膜作为进一步的防渗材料在高度为1m的长度方向墙上预留两个50mm外径的出水口。进、出水口连接进水管12、出水管13,测压管14和光缆15同塑料薄膜的接口部分采用橡皮勒紧和502胶水密封防水;水池底部铺设30cm由各种粒径组成的反滤层16;反滤层上面铺设反滤网17;其上铺设55cm厚的细砂18,细砂上面依旧是反滤网17和反滤层16;在水池的两个宽度方向面的中心,高度为65cm的位置预留目标光纤15布置用的穿墙孔。具体见附图7、8。  (2) Construct the model groove of the porous medium structure embedded with the monitoring optical fiber. Based on different test requirements, according to the specific design, a model tank to be monitored of a porous medium structure with an optical fiber is built. In this embodiment, a model tank with a length of 2.6m, a width of 1m, and a height of 1.15m is mainly built, and it is built with M5 cement mortar. M10 mortar plastering; plastic film is laid on the inner wall of the pool as a further anti-seepage material, and two water outlets with an outer diameter of 50mm are reserved on the lengthwise wall with a height of 1m. The water inlet and outlet are connected to the water inlet pipe 12, the water outlet pipe 13, the interface between the pressure measuring pipe 14 and the optical cable 15 and the plastic film is sealed and waterproof with rubber tightening and 502 glue; a 30cm reverse filter layer composed of various particle sizes is laid on the bottom of the pool 16; Lay reverse filter screen 17 above the reverse filter layer; Lay 55cm thick fine sand 18 on it, still be reverse filter screen 17 and reverse filter layer 16 above the fine sand; In the center of two width direction faces of pond, height is A wall hole for the layout of the target optical fiber 15 is reserved at the position of 65 cm. See attached drawings 7 and 8 for details. the

(3)调整出水系统以形成均匀稳定渗流场。基于不同设计的试验工况,经多次调试,将供水系统阀门调节到某一确定位置,后持续监测出水系统的出流量,待出流量稳定时,可认为均匀稳定渗流场已经形成。  (3) Adjust the outlet system to form a uniform and stable seepage field. Based on the test conditions of different designs, the valves of the water supply system are adjusted to a certain position after several times of debugging, and then the outflow of the water outlet system is continuously monitored. When the outflow is stable, it can be considered that a uniform and stable seepage field has been formed. the

(4)基于分布式光纤温度传感系统对埋设于模型槽中的监测光纤进行温度监测;采用英国Sensornet公司生产的Sentinel DTS-LR型号的分布式光纤测温主机,Sentinel DTS配设一个脉冲激光设备,它同50/125多模光纤相连并输出一种10纳秒的光脉冲,其尾部同E2000光纤连接器相连。  (4) Based on the distributed optical fiber temperature sensing system, the temperature monitoring of the monitoring optical fiber buried in the model groove is carried out; the Sentinel DTS-LR type distributed optical fiber temperature measurement host produced by the British Sensornet company is used, and the Sentinel DTS is equipped with a pulse laser A device that connects to a 50/125 multimode fiber and outputs a 10 nanosecond optical pulse whose tail is connected to an E2000 fiber optic connector. the

(5)确定加热方式。本实施例采用单线热源法加热,在土石坝及土石堤防的渗流监测中,单线热源法同双线热源法最大的不同在于,单线热源法只需在渗流场区域布设一根测温光纤,利用DTS测温仪测出目标光纤稳定温度T1、起始温度(即加热时的环境温度)T0以及1#光纤的加热功率q。利用上述数据即可通过单线热源法反演出渗流流速v。  (5) Determine the heating method. In this embodiment, the single-line heat source method is used for heating. In the seepage monitoring of earth-rock dams and embankments, the biggest difference between the single-line heat source method and the double-line heat source method is that the single-line heat source method only needs to arrange a temperature-measuring optical fiber in the seepage field area. The DTS thermometer measures the stable temperature T 1 of the target fiber, the initial temperature (that is, the ambient temperature during heating) T 0 and the heating power q of the 1# fiber. Using the above data, the seepage flow velocity v can be inverted by the single-line heat source method.

