Solution of inverse heat conduction problem.
\r\n\t
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Tiefenbacher",publishedDate:null,coverURL:"https://cdn.intechopen.com/books/images_new/10765.jpg",keywords:"Managing Urbanization, Managing Development, Managing Resource Use, Drought Management, Flood Management, Water Quality Monitoring, Air Quality Monitoring, Ecological Monitoring, Modeling Extreme Natural Events, Ecological Restoration, Restoring Environmental Flows, Environmental Management Perspectives",numberOfDownloads:null,numberOfWosCitations:0,numberOfCrossrefCitations:null,numberOfDimensionsCitations:null,numberOfTotalCitations:null,isAvailableForWebshopOrdering:!0,dateEndFirstStepPublish:"January 12th 2021",dateEndSecondStepPublish:"February 9th 2021",dateEndThirdStepPublish:"April 10th 2021",dateEndFourthStepPublish:"June 29th 2021",dateEndFifthStepPublish:"August 28th 2021",remainingDaysToSecondStep:"23 days",secondStepPassed:!1,currentStepOfPublishingProcess:2,editedByType:null,kuFlag:!1,biosketch:"A geospatial scholar working at the interface of natural and human systems, collaborating internationally on innovative studies about hazards and environmental challenges. 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More recently his work pertains to spatial adaptation to climate change, spatial responses in wine growing regions to climate change, the geographies of viticulture and wine, artificial intelligence and machine learning to predict patterns of natural processes and hazards, historical ethnic enclaves in American cities and regions, and environmental adaptations of 19th century European immigrants to North America's landscapes.",institutionString:"Texas State University",position:null,outsideEditionCount:0,totalCites:0,totalAuthoredChapters:"1",totalChapterViews:"0",totalEditedBooks:"6",institution:{name:"Texas State University",institutionURL:null,country:{name:"United States of America"}}}],coeditorOne:null,coeditorTwo:null,coeditorThree:null,coeditorFour:null,coeditorFive:null,topics:[{id:"12",title:"Environmental Sciences",slug:"environmental-sciences"}],chapters:null,productType:{id:"1",title:"Edited Volume",chapterContentType:"chapter",authoredCaption:"Edited by"},personalPublishingAssistant:{id:"194667",firstName:"Marijana",lastName:"Francetic",middleName:null,title:"Ms.",imageUrl:"https://mts.intechopen.com/storage/users/194667/images/4752_n.jpg",email:"marijana@intechopen.com",biography:"As an Author Service Manager my responsibilities include monitoring and facilitating all publishing activities for authors and editors. 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The first law of thermodynamics defines that the flowing heat energy is conserved in the absence of heat sources and sinks. It is, therefore, important to study the influence of thermocouple lead wires and distortion due to the thermocouple cavity in solution of the inverse heat conduction problem. According to the second law of thermodynamics, the heat will be transferred from one body to another body only when the bodies are at two different temperatures level and the heat will flow from the point of higher to the point of lower temperature.
\nA direct solution of transient heat conduction equation with prescribed initial and boundary conditions yields temperature distribution inside a slab of finite thickness. The direct solution is mathematically considered as well-posed because the solution exists, unique and continuously depends on input data. The estimation of unknown parameters from the measured temperature history is called as inverse problem of heat conduction. It is mathematically known as an ill-posed problem since the solution now does not continuously depend on the input data. Measurement data error in temperature, thermal lagging, thermocouple’s cavity, signal noise, etc. makes stability problem in the estimation of unknown parameters.
\nNumerical inversion of the integral solution [1], exact solution [2], numerical techniques [3], least-squares method [4], transform methods [5], different series approach [6], variable time-step size [7] have been applied to solve inverse heat conduction problems. Solutions of the ill-posed inverse heat conduction problem have been presented in detail by Beck et al. [8] and Özisik et al. [9]. Tikhonov regularization method [10] has been described for cross-validation criterion for selecting the regularization parameter to obtain a stable approximation to the solution. Kurpisz et al. [11] have presented series with derivatives with temperature to solve inverse thermal problem. Hensel [12] has described space marching numerical methods to solve inverse heat transfer problem. Various mathematical methods and numerical algorithms for solving inverse heat conduction problems are described and compared by Alifanov [13]. Taler and Duda [14] have presented solutions of direct and inverse heat conduction problems.
\nInverse heat conduction analysis provides an efficient tool for estimating the thermophysical properties of materials, the boundary conditions, or the initial conditions. Estimation of surface heat flux has been carried out without [15] and with [16] heat conduction and comparison between them shows discrepancies as high as about 27% [17]. Moving window optimization method [18] has been applied to predict the aerodynamic heating in a free-flight of sounding rocket by comparing numerically calculated and measured temperature history. Howard [19] developed a numerical procedure for estimating the heat flux with variable thermal properties using a single embedded thermocouple. Simultaneous identification of the temperature-dependent thermal conductivity and the asymmetry parameter of the Henyey-Greenstein scattering phase function have been shown by Zmywaczyk and Koniorczyk [20].
\nThe conjugate gradient method with adjoint problem for function estimation iterative technique is used to solve IHCP to estimate heat flux and internal wall temperature of the throat section of the rocket nozzle [21]. Heisler [22] have reported supplementary “short-time” temperature-time charts for the center, mid-location and surface of large plates, long cylinders and spheres for the dimensionless time sub-domain. Convective heat transfer coefficient and combustion temperature in a rocket nozzle is determined using transient-temperature response chart [23].
\nThe solution of transient IHCP can be obtained using analytical or numerical schemes in conjunction with measured temperature-time history. The estimation of the unknown parameters can be carried out by employing gradient or non-gradient methods to predict the unknown parameters in a prescribed tolerance limit. The focus of the present work is to investigate the influence of various parameters on the solution of inverse heat conduction problem.
\nExperimental difficulties [24] are noticed in implanting thermocouples at the surface for temperature measurements. Temperature response delays have been studied to solve IHCP applied to cooled rocket thrust chamber [25]. The temperature measured inside the slab may delay and damp depending on xm\n as illustrated in Figure 1. A thermocouple indicates temperature lag behind the actual temperature. The effect of the thermocouple sensor dynamics on prediction of a triangular heat flux history has been analyzed with simulated data in a one-dimensional domain by Woodbury [26].
