Aalborg Universitet. Simulation of Simple Test Case 2D1 Two-Dimensional Isothermal Forced Convection Skovgaard, M.; Nielsen, Peter Vilhelm

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Downloaded from vbn.aau.dk on: April 25, 219 Aalborg Universitet Simulation of Simple Test Case 2D1 Two-Dimensional sothermal Forced Convection Skovgaard, M.; Nielsen, Peter Vilhelm Publication date: 1991 Document Version Publisher's PDF, also known as Version of record Link to publication from Aalborg University Citation for published version (APA): Skovgaard, M., & Nielsen, P. V. (1991). Simulation of Simple Test Case 2D1: Two-Dimensional sothermal Forced Convection. Aalborg: Dept. of Building Technology and Structural Engineering, Aalborg University. Gul Serie, No. 1, Vol.. R9131 General rights Copyright and moral rights for the publications made accessible in the public portal are retained by the authors and/or other copyright owners and it is a condition of accessing publications that users recognise and abide by the legal requirements associated with these rights.? Users may download and print one copy of any publication from the public portal for the purpose of private study or research.? You may not further distribute the material or use it for any profit-making activity or commercial gain? You may freely distribute the URL identifying the publication in the public portal? Take down policy f you believe that this document breaches copyright please contact us at vbn@aub.aau.dk providing details, and we will remove access to the work immediately and investigate your claim.

NSTTUTTET FOR BYGNNGSTEKNK DEPT. OF BULDNG TECHNOLOGY AND STRUCTURAL ENGNEERNG AALBORG UNVERSTETSCENTER AUC AALBORG DANMARK nternational Energy Agency, Energy Conservation in Building and Community Systems, Annex 2: Air Flow patterns Within Buildings M. SKOVGAARD & P. V. NELSEN SMULATON OF SMPLE TEST CASE, CASE 2D1 (Two-Dimensional sothermal Forced Convection) SEPTEMBER 1991 SSN 92-7513 R9131

NSTTUTTET FOR BYGNNGSTEKNK DEPT. OF BULDNG TECHNOLOGY AND STRUCTURAL ENGNEERNG AALBORG UNVERSTETSCENTER AUC AALBORG DANMARK nternational Energy Agency, Energy Conservation in Building and Community Systems, Annex 2: Air Flow patterns Within Buildings M. SKOVGAARD & P. V. NELSEN SMULATON OF SMPLE TEST CASE, CASE 2Dl (Two-Dimensional sothermal Forced Convection) SEPTEMBER 1991 SSN 92-7513 R9131

nternational Energy Agency Energy Conservation in Building and Community Systems Annex 2 : Air Flow patterns within Buildings Subtask 1 : Room Air and Contaminant Flow RESEARCH TEM 1.46dk SMULATON OF SMPLE TEST CASE, CASE 2D1 (two dimensional isothermal forced convection) Author Date Report no. Report typ(f Distribution 1 Available Skovgaard, M. and Nielsen, P.V. The University of Aalborg, Department of Building Technology and Structural Engineering. Sohngardsholmsvej 57, 9 Aalborg, Denmark May the 1st. 1991 (revised 25.7.91). Annex report. Unlimited. The University of Aalborg. Table of contents Ust of figures Summary Acknowledgements ntroduction Simulation method Numerical model Computer code Test case - geometry and boundary conditions Results and discussion Comparisons with LDA measurements Other numerical predictions References 3 3 3 4 5 5 5 9 9

LST OF FGURES Fig. 1. The geometry of test case 2Dl. Fig. 2. The predicted velocity field U /U and the distribution of turbulent kinetic energy k~/u Fig. 3. Measured and simulated flow profiles. Fig. 4. Comparisons between predicted and measured values in cross section y = h/2 and y=h-h/2. Fig. 5. Decay of the maximum velocity in the wall jet. Fig. 6. The growt~ in \Yall jet width. Fig. 7. Predictions_ of t~e velocity distribution in the two.:.dimensional test case. SUMMARY.. The turbulent flow pattern is calculated with a low Re number version of the k-e model in a room with two-dimensional isothermal flow. The results are compared both to LDA measurements obtained in a scale model and to other data obtained by numerical simulation. The overall performance is good and indeed satisfactory. With respect to maximum velocity and turbulence level in the occupied zone the results are very good and with respect to th~ decay of the maximum velocity in the wall jet and the growth of jet width small discrepancies are found. ACKNOWLEDGEMENTS This report is partly made while one of the authors (Skovgaard, M.) stayed at UMST, Manchester, UK. The authors would like to send many thanks to the staff of UMST, who made the stay very pleasant and especially we would like to thank Dr. N. nze and Prof. B. Launder who have been very supportive and participating throughout the work at UMST.