(6)通过加热系统对目标光纤做通电加热操作。如果需要比较大的加热功率,就需要很大的电流,因此在选用调压器的时候,一定要考虑调压器的额定电流。本装置选用TDGC2-5型单相调压器可调节电压交流电源可以选用调压器。并且设置了防跳闸启动加载电路;经分布式光纤温度传感系统监测10分钟之后,开始对目标光缆中固定用钢丝利用即单端加热法通电加热,同时不断监测目标光缆的分布式温度并记录下加热功率和起始加热时刻的监测文件名,为以后整理数据提供依据。在一次监测周期完成后,改变加热功率,测得在该渗流速度下不同加热功率的温升曲线。  (6) Conduct electric heating operation on the target optical fiber through the heating system. If a relatively large heating power is required, a large current is required, so when selecting a voltage regulator, the rated current of the voltage regulator must be considered. This device adopts TDGC2-5 single-phase voltage regulator, and the adjustable voltage AC power supply can choose a voltage regulator. And set up the anti-tripping start-up loading circuit; after being monitored by the distributed optical fiber temperature sensing system for 10 minutes, the fixed steel wire in the target optical cable will be heated by the single-ended heating method, and the distributed temperature of the target optical cable will be continuously monitored and recorded. The heating power and the monitoring file name of the initial heating time will provide the basis for the data sorting in the future. After a monitoring period is completed, the heating power is changed, and the temperature rise curve of different heating powers at the seepage velocity is measured. the

(7)在测得该稳定渗流情况下的不同加热功率的温升曲线之后,改变供水系统的流速控制阀门开度,改变渗流场,待该渗流场稳定之后,重复上述步骤, 测得不同渗流场下不同加热功率的温升曲线。  (7) After measuring the temperature rise curves of different heating powers under the condition of stable seepage, change the flow rate of the water supply system to control the valve opening and change the seepage field. After the seepage field is stable, repeat the above steps to measure different seepage flows. The temperature rise curve of different heating power under the field. the

(8)构建基于热线法的导热系数计算模型。热线表面温升θ的表达式可简化为式中:θ为光缆绝对温升,θ=T-T0,T为时间τ时光缆的温度,T0为加热初始光缆温度;q为单位长度加热功率,单位为W/m;λ为导热系数,单位为W·m-1·K-1;τ为加热时间;a为热扩散系数,单位为m2/s;r0为热线半径;C为比热容,单位J·kg-1·K-1,上式即为建立的瞬态热线法测量导热系数的基本方程。  (8) Construct a thermal conductivity calculation model based on the hot wire method. The expression of the surface temperature rise θ of the hot wire can be simplified as In the formula: θ is the absolute temperature rise of the optical cable, θ=TT 0 , T is the temperature of the cable at the time τ, T 0 is the initial temperature of the cable during heating; q is the heating power per unit length, in W/m; λ is the thermal conductivity, The unit is W·m -1 ·K -1 ; τ is the heating time; a is the thermal diffusivity, the unit is m 2 /s; r 0 is the radius of the heating line; C is the specific heat capacity, the unit is J·kg -1 ·K -1 , the above formula is the basic equation for measuring the thermal conductivity established by the transient hot wire method.

(9)计算光缆所在介质的导热系数。根据瞬态热线法测量导热系数的基本方程,基于实验分析,绘制出θ~lnτ关系图,找出其中的直线段并求出其斜率,由该斜率值和加热功率q即可算出导热系数λ,其中λ的表达式为: 

Figure DEST_PATH_GDA0000417473680000092
通过前面推导的热线法计算模型进而可以计算出其导热系数。  (9) Calculate the thermal conductivity of the medium where the cable is located. According to the basic equation of measuring the thermal conductivity by the transient hot wire method, based on the experimental analysis, draw the relationship diagram of θ~lnτ, find out the straight line segment and calculate its slope, and calculate the thermal conductivity λ from the slope value and the heating power q , where the expression of λ is:
Figure DEST_PATH_GDA0000417473680000092
The thermal conductivity can be calculated through the calculation model of the hot wire method deduced above.