\nGeometry of the specimen.
Chen and Danh [27] have carried out experimental studies to obtain transient temperature distortion and thermal delay in a slab due to presence of thermocouple cavity. The distortion of temperature profiles inside the slab may be influenced by the dissimilar thermophysical properties of thermocouple and surrounding materials and by the diameter and depth of the cavity. The temperature distortion [28] inside a slab is a function of the thermocouple cavity diameter d and location xm\n.
\nStandard statistical analysis consists of error in the measurement as an additive of true plus random, in zero mean, in constant variance, uncorrelated, normal, bell shaped probability density function, constant variance known, errors in the dependent variables and no-prior information about the parameters. The error in measurement can be obtain using exact analytical solution [29] as
\nwhere ε and δτ refer to error in measurement of thermocouple location and in time recording, respectively. One of the important points that must be mentioned, here, is the use of a starting solution. In the case of a solid rocket motor where boundary conditions are suddenly imposed by a wall, there will be high intensity of heat flux on cold wall, and the heat flux during the first few steps in time may not be very accurate. The numerical solution is initiated using an exact analytical solution instead of starting from the initial constant condition. Such solutions can be obtained from to exact analytical solution [30] of transient heat conduction equation. Heat transfer rates to the calorimetric probe are estimated from measurements of temperature and rate of temperature change using energy conservation considerations [31].
\nAn optimization method based on a direct and systematic search region reduction optimization method [32] can be employed to estimate the unknown convective heat transfer coefficient in a typical rocket nozzle. The most attractive feature of the direct search scheme is the simplicity of computer programming. The pseudo-random algorithm, an effective tool for optimization, does not require computation of derivatives but depends only on function evaluation. It works even when the differentiability requirements cannot be ensured in the feasible domain. For initiating the search only an estimate of the feasible domain is needed. Therefore, another advantage of the method is that the starting condition is not crucial; any reasonable value will do.
\nThe computation of the turbulent convective heat transfer coefficient from combustion gases to the rocket nozzle wall is based on the Bartz’s equation [33] incorporating the effects of compressibility, throat curvature and variation of transport properties in the boundary layer. The transient heat conduction in a one-dimensional Cartesian coordinate system having two parallel plane surfaces Sn\n (n = 1, 2) of a slab may be written in dimensional form [34] as.
\nwith following initial and boundary conditions:
\nwhere fi\n is initial temperature distribution in the region R of the slab. Eq. (4) represents both convective heat transfer or heat flux condition as applied to the inner surface.
\nWe now consider the constant thermal property solution and can be written in terms of eigen function \n
In the above Eq. (5), Bi or qw\n is the unknown parameter to be determined using measured temperature time history at location xm\n as depicted in Figure 1. In estimating the unknown condition, one has to minimize the absolute difference between the calculated and measured temperature at specified location and time (xm\n, τ) in a prescribed tolerance value using an iteration procedure. The iteration scheme is described in the following sections.
\nThe IHCP is solved by comparing calculated and measured temperature using an iterative technique [30]. In estimating qw\n, one minimizes
\nwhere θc\n and θm\n are the calculated and measured temperatures at (Xm\n, τ), respectively. The computed temperature is a nonlinear function of unknown parameters such as wall heat flux or convective heat transfer coefficient. Temperature is calculated using Eq. (6) and compared with the measured temperature as expressed in Eq. (7). The inverse problem starts with initial guess value of the unknown parameter. The second step is to correct the previous guessed unknown parameter using the Newton-Raphson method. The sensitivity coefficient can be obtained by differentiating temperature with respect to wall heat flux qw\n. The iteration procedure will continue until │F(qw\n)│ ≤ 10−4. This iterative scheme estimates the component of the qw\n at a time and thus may be considered on-line method.
\nThe inverse method for solving a value of qw\n(0, τ) is as follows. Initiate with an initial guess value of qw\n, satisfy the convergence criterion, and implement the Newton-Raphson to obtain the estimate value.
\nNow, it is possible to estimate convective heat transfer coefficient and combustion gas temperature in conjunction with measured temperature history [35]. The equation for converting the calculated heat flux to the heat transfer coefficient is
\nIn the foregoing equation, T\ng is an unknown quantity and can be estimated using again the above-mentioned minimization and iteration methods. The convergence criterion for the iterative scheme remains same as mentioned above.
\nIt is not always feasible to obtain analytical solution of temperature-dependent thermal conductivity and radiation boundary condition. The Crank-Nicolson finite difference method with two-time level implicit numerical scheme [36] has been employed to solve the nonlinear conduction problem with the Newton-Raphson method to consider the radiation boundary condition.
\nDeforming or moving finite elements method [37] is used to solve linear heat conduction equation. The moving finite element [38] is used to consider the time delay in the measurement of back wall temperature.
\nFor only two nodes the system of [39] equations reduce to the following pair of equations:
\nwhere 0 and 1 represent node in a slab of finite thickness. These are the exact solutions to the system of two ordinary differential equations which resulted from a two-node finite-difference approximation to the original problem.
\nwhere \n
Solution of the above simultaneous equation calculates the temperature with a given value of Bi. The solution is now solving simultaneously Eqs. (11) and (12) to determine the unknown parameter.
\nThe influence of constant (average) thermal conductivity, temperature-dependent thermal conductivity, computational grid in numerical solver, nonlinear boundary condition, cylindrical coordinate and the estimation of the wall heat flux and convective heat transfer is carried out by employing measured temperature history of a rocket nozzle of a solid motor. Solution of linear heat conduction equation is used to estimate the convective heat transfer coefficient with the measured temperature data of outer wall of a rocket nozzle. The running time of rocket motor is 16 s. The nozzle wall thickness L = 0.0211 m. The thermo-physical properties of the material are: ρ = 7900 kg m−3, Cp\n = 545 J kg−1 K−1, K (average) = 35 Wm−1 K−1. Initial temperature Ti\n = 300 K and combustion gas temperature Tg\n = 2946.2 K are used in the solution of the heat conduction equation.