3 NTRODUCTON This annex 2 report shows the results of the simulation of the test case given by Nielsen (199). The test case is two-dimensional and is chosen because of the detailed experimental data available. The experimental result is obtained by the laser-doppler anemometry technique Restivo (1979) and Nielsen et al (1978). SMULATON METHOD Mathemati~al model.. The numerical predictions are obtained by a numerical solution of the time averaged momentum equations, the continuity equation and an Eddy viscosity concept for the turbulent Reynolds stresses. The governing equations for two-dimensional steady, isothermal flow are a -(PU) = & a ap a [ [ a~ a 1] -] -(puu) = -- +- jl -+- - puu & J ax, ax, & & J 1 J (1) (2) For description of the Reynolds stresses several models can be adopted, see Pate! et al (1985). Here the Launder-Sharma (1974) version of the!ones-launder (1972) low Reynolds number k-e model is used (for detailed description see also nze (1989)) : _ 2 [a~ a 1] puu = -o.. pk -ut-+- 1 J 3 J r & &. J e.. e - 2# ~[a{f] 2 pdxj &j (3) (4) a a [( llt J ak J -(P~k) = - jl- - + P - pe ~ ~ ak dxj (5)

4 where P is the generation rate due to turbulent shear effects p = -u.~ _a~ dx,.. J The values of the turbulent model constants and functions can be seen in the table below.9 1.44 1.92 1.3.9 1.44 1.92 2 1.3 exp(-3.4/(1 + Rtf5) 2 ) 1-.3exp(-Rt 2 ) p k2 R = -- r ~ f Computer code The two-dimensional elliptic flow solver TEAM (Huang (1986)), which has been extensively used and validated, was used to obtain the flow solutions. The code.is using the finite volume technique employing the staggered grid layout to overcome the checkerboard phenomenon. The solution scheme used is SMPLE and the differencing scheme is PLDS for all terms. A non-uniform grid is used in order to produce a finer grid in the boundary layer. n fact the solution is rather sensitive to grid layout if coarser grids are used, especially in the region 5 < y + < 3. The equations are solved line by line in an AD iterative manner. As expected the convergence is rather slow because of the slow diffusive process in the boundary layer and because of the fine grid required.

5 TEST CASE - geometry and boundary conditions The geometry of the test case is L/H=3., h/h=.56 and t/h=.16 (see fig.1) and the actual dimensions used in the present simulation are H=3.m, L=9.m, h=.168m and t =.48m. As pointed out in the specification the inlet opening is rather large compared to practical diffusers (it can be mentioned that the ratio a ~/H is equal to.35 in the three-dimensional test case), but this will only make it easier to use a standard k-e model. n the present case where a low Re number k-e model is used it is necessary to use fine grid in the opening because of the inlet location close to the ceiling. The grid used is 38x78. - - nlet +-+ :::- ;------------~---- Yi H ----------------llk-----lt Outlet L Fig. 1. The, geometry of test case 2Dl. The bound~ry conditions for the test case are : nlet Outlet Wall U =5,u/(ph) =.455 m/s V =. ~= 1.5(.4) 2 E=~LS /(h/1) Uout= Uoh/t =.159 m/s dv dx =de/ dx = dk/ dx =. U=V=E=k=O.O RESULTS AND DSCUSSON Comparisons with LDA measurements Figure 2 shows the predicted velocity field and the distribution of turbulent kinetic energy. Fig. 3 shows the comparison between the computed velocity and kinetic energy profiles. As seen the overall agreement is very good. t is seen that the inlet conditions for ~ have very little effect on the turbulence level in a distance from the inlet, which again m~ans

that the turbulence is created by the shear effect. The k 1 / 2 level can be compared to the measured level of (u 2 ) 1 1 2 (Nielsen 199). t is noted that the decay of Umax is sligthly higher than in the measurements which becomes more evident in fig. 5. 6 ~ ~ ~ ~ '\ \ \ - ' ~ ll ~~ Fig. 2. The predicted velocity field U /Uo and the distribution of turbulent kinetic energy k 2/U(f.2.4.6..2 U/ U t> {::2/Uo -U/U ---- {k /Uo ziw=. Fig. 3. Measured and simulated flow profiles. n fig 4. results from two cross sections in the y-direction are compared with measured data.

7 U/U, Otu, Vk/U. 75. y = h/2 U/U {:;2/Uo 6 U/U -- -.fktu ----.5.25 o.o6,. / -- ------------- -.25 ~--------~~--------~---------~ U/Uo, 2. x /H ~/Uo,~----------------------------~ -{l(iuo.5 Y= H-h/2 c9. 25 -.25 2. x/h Fig. 4. Comparison between predicted and measured values in cross section y = h/2 and y = H h/2.