(10)首创提出相应渗流场下的名义导热系数。提取本试验中监测光纤5m位置处的有效数据,得到不同流速工况下该点的温度变化过程线,绘制θ~lnτ关系图,见附图9~13。观察该温升过程线图即可发现,同传统热线法一样,图中同样存在着直线段,利用该直线段区间的数据可以拟合出一个斜率,进而可算出一个与之对应的导热系数。与传统热线法对比分析,提出了一种包含渗流对热线影响的导热系数,将其称为名义导热系数。  (10) The first to propose the nominal thermal conductivity under the corresponding seepage field. Extract the effective data at the 5m position of the monitoring optical fiber in this test, obtain the temperature change process line at this point under different flow rate conditions, and draw the θ~lnτ relationship diagram, see Figures 9-13. Observing the line diagram of the temperature rise process, it can be found that, like the traditional hot-line method, there is also a straight line segment in the figure, and a slope can be fitted by using the data in the line segment interval, and then a corresponding thermal conductivity can be calculated. Compared with the traditional hot wire method, a thermal conductivity coefficient including the influence of seepage on the hot wire is proposed, which is called the nominal thermal conductivity. the

该导热系数不是传统意义上无渗流状态下无限大均匀介质的导热系数,而是一种处于渗流场中,包含了渗流对热线影响的导热系数,该名义导热系数既包含了传统意义上的热传导部分,也包含了渗流对热线的影响。不同的渗流场,与之对应的名义导热系数必定不同,这两者之间存在某种关系,利用直线段区间的数据可以拟合出一个斜率,将该斜率代入导热系数计算模型中,即可算出一个与之对应的名义导热系数,其计算结果见附表1。  The thermal conductivity is not the thermal conductivity of an infinite homogeneous medium in the traditional sense without seepage, but a thermal conductivity in the seepage field that includes the influence of seepage on the hot line. The nominal thermal conductivity includes both the traditional thermal conductivity section, also covers the effect of percolation on the hot wire. For different seepage fields, the corresponding nominal thermal conductivity must be different. There is a certain relationship between the two. A slope can be fitted by using the data of the straight line interval, and the slope can be substituted into the thermal conductivity calculation model. Calculate a corresponding nominal thermal conductivity, and the calculation results are shown in Attached Table 1. the

表1不同工况下的名义导热系数计算表  Table 1 Calculation table of nominal thermal conductivity under different working conditions

Figure DEST_PATH_GDA0000417473680000101
Figure DEST_PATH_GDA0000417473680000101

(11)确定名义导热系数和渗流流速的关系数学模型。不同的渗流场,与之对应的名义导热系数必定不同,以渗流流速为y轴,平均导热系数为x轴,绘制散点图,见附图14;从附图14中可以看出,渗流流速和平均名义导热系数的线性相关关系非常明显;对该散点图进行线性拟合得渗流流速的计算公式 v=5.5848λ-2.7727;式中:v为渗流速度,单位10-3m/s;λ为名义导热系数,单位W(m·k);复相关系数R=0.9877,两者线性相关性非常明显,据此,建立了名义导热系数和渗流流速的关系数学模型。  (11) Determine the mathematical model of the relationship between nominal thermal conductivity and seepage velocity. For different seepage fields, the corresponding nominal thermal conductivity must be different. Take the seepage velocity as the y-axis and the average thermal conductivity as the x-axis. Draw a scatter diagram, see attached drawing 14; it can be seen from attached drawing 14 that the seepage velocity The linear correlation with the average nominal thermal conductivity is very obvious; the calculation formula of the seepage flow velocity v=5.5848λ-2.7727 is obtained by linear fitting of the scatter diagram; where: v is the seepage velocity, and the unit is 10 -3 m/s; λ is the nominal thermal conductivity, the unit is W(m·k); the complex correlation coefficient R=0.9877, and the linear correlation between the two is very obvious. Based on this, the mathematical model of the relationship between the nominal thermal conductivity and the seepage velocity is established.

如上所述,尽管参照特定的优选实施例已经表示和表述了本发明,但其不得解释为对本发明自身的限制。在不脱离所附权利要求定义的本发明的精神和范围前提下,可对其在形式上和细节上作出各种变化。  As stated above, while the invention has been shown and described with reference to certain preferred embodiments, this should not be construed as limiting the invention itself. Various changes in form and details may be made therein without departing from the spirit and scope of the invention as defined by the appended claims. the

Claims (2)