\nPrediction of convective heat transfer coefficient is carried out in conjunction with the calculated and measured temperature history at outer surface of nozzle divergent in a solid rocket motor static test. The constant thermal conductivity solution of the linear transient heat conduction problem [30] is
\nFor estimating unknown boundary condition, the heat conduction equation is and solved with the following boundary and initial conditions.
\nand
\nExact analytical solution of transient heat conduction as written in Eq. (13) is used to estimate convective heat transfer on the inner surface of the rocket nozzle. An iterative scheme is used to solve inverse problem [30]. The iteration is carried out till the absolute difference between calculated and measured temperature is less than or equal to 10−4. Table 1 exhibits the comparison between the estimated values of the convective heat transfer coefficient based on the exact solution of heat conduction equation with the calculated values of Bartz [33]. Bartz’s equation calculates conservative estimates for the convective heat transfer to the wall [40].
\n\nt, s | \n\nθ\n0 at inner surface | \n\nθc\n at outer surface | \n\nθm\n at outer surface | \n\nh, W/m2K | \n\nhB\n, W/m2K | \n
---|---|---|---|---|---|
6 | \n0.2950 | \n0.0098 | \n0.0096 | \n1821.9 | \n2254.2 | \n
7 | \n0.3109 | \n0.0159 | \n0.0158 | \n1810.0 | \n2254.2 | \n
8 | \n0.2996 | \n0.0212 | \n0.0211 | \n1610.3 | \n2254.2 | \n
9 | \n0.3244 | \n0.0301 | \n0.0302 | \n1690.9 | \n2254.2 | \n
10 | \n0.3340 | \n0.0386 | \n0.0385 | \n1669.7 | \n2254.2 | \n
11 | \n0.3416 | \n0.0473 | \n0.0472 | \n1641.9 | \n2254.2 | \n
12 | \n0.3302 | \n0.0529 | \n0.0529 | \n1497.6 | \n2254.2 | \n
13 | \n0.3312 | \n0.0602 | \n0.0604 | \n1443.1 | \n2254.2 | \n
14 | \n0.3409 | \n0.0677 | \n0.0676 | \n1387.0 | \n2254.2 | \n
15 | \n0.3442 | \n0.0781 | \n0.0782 | \n1413.0 | \n2254.2 | \n
16 | \n0.3475 | \n0.0862 | \n0.0861 | \n1383.7 | \n2254.2 | \n
Solution of inverse heat conduction problem.
An iteration procedure [41] is employed in conjunction with exact solution to predict convective heat transfer coefficient from the measured temperature-time data at the outer wall of the nozzle as shown in Table 2. The expression for temperature-dependent conductivity is K(T) = k0\n − βT. The value of k0\n and β are 57 Wm−1 K−1 and 2.718 Wm−1 K−2, respectively. The advantage of using the exact solution is found directly at specified location and time as compared to the numerical method which needs the computation from the initial state.
\n\nt, s | \n\nθ(0, τ) | \n\n | \nh, W/m2K | \n|||
---|---|---|---|---|---|---|
Iterative method | \nBeck method | \n\nθc\n(1, τ) | \nθ\nm\n(1, τ) | \nIterative method | \nBeck method | \n|
6 | \n0.0883 | \n0.0838 | \n0.0099 | \n0.0098 | \n536.6 | \n581.7 | \n
7 | \n0.1067 | \n0.1075 | \n0.0158 | \n0.0159 | \n600.6 | \n587.0 | \n
8 | \n0.1144 | \n0.1116 | \n0.0220 | \n0.0212 | \n592.6 | \n598.4 | \n
9 | \n0.1367 | \n0.1367 | \n0.0302 | \n0.0302 | \n674.2 | \n685.3 | \n
10 | \n0.1522 | \n0.1545 | \n0.0386 | \n0.0385 | \n712.9 | \n693.2 | \n
11 | \n0.1654 | \n0.1690 | \n0.0472 | \n0.0472 | \n737.4 | \n730.0 | \n
12 | \n0.1686 | \n0.1639 | \n0.0529 | \n0.0529 | \n718.2 | \n721.9 | \n
13 | \n0.1773 | \n0.1777 | \n0.0605 | \n0.0605 | \n723.6 | \n725.8 | \n
14 | \n0.1844 | \n0.1813 | \n0.0677 | \n0.0676 | \n723.0 | \n725.1 | \n
15 | \n0.1944 | \n0.2040 | \n0.0781 | \n0.0782 | \n753.6 | \n765.0 | \n
16 | \n0.2083 | \n0.2174 | \n0.0862 | \n0.0862 | \n758.3 | \n770.0 | \n
Comparison between iterative and Beck methods.
Deforming or moving finite element is used to consider the time delay in temperature at the outer wall of the slab [37]. Estimated values of wall heat flux and heat transfer coefficient are tabulated in Table 3. It can be observed from the table that the estimated wall quantities are having significant influence on the predicted unknown boundary conditions. This example is extended to consider spatial grid changed and temporal dependence on the numerical solution using moving finite element method [38].