The effect from the shear layer outside the potential core of the jet is seen. t is seen that the recirculating flow recorded in the measurements in both cross sections is predicted in the simulation, although the magnitude of the counter flow is too low. The maximum velocity in the occupied zone is well predicted both with respect to location and to magnitude. Ux/Uo 8.8.6.4 o Restive (1979) -- Present simulation (1991) ---- Myers et al. (1963) - - Schwarz and Cosart (1961).2.4.8 1.5 2. 2.5 3. x/h Fig. 5. Decqy of the maximum velocity in the wall jet. y1/2/h 4..--------------------------------------~~~ 3. 2. o Restive (1979) --- Present simulation (1991) ---- Myers et al. (1963) - - Schwarz and Cosart (1961) - - Sigalla (1958) 1 2 3 4 5 x/h Fig. 6. The growth in wall jet width. The decay of the maximum velocity and the downstream growth of the jet width are

depicted in fig 5 and 6. The velocity decay is slightly overpredicted and it can be seen that the faster decay corresponds to a faster growth in the jet width than recorded in the experiments (fig. 6). No investigation of grid dependency of the solution has been carried out so it is possible that some numerical diffusion may be present. 9 Other numerical predictions y/h O.b,...----,------,-----,.---.-------""l"'h":l:---"'1.2.6 x/h =2. z/w =.. / cw /. / b.4 / / /. / / "/ / /.8 o Nielsen et al. (1978) -- Nielsen et al. (1978) - - Nielsen (1976) - - Davidson and Olsson (1987 ) ---- Davidson and Olsson (1987) - 2..2.4.6 U/U Fig. 7. Predictions of the velocity distribution in the two-dimensional test case. Fig. 7 shows some other numerical predictions which can be used for comparisons. The measurements are made by Restivo 1978 and reported by Nielsen et al 1978. One set of predictions is made by the TEACH-T code and a k,e turbulence model with wall functions (Nielsen et al 1978). Fig. 7 also shows some old predictions made by vorticity-stream function as dependent variables and a k,e model. The predictions are made at a Reynolds number of 71 and the inlet conditions are given by a box method. The predictions by Davidson and Olsson 1987 are made by a k,e model and with a oneequation turbulence model. The one-equation model is giving a lower velocity level in the wall jet below the ceiling, see fig. 7. REFERENCES Davidson, L. and Olsson, E. Calculation of Some Parabolic and Elliptic Flows Using a New One-Equation Turbulence Model. Proc. 5th. nternational Conference on Numerical Methods in Laminar and

1 Turbulent Flow. Montreal. 1987. Huang, P. G. and Leschziner, MA. An ntroduction and guide to the computer code TEAM. UMST Mechanical Engineering Dept. July 1983. nze, N.Z. and Launder, B.E. On the Computation of Buoyancy-driven Turbulent Flows in Rectangular Enclosures. nt. J. Heat and F~uid Flow: Vol. 1, No. 2. June 1989. ]ones, W.P.. and Launder, B.E. nt. J. Heat and Mass Transfer, 15, 31. 1972. Launder, B.E. and Sharma, B.L Letters in Heat Mass Transfer, 1, 131. 1974. Myers, G.E., Schauer, 11 and Eustis, RH. The Plane Turbulent Wall Jet. Jet Development and Friction Factor. Trans. AS.M.E., J. Basic Eng., 85, p. 47. 1963. Nielsen, P. Jl}, Flow in Air Conditioned Rooms (English translation of Ph.D. thesis, Technical University of Denmark, 1974), Danfoss A/S, Denmark. 1976. Nielsen, P. V.~ Restivo, A. and Whitelaw, 1H. The Velocity Characteristics of Ventilated Rooms. Journal of Fluids Engineering. vol. 1, pp. 291-298. Sept. 1978. Nielsen, P. V. Specification of a Two-Dimensional Test Case. nternal report for the nternational Energy Agency, Annex 2. University of Aalborg, Denmark. SSN 92-7513 R94. Nov. 199. Restivo, A. Turbulent Flow in Ventilated Rooms. Ph.D. Thesis. mperial College, LondQn. March 1979. Schwarz, W.H. and Cosart, W.P. The Two-Dimensional Turbulent Wall Jet. J. Fluid Mech. Vol. 1. 1961. Sigalla, A. Measurements of Skin Friction Factor in a Plane Turbulent Wall Jet. J.R. Aeronaut., Soc., 62, p. 873. 1958.