1.一种多孔介质结构体渗流流速监测试验装置,其特征在于:包括加热系统(1)、分布式光纤温度传感系统(2)、埋设有监测光纤的多孔介质结构体模型槽(3)和出水系统(4);所述加热系统(1)、分布式光纤温度传感系统(2)和出水系统(4)分别与所述多孔介质结构体模型槽(3)连接。 1. A porous media structure seepage velocity monitoring test device, characterized in that it includes a heating system (1), a distributed optical fiber temperature sensing system (2), and a porous media structure model tank (3) embedded with monitoring optical fibers and a water outlet system (4); the heating system (1), the distributed optical fiber temperature sensing system (2) and the water outlet system (4) are respectively connected to the porous medium structure model tank (3). 2.根据权利要求1所述的多孔介质结构体渗流流速监测试验装置,其特征在于: 2. The porous media structure seepage velocity monitoring test device according to claim 1, characterized in that: 所述加热系统为主要由交流电源(9)、调压器(10)和负载发热电阻丝(11)组成的并联电路,通过负载发热电阻丝(11)对监测光纤加热,通过调压器(10)控制电压从而控制加热功率; The heating system is a parallel circuit mainly composed of an AC power supply (9), a voltage regulator (10) and a load heating resistance wire (11). The monitoring optical fiber is heated through the load heating resistance wire (11), and the voltage regulator ( 10) Control the voltage to control the heating power; 所述分布式光纤温度传感系统包括分布式光纤测温主机和线性多模感温光缆,所述分布式光纤测温主机通过脉冲激光设备与所述线性多模感温光缆相连并输出光脉冲;所述线性多模感温光缆的尾部与光纤连接器相连; The distributed optical fiber temperature sensing system includes a distributed optical fiber temperature measurement host and a linear multi-mode temperature-sensing optical cable, and the distributed optical fiber temperature measurement host is connected to the linear multi-mode temperature-sensing optical cable through a pulse laser device and outputs optical pulses ; The tail of the linear multimode temperature-sensing optical cable is connected to the optical fiber connector; 所述出水系统包括水箱(5)、流速控制阀(6)、水泵(7)及循环水池(8);所述水箱(5)的位置高于所述循环水池(8),所述水箱(5)的水位线上部通过溢流管与所述循环水池(8)连接;所述循环水池(8)通过水泵(7)将水输送到水箱(5)中;所述水箱(5)底部通过管道与所述多孔介质结构体模型槽(3)连接;所述流速控制阀(6)分别设置在水箱(5)与所述多孔介质结构体模型槽(3)和循环水池(8)之间的管道上。 The water outlet system includes a water tank (5), a flow rate control valve (6), a water pump (7) and a circulating water pool (8); the water tank (5) is located higher than the circulating water pool (8), and the water tank ( The upper part of the water level line of 5) is connected to the circulating pool (8) through an overflow pipe; the circulating pool (8) delivers water to the water tank (5) through the water pump (7); the bottom of the water tank (5) passes through The pipeline is connected to the porous medium structure model tank (3); the flow rate control valve (6) is respectively arranged between the water tank (5) and the porous medium structure model tank (3) and the circulating water pool (8) on the pipeline.
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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103412142A (en) * 2013-09-10 2013-11-27 河海大学 Device and method for monitoring and testing seepage speed of porous medium structural body
CN105785068A (en) * 2016-05-06 2016-07-20 河海大学 Distributed fiber monitoring system and method for seepage flow velocity of hydraulic structural body
CN111220818A (en) * 2019-12-10 2020-06-02 哈尔滨工程大学 A Device for Calibrating Velocity Measurement Accuracy of Doppler Current Meter
CN117890264A (en) * 2023-12-22 2024-04-16 河海大学 A calculation method for the water vapor diffusion coefficient of glass sand porous media

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103412142A (en) * 2013-09-10 2013-11-27 河海大学 Device and method for monitoring and testing seepage speed of porous medium structural body
CN103412142B (en) * 2013-09-10 2015-04-08 河海大学 Device and method for monitoring and testing seepage speed of porous medium structural body
CN105785068A (en) * 2016-05-06 2016-07-20 河海大学 Distributed fiber monitoring system and method for seepage flow velocity of hydraulic structural body
CN111220818A (en) * 2019-12-10 2020-06-02 哈尔滨工程大学 A Device for Calibrating Velocity Measurement Accuracy of Doppler Current Meter
CN111220818B (en) * 2019-12-10 2021-10-19 哈尔滨工程大学 A Device for Calibrating Velocity Measurement Accuracy of Doppler Current Meter
CN117890264A (en) * 2023-12-22 2024-04-16 河海大学 A calculation method for the water vapor diffusion coefficient of glass sand porous media
CN117890264B (en) * 2023-12-22 2024-10-11 河海大学 A calculation method for water vapor diffusion coefficient of glass sand porous medium

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