\n\nt, s | \n\nTm\n K at X = 1 | \nUniform grid | \nNon-uniform grid | \nMoving grid | \n|||
---|---|---|---|---|---|---|---|
\nqw\n × 106, W/m2\n | \n\nh\nc, W/m2K | \n\nqw\n × 106, W/m2\n | \n\nh\nc, W/m2K | \n\nqw\n × 106, W/m2\n | \n\nh\nc, W/m2K | \n||
6 | \n326 | \n3.715 | \n1964.5 | \n3.846 | \n2044.9 | \n4.517 | \n2412.1 | \n
7 | \n342 | \n2.700 | \n1408.8 | \n2.848 | \n1449.6 | \n2.818 | \n1485.9 | \n
8 | \n356 | \n2.698 | \n1436.9 | \n2.840 | \n1531.6 | \n2.820 | \n1512.8 | \n
9 | \n380 | \n2.704 | \n1463.0 | \n2.589 | \n1569.8 | \n2.842 | \n1552.8 | \n
10 | \n402 | \n2.705 | \n1491.4 | \n2.858 | \n1603.3 | \n2.846 | \n1586.7 | \n
11 | \n425 | \n2.704 | \n1518.9 | \n2.852 | \n1632.6 | \n2.845 | \n1618.5 | \n
12 | \n440 | \n2.691 | \n1539.7 | \n2.805 | \n1636.2 | \n2.812 | \n1630.8 | \n
13 | \n460 | \n2.683 | \n1564.6 | \n2.776 | \n1649.7 | \n2.791 | \n1650.6 | \n
14 | \n479 | \n2.673 | \n1588.1 | \n2.738 | \n1657.1 | \n2.764 | \n1665.9 | \n
15 | \n507 | \n2.094 | \n1226.4 | \n2.015 | \n1190.6 | \n2.091 | \n1235.4 | \n
16 | \n528 | \n2.086 | \n1231.8 | \n1.981 | \n1178.5 | \n2.067 | \n1231.6 | \n
Wall heat flux at various grid arrangements.
Numerical analysis of nonlinear heat conduction with a radiation boundary condition [36] is carried out to estimate wall heat flux using temperature history on the back wall of the rocket nozzle. The high temperature variation alters thermophysical properties of the material of mild steel. Table 4 shows comparison between the estimated convective heat transfer coefficients with the Bartz solution [33]. Effects of nonlinear IHCP with radiation boundary condition are investigated and results are presented in Table 4.
\n\nt, s | \n\nTo\n, K at X = 0 | \n\nTm\n K at X = 1 | \n\nqc\n × 106 W/m2\n | \n\nh W/m2K | \n\nhB\n W/m2K | \n\nTgc\n K | \n\nTg\n K | \n
---|---|---|---|---|---|---|---|
6 | \n659.8 | \n326 | \n2.3547 | \n950.0 | \n2254.2 | \n3137 | \n2946.2 | \n
7 | \n801.0 | \n342 | \n2.3899 | \n1019.6 | \n2254.2 | \n3122 | \n2946.2 | \n
8 | \n900.7 | \n356 | \n2.2211 | \n992.4 | \n2254.2 | \n3115 | \n2946.2 | \n
9 | \n996.3 | \n380 | \n2.6489 | \n1237.1 | \n2254.2 | \n3113 | \n2946.2 | \n
10 | \n1050.5 | \n402 | \n2.3670 | \n1135.5 | \n2254.2 | \n3108 | \n2946.2 | \n
11 | \n1066.4 | \n425 | \n1.7100 | \n827.3 | \n2254.2 | \n3104 | \n2946.2 | \n
12 | \n1201.8 | \n440 | \n2.8144 | \n1459.2 | \n2254.2 | \n3099 | \n2946.2 | \n
13 | \n1320.0 | \n460 | \n2.6559 | \n1467.0 | \n2254.2 | \n3098 | \n2946.2 | \n
14 | \n1354.8 | \n479 | \n1.7595 | \n991.7 | \n2254.2 | \n3095 | \n2946.2 | \n
15 | \n1383.4 | \n507 | \n1.3810 | \n791.4 | \n2254.2 | \n3094 | \n2946.2 | \n
16 | \n1414.9 | \n528 | \n1.1684 | \n681.8 | \n2254.2 | \n3094 | \n2946.2 | \n
Solution with nonlinear boundary condition.
A grid point shift strategy [42] is adapted to solve inverse conduction problem in a radial coordinate of rocket nozzle with inner and outer radius of rocket nozzle. The inner and outer radius of the nozzle is 0.0839 m and 0.0105 m, respectively. The purpose of the present example to investigate the influence of radial coordinate on the estimated values of heat transfer coefficient. Table 5 shows the effect of geometrical parameters on the predicted heat transfer coefficient.
\n\nt, s | \n\nTo\n K at X = 0 | \n\nTm\n K at X = 1 | \n\nqc\n × 106 W/m2\n | \n\nh, W/m2K | \n\nhB\n, W/m2K | \nθg, K | \nθgc, K | \n
---|---|---|---|---|---|---|---|
6 | \n1260.2 | \n326 | \n3.6805 | \n1789.6 | \n2254.2 | \n3316 | \n2946 | \n
7 | \n1175.9 | \n342 | \n3.3995 | \n1628.0 | \n2254.2 | \n3264 | \n2946 | \n
8 | \n1160.7 | \n356 | \n2.4745 | \n1181.4 | \n2254.2 | \n3255 | \n2946 | \n
9 | \n1165.8 | \n380 | \n2.5385 | \n1194.7 | \n2254.2 | \n3290 | \n2946 | \n
10 | \n1196.0 | \n402 | \n2.5348 | \n1261.1 | \n2254.2 | \n3206 | \n2946 | \n
11 | \n1192.3 | \n425 | \n2.3385 | \n1166.4 | \n2254.2 | \n3197 | \n2946 | \n
12 | \n1205.8 | \n440 | \n2.2094 | \n1114.8 | \n2254.2 | \n3187 | \n2946 | \n
13 | \n1211.0 | \n460 | \n2.1333 | \n1229.5 | \n2254.2 | \n2946 | \n2946 | \n
14 | \n1222.1 | \n479 | \n2.0441 | \n1187.5 | \n2254.2 | \n3943 | \n2946 | \n
15 | \n1237.1 | \n507 | \n2.0626 | \n1206.7 | \n2254.2 | \n2946 | \n2946 | \n
16 | \n1249.1 | \n528 | \n2.0027 | \n1180.9 | \n2254.2 | \n2945 | \n2946 | \n
Inverse problem in a hollow cylinder.
The calculated convective heat transfer coefficients and inner wall temperature are used to determine the wall heat flux and the combustion temperature using Eq. (8). The iterative scheme is based on relation between wall heat flux and convective heat transfer coefficient [35]. Table 6 shows the predicted values of wall heat flux and convective heat transfer coefficient. The IHCP is extended to determine wall heat flux in conjunction with convective heat transfer coefficient. A similar IHCP but referring to the 122 mm medium-range missile during correction engine operation has been considered by Zmywaczyk et al. [43].
\n\nt, s | \n\nT0\n K at X = 0 | \n\nTm\n K at X = 1 | \n\nqc\n × 106, W/m2\n | \n\nh, W/m2K | \n\nhB\n, W/m2K | \n\nTg\n, K | \n\nTgc\n, K | \n
---|---|---|---|---|---|---|---|
6 | \n1355.6 | \n326 | \n3.2502 | \n2631.2 | \n2254.2 | \n3351 | \n2946 | \n
7 | \n1287.8 | \n342 | \n3.2950 | \n1805.3 | \n2254.2 | \n3113 | \n2946 | \n
8 | \n1315.6 | \n356 | \n3.2974 | \n1861.5 | \n2254.2 | \n3087 | \n2946 | \n
9 | \n1368.9 | \n380 | \n3.2967 | \n1885.9 | \n2254.2 | \n3117 | \n2946 | \n
10 | \n1414.4 | \n402 | \n3.2837 | \n1962.1 | \n2254.2 | \n3088 | \n2946 | \n
11 | \n1463.6 | \n425 | \n3.2718 | \n2049.5 | \n2254.2 | \n3060 | \n2946 | \n
12 | \n1370.8 | \n440 | \n2.3825 | \n1476.0 | \n2254.2 | \n2985 | \n2946 | \n
13 | \n1360.9 | \n460 | \n2.4140 | \n1502.1 | \n2254.2 | \n2968 | \n2946 | \n
14 | \n1370.3 | \n479 | \n2.3625 | \n1520.6 | \n2254.2 | \n2924 | \n2946 | \n
15 | \n1382.5 | \n507 | \n2.3675 | \n1517.2 | \n2254.2 | \n2943 | \n2946 | \n
16 | \n1399.3 | \n528 | \n2.3645 | \n1540.7 | \n2254.2 | \n2934 | \n2946 | \n
Wall heat flux and convective heat transfer coefficient.
A two-node exact solution is used to calculate the back-wall temperature as described in Section 3.4. The iterative method described above has been used for estimating aerodynamic heating for a sounding rocket in free flight test. Here, the wall heat flux is estimated using the measured temperature history in conjunction with the iterative technique [30]. The aerodynamic heating rate is estimated for a typical sounding rocket as depicted in Figure 2. The location of thermocouple is marked in the diagram. The thermophysical properties of Inconel and wall thickness are k = 18 Wm−1 K−1, α = 4.47 × 10−6 m2/s, L = 0.7874 × 10−3 m. Figure 3 depicts the measured temperature time history at different locations measured from the tip of the cone in the free flight of a sounding rocket as delineated in Figure 2. It can be observed from temperature history that the initial time delay in thermal response is 6 s. The unknown qw\n are estimated using an iterative technique which starts with an initial value of wall heat flux and is repeated until |F(qw\n)| ≤ 10−4.
\nSchematic sketch of sounding rocket showing location of thermocouple.
Measured temperature history in free flight of the sounding rocket.
A two-node exact solution is used to calculate the wall temperature distribution. The unknown qw\n are estimated using an iterative technique which starts with an initial value of wall heat flux and is repeated until |F(qw\n)| ≤ 10−4. Figure 4 displays the estimated variation of the wall heat flux as a function of flight time of the sounding rocket.
\nVariations of wall heat flux vs. flight time.
The wall heat flux variation depends on the sounding rocket speed. The increase and decrease of the aerodynamic heating are a function of flight Mach number.
\nThe estimated wall heat flux is compared with Van Driest’s results [44]. Table 7 depicts the estimated values of wall heat flux as a function of flight time at thermocouple location 29 as shown in Figure 2. It can be observed from the table that highest aerodynamic heating occurs during 7–8 s, another significant peak wall heat flux was found at 22 s.
\n\nt, s | \n\nTm\n, K | \n\nTc\n, K | \n\n\n | \n\n\n | \n
---|---|---|---|---|
6 | \n313.0 | \n320.0 | \n2.756 | \n8.246 | \n
7 | \n341.3 | \n349.4 | \n16.695 | \n14.82 | \n
8 | \n408.0 | \n412.3 | \n19.387 | \n22.647 | \n
9 | \n469.7 | \n469.3 | \n8.657 | \n18.876 | \n
10 | \n495.2 | \n495.8 | \n8.145 | \n10.117 | \n
11 | \n504.1 | \n513.3 | \n9.302 | \n4.569 | \n
12 | \n502.4 | \n521.2 | \n2.757 | \n1.176 | \n
13 | \n495.2 | \n506.8 | \n−7.695 | \n−0.977 | \n
14 | \n487.4 | \n487.6 | \n−0.040 | \n−2.320 | \n
15 | \n477.4 | \n477.0 | \n−0.037 | \n−3.134 | \n
16 | \n467.4 | \n467.0 | \n−0.028 | \n−3.578 | \n
17 | \n457.4 | \n457.5 | \n−0,034 | \n−3.769 | \n
18 | \n445.8 | \n447.2 | \n−0.905 | \n−3.789 | \n
19 | \n438.6 | \n437.5 | \n−0,005 | \n−1.628 | \n
20 | \n444.1 | \n445.9 | \n5.173 | \n4.135 | \n
21 | \n469.1 | \n467.5 | \n13.518 | \n11.524 | \n
22 | \n533.0 | \n521.2 | \n20.618 | \n19.732 | \n
23 | \n556.3 | \n558.4 | \n9.180 | \n13.122 | \n
24 | \n567.1 | \n573.5 | \n6.514 | \n8.581 | \n
25 | \n584.1 | \n587.2 | \n8.592 | \n5.467 | \n
26 | \n596.9 | \n602.2 | \n7.018 | \n3.314 | \n
Comparison between calculated and Van Driest’s heat flux at location 29.
Analytical, transient numerical and two-node methods are used to compute temperature distribution in a finite slab. Numerical solution is carried out with temperature-dependent thermal conductivity. Implicit finite difference scheme with two-time level technique is implemented to solve nonlinear problem of heat conduction. Time delay is studied using finite element method with deforming grid strategy. A boundary shifting numerical scheme is used to solve transient heat conduction in radial coordinate. Evidence of temporal accuracy and dependence on time-step is demonstrated in the numerical solving of IHCP. Influence of thermocouple cavity and measurement errors in location and time are discussed. The IHCP is applied to predict the wall heat flux in a rocket nozzle of a solid motor. Wall heat flux is estimated in a free flight of a sounding rocket using the two-node method.
\nBiot number, hL/k\n
\nspecific heat
\nheat transfer coefficient
\nthermal conductivity, k(θ)/k0\n\n
\nreference thermal conductivity at Ti\n\n
\nslab thickness
\nnondimensional parameter, αΔT/(Δx)2\n
\nwall heat flux
\ntemperature
\ntime
\ndistance from the inner surface
\ndimensionless coordinate
\nthermal diffusivity
\ndensity
\nnondimensional temperature, = (T − Tg\n)/(Tg\n − Ti\n)
\nnondimensional time, αt/L2\n\n
\nBartz
\ncomputed
\ncombustion gas temperature
\ninitial value
\nmeasured
\nouter wall
\nwall
\nconstant thermal conductivity coefficient
\nSolid waste can be broadly classified as putrescible and non-putrescible, based on its biodegradability. Putrescible waste contains organic matter. This waste is suitable for digestion and land disposal. Non-putrescible waste is generally non-biodegradable waste which cannot be digested. Municipal solid waste contains food waste, papers, plastic, paints, heavy metals and rubber. Municipal waste needs to be classified based on biodegradability for further treatment. Local civic bodies are now putting stringent norms for classification of solid waste. In India green and blue containers are provided to households to separate this waste and source. Industrial solid waste may contain, waste adsorbent, waste catalyst sludge, solid residue of by-product, residue of reactions, etc. This solid waste may contain hazardous material also. Dewatering, centrifugal filtration, drying and incineration are usual steps used for solid waste treatment in industries. Bio-degradable solid waste, rich in organic content can be used to synthesize various useful organic compounds. Non-biodegradable waste like plastic, rubber can be reused or recycled. Reduce, reuse and recycle are nowadays trending concepts in solid waste management. Non-government organizations (NGOs) in developing countries are playing key role in developing awareness among people about proper segregation and collection of solid waste. Recycling industry is promoted by government through various schemes and initiatives. This chapter briefly explains initiatives and investigations aimed at various solid minimizations, reuse and recycle methods and methods used for synthesis of value-added products from solid wastes. Initiatives taken by governments; non-government organizations are briefed in the chapter. Also, investigations carried out by scientific community to treat and recycle solid waste are reviewed. The chapter contains efforts taken for solid waste recycle and reuse in Asian countries, though it contains some significant efforts in other developing countries also. This review is based on available literature, research papers and available reports on solid waste management.
Solid waste contains bio-degradable and non-bio-degradable material. Non-bio-degradable material cannot be digested and hence reuse or recycle of this type of waste is becoming important area of investigation. Countries like China, Taiwan and Malaysia are taking initiatives to reduce plastic waste by reuse and recycle principle. First three sections (Sections 3–5) of the chapter are devoted to plastic and non-bio-degradable waste. In remaining sections, reuse, recycle, recovery and energy generation methods for biodegradable waste are explained with the help of available literature and research papers. Domestic and municipal solid waste treatment needs to be more familiar with people. For this, efforts are being taken by government authorities by adopting regulations and stricter norms. These regulations along with awareness created by social groups and organizations can improve waste management scenario in developing countries. Another aspect of solid waste treatment discussed in this chapter is investigations carried out by researchers to optimize the waste reuse and recycle technologies. This aspect is briefed with the help of research papers published by investigators from these developing countries.
Plastic bags are used for containing and transporting goods. Also, they are used for vegetables, groceries and other domestic items as a container. Plastic, which sometimes is non-replaceable, is very important material if used sensibly. The plastic bags are very thin and flexible. The disposal of these plastic bags is creating huge problems in developing countries. If these bags are recycled, the disposal problem would not arise. But lack of awareness and willpower has played a great roll in plastic ban. Nowadays the governments have banned the use of plastic bags above certain thickness. Even many other civic bodies are banning plastic use. Studies show that increase in reuse of plastic can reduce the eco-impact of plastic to a great extent [1]. In developing countries, blockage of drainage due to plastic causes calamities such as flood. Also, it can be a reason for mosquito breeding. Lack of sophistication of the recycle and waste treatment facility develops concern about manufacture and use of plastic [2]. Many developing countries in Africa have adopted use of glass container instead of plastic. They are promoting use of cloth bags instead of plastic bags [3, 4].
Waste plastic and rubber can be used in road construction [5]. Semi-dense bitumen concrete can be prepared and used for road construction. Waste plastic material such as high-density polyethylene (HDPE-2), low-density polyethylene (LDPE-4), poly propylene (PP-5) and polystyrene (PS-6) can be used for obtaining different products [6]. Slurry formation, liquefaction, recovery and condensation are the steps in the process. Use of superplasticizer can enhance the properties of waste plastic in road construction [7]. Biomedical plastic waste finds application in road construction. Compared to normal the bituminous mix, bio-medical plastic waste coated mix had better properties [8]. Pyrolysis oil can be derived from the waste plastic and can be used to derive diesel. Studies indicate that this diesel is suitable for use in engine [9]. Use of plastic waste in the flexible pavements increases strength and durability [10, 11]. Bitumen requirement can be reduced by 8–12% by using plastic waste for pavement material [12]. Thermal cracking of waste plastic can convert them into usable oil form [13]. Also, plastic bottles can be used for the construction of house. It is observed that these houses are bioclimatic. It means that when it is cold outside is warm inside and vice versa [14].
Discarded, obsolete, end of life electrical and electronics equipment forms Electronic waste (E-waste). Heavy metals such as lead, cadmium, chromium, mercury, barium is present in E-waste [15]. The E-waste recycling needs quantitative measures for recycling and reuse of E-waste [16]. Illegally imported E-waste from developed countries is additional E-waste problem faced by India like countries [17]. There is need for increasing awareness about health effects of E-waste and importance of recycling. Inventorization and unhealthy conditions of informal recycling, inadequate legislation, poor awareness and reluctance on part of the corporate to address solid waste issues are drawbacks of waste minimization programs in India [18]. Waste materials from discarded computers, televisions, stereos, copiers, fax machines, electric lamps, cell phones, audio equipment and batteries can be hazardous to health. For example, lead can leach out from the E-waste materials, and enter into human bodies through oral route [19]. According to Kumar and Shah, the crude recycling activities cause irreversible health and environmental hazards [20]. So, there is need of refinement of the process adopted for recycle. According to Kumar and Karishma, India is fifth largest producer of E-waste in the world. In India only recycling of E-waste is 10% of recycle business [21]. About 65% of E-waste is generated in urban Area in India [21]. About 21% of this E-waste is plastic. E-waste is fastest growing waste stream in the world [22, 23]. Around seven lakh tons of E-waste were produced in India in 2016 [24]. Individual and government contributions can help to tackle this E-waste problem [25]. It is important to bridge the gap between the formal and informal divide in E-waste management in India [26]. E-waste recycling provides jobs to thousands of people in India. There needs to be coordination between formal and non-formal sectors for proper treatment and recycling of E-waste. There is need for the collection, segregation and primary dismantling of non-hazardous fractions of E-waste. Compatible and efficient technology for E-waste was a matter of concern for India and many developing countries. According to Vats and Singh, informal recyclers are treating 95% of the E-waste generated with hazardous practices [27].
Food waste can be used for synthesis of various useful chemicals. Source separated food waste can be used for synthesis of ethanol with thermophilic enzymes [28]. Food waste biomass can be used in treating wastewater. Anaerobic digestion of this waste upon acidogenesis produces volatile fatty acids [29]. Ethanol cultivated biomass can be used effectively for the effluent of the food waste digestion. Food waste can be processed in long-term operation of a laboratory anaerobic reactor in mesophilic conditions for anaerobic fermentation to produce biogas and useful products [30]. Shukla et al. have explored the possibility of biohydrogen production from food waste [31]. Degradation of food waste and energy recovery through biogas production are twin benefits of the anaerobic digestion [32]. Factors such as organic loading rate, temperature, time, pH, carbon to nitrogen ratio play vital role in the process. With increase in methanogenic bacteria, the methane percent in biogas increases significantly [33]. An investigation by Akpan indicated that producing ethanol from food waste is more economical than producing it from other waste organic sources like old newspapers [34]. For synthesis of biohydrogen from waste, methods such as the methods like electrolysis of water, steam reforming of hydrocarbons and auto-thermal processes can be used [35]. According to Kapdan and Kargi, use of photosynthetic algae is one of the important methods for hydrogen synthesis from waste [36]. Investigations are reported on synthesis of bioplastic from food waste. Ingredients from food waste such as starch, cellulose, fatty acids, sugars and proteins can be used for bioplastic synthesis [37]. Many investigations are reported on hydrolysis of food waste and subsequent ethanol formation [38, 39]. Various investigations are reported on synthesis of lactic acid, vinegar and citric acid from waste materials including food waste [40, 41, 42, 43].
Anaerobic methods reduce the sludge volume significantly and produce biogas fuel. Major disadvantage of this method is that it causes nuisance to nearby population [44, 45]. Aerobic thermophiling composting reduces odor problem [46]. pH, temperature, moisture content, organic carbon, volatile solids are vital factors during aerobic composting [47]. Also, C/N ratio and volume reduction are performance indicators of the process [48]. Obtaining optimal performance system is very vital in increasing acceptability of the waste treatment method [49]. Waste management strategy includes many steps such as disposal, treatment, reduction, recycling, segregation and modification [50].
Vermicomposting has advantages over aerobic and anaerobic digestion methods as it overcomes few drawbacks like odor, space and cost of these two methods. Vermicomposting is a method used to convert organic waste into fertilizers with the help of worms. Factors affecting the process are parameters like the growth rate (pH), number of worms, number of cocoons and worm biomass [51]. Bedding material has also influence on the process. Newspaper bedding was effective in the investigation carried out by Manaf et al. [51]. Studies have shown that vermicomposting improves the soil structure, enhancing soil fertility, moisture holding capacity and in turn increase the crop yield [52, 53]. Vermicomposting derived liquid can be used for agriculture [54]. This liquid has very high nutrient value. Studies confirm that home composting has potential to reduce the greenhouse gas emission [55]. Investigation carried out by Kulkarni and Sose indicated that pH values between 6.4 and 7.6 are favorable for vermicomposting. 30–50% moisture is required for vermicomposting [56]. Optimum temperature lies between 25 and 30°C.
Paper waste can be used for applications like biofuel synthesis and ceiling boards, bioelectricity production, and fuel gas generation. Also, it can be used in mixed concrete. Papers are normally recycled. In order to prepare good quality paper only limited number of recycles can be done. So finally, it results into huge amount of waste, this waste sludge can be used in the concrete up to 30% concentration, as investigation revealed that up to 30% addition the concrete quality increases and it decreases after that [57]. Also, waste paper sludge can be used for biofuel synthesis. The sludge can be converted into simple fermentable sugar by microbial process [58]. The waste sludge can be mixed in 1:1 proportion with calcium carbonate additive to form good quality ceiling boards [59]. Detachment of ink from the-waste papers increases their drainability [60]. According to Allahvakil et al. [60], it is possible to modify the chemical or physical bonds with enzymes such as pectinase, cellulase and hemicellulose. This helps in detachment of ink from the paper. The waste papers can also be used as raw material for bioelectricity generation. Microbial fuel cell with Clostridium species can be used for the purpose [61]. According to research carried out by Mathuria and Sharma [61], a microwave plasma reactor can be used for conversion of waste papers to fuel gas. Waste paper sludge ash can be used for stabilization of clay soil. An investigation by Khalid et al. [62] indicated that the waste sludge ash up to 10% can exhibit excellent binding properties in the clay. According to Arshad and Pawade [63], the addition of waste paper also reduces the quantity of clay required.
Electronic and mobile component contain valuable materials like gold and platinum. Ammonium thiosulfate can be used for leaching gold from mobile circuit boards [64]. According to Chehade et al. [65], the printed circuit board contains about 0.15% of gold. Aqua regia can be used as a leaching agent for recovery of gold [66]. This process can be automized to provide solution to gold recovery [67]. Fibrous ion exchange resins can improve gold and platinum recovery. Catalyst industry waste contains gold, platinum and valuable metals [68]. About 3 vol% NaClO, 5 kmol/m3 HCl and 1 vol% H2O2 can be used for leaching platinum compounds [69]. In case of hydrochloric acid (HCl), the recovery is 99%. Platinum and gold removal from the industrial waste is necessity from ecological and environmental point of view [70].
Factors such as pH, organic loading, moisture content plays significant role in biogas production. Various types of biomass like fruit waste, domestic waste and crop residues can be used for biogas production. Pineapple waste biomass 48% concentration in biogas was obtained in less than 50 days [71]. Cow dung is also very good source of biomass. Paper waste exhibits highest methane concentration in biogas, about 73% than other solid wastes such as cow dung, saw dust, rice husk and millet waste. However, hydrogen sulfide concentration is highest in this biogas [72]. A mixture of equal percentage of paper waste and biomass can be used for biogas production to increase quality of biogas. It is observed that the biogas production increases by 50% than paper waste alone. In case of orange peels, it is needed to pre-treat the peels as that content limonene, which is antimicrobial [73]. Many such investigations are reported on biogas synthesis from various type of solid waste [74, 75, 76, 77]. Disposal of the final sludge from treatment plants needs to undergo drying and further incineration or dumping of dry biomass [78].
Putrescible solid waste like food and fruit waste, food grain waste, vegetable waste can be used for production of various products by employing bioconversion with suitable bacteria or microorganism [79]. Single cell protein can be obtained from orange peels and cucumber peel by using Aspergillus niger and Saccharomyces cerevisiae [79, 80]. These investigations suggested that glucose addition to the supplemented fruit hydrolysate medium. Solid state fermentation of orange peels with Aspergillus niger yields pectinase [81]. Content of ammonium sulfate, glucose and water in the culture medium affects the process [81]. Ethanol synthesis from fruit and other biodegradable waste is very common method of utilizing waste [82, 83, 84, 85, 86, 87]. Number of other products such as citric acid, acetic acid, lactic acid, lactic acid, etc. can be obtained by using suitable microorganisms and operating conditions [84, 85, 86, 87]. These conditions differ from product to product and waste type.
Hazardous waste poses serious problem to human being and environment. These hazardous wastes may contain biological waste, nuclear waste, heavy metals and flammable materials to considerable extent. Stricter laws and their implementation are required to save the environmental from the hazardous waste [88]. Proper classification and monitoring of hazardous waste can help to treat the waste efficiently [89]. Incineration and recycling are two most sustainable waste management practices [90, 91].
Bio-degradable solid waste, rich in organic content can be used to synthesize various useful organic compounds. Non-biodegradable waste like plastic, rubber can be reused or recycled. Reduce, reuse and recycle are nowadays trending concepts in solid waste management. Non-government organizations (NGOs) in developing countries are playing key role in developing awareness among people about proper segregation and collection of solid waste. Recycling industry is promoted by government through various schemes and initiatives. Local civic bodies are now putting stringent norms for classification of solid waste. In India green and blue containers are provided to households to separate this waste and source. Industrial solid waste may contain, waste adsorbent, waste catalyst sludge, solid residue of by-product, residue of reactions, etc. This solid waste may contain hazardous material also. Dewatering, centrifugal filtration, drying and incineration are usual steps used for solid waste treatment in industries. In developing countries, blockage of drainage due to plastic causes calamities such as flood. Also, it can be a reason for mosquito breeding. Lack of sophistication of the recycle and waste treatment facility develops concern about manufacture and use of plastic. Following observations were made based on study of literature on solid waste treatment.
Many developing countries in Africa have adopted use of glass container instead of plastic.
Compatible and efficient technology for E-waste was a matter of concern for India and many developing countries.
Various investigations are reported on synthesis of lactic acid, vinegar and citric acid from waste materials including food waste.
Waste management strategy includes many steps such as disposal, treatment, reduction, recycling, segregation and modification.
Various types of biomass like fruit waste, domestic waste and crop residues can be used for biogas production.
Studies have shown that vermicomposting improves the soil structure, enhancing soil fertility, moisture holding capacity and in turn increase the crop yield.
Paper waste can be used for applications like biofuel synthesis and ceiling boards, bioelectricity production, and fuel gas generation. Also, it can be used in mixed concrete.
Hazardous waste poses serious problem to human being and environment. These hazardous wastes may contain biological waste, nuclear waste, heavy metals and flammable materials to considerable extent. Stricter laws and their implementation are required to save the environmental from the hazardous waste.
Platinum and gold removal from the industrial waste is necessity from ecological and environmental point of view.
IntechOpen's Authorship Policy is based on ICMJE criteria for authorship. An Author, one must:
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\n\nIf it is felt necessary to make changes to the list of Authors after a manuscript has been submitted or published, it is the responsibility of the Author concerned to provide a valid reason to amend the published list. Additionally, all listed Authors must verify and approve the proposed changes in order for any amendments to be made.
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\n\nAuthors are responsible for ensuring all addresses and emails provided are correct. Under affiliation(s) all Authors should indicate where the research was conducted. Please note that no changes to the affiliation(s) can be made after the chapter has been published.
\n\nPolicy last updated: 2017-05-29
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