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Thomes

This method, though comparatively simple, is attended by several disadvantages there is a [Pg.19]

It is better to employ some method by which the change of receiver may be effected without, admitting air at all, and there are two forms of apparatus in general use by means of which this may be done. [Pg.19]

Bredt s Apparatus.—To the end of the delivery tube from the still-head is attached a round-bottomed flask with a long neck to which are sealed three narrow tubes a, b, and c, approximately at right angles to it (Fig. 11), and a fourth 0 2 [Pg.19]

—Bredt s apparatus for distillation under reduced pressure. [Pg.19]


J. B. Weaver and H. C. Thome, eds.. Investment Appraisalfor Chemical Engineers, AIChE Symposium Series No. 285, American Institute of Chemical Engineers, New York, 1991. [Pg.452]

Prior, J., Wallace, D., Hamer, A. and Powers, N., A sprayable hemostat containing fibrillar collagen, bovine thrombin, and autologous plasma. Ann. Thome. Surg., 68, 479-485 (1999). [Pg.1128]

Thome et al. (2004) and Dupont et al. (2004) proposed the first mechanistic analysis for vaporization in a micro-channel, with a three-zone flow boiling model describing... [Pg.43]

Fig. 2.28 Schematic of three-zone vaporization model. Reprinted from Thome et al. (2004) with permission... Fig. 2.28 Schematic of three-zone vaporization model. Reprinted from Thome et al. (2004) with permission...
Fig. 2.32 Diabatic flow pattern map for vaporizing flow in uniformly heated micro-channel, R-134a, d = 0.5 mm, L = 70 mm, Tg = 30 °C, = 50 kW/m without subcooling at inlet. Flow patterns isolated bubble regime (IB), coalescing bubble regime (CB), annular (completely coalesced) regime (A), post-dryout regime (PD). Reprinted from Thome et al. (2006) with permission... Fig. 2.32 Diabatic flow pattern map for vaporizing flow in uniformly heated micro-channel, R-134a, d = 0.5 mm, L = 70 mm, Tg = 30 °C, = 50 kW/m without subcooling at inlet. Flow patterns isolated bubble regime (IB), coalescing bubble regime (CB), annular (completely coalesced) regime (A), post-dryout regime (PD). Reprinted from Thome et al. (2006) with permission...
In Proceedings of 21st SemiTherm Symposium, San Jose, 15-17 March 2005, pp 1-7 Copeland D, Behnia M, Nakayama W (1997) Manifold micro-channel heat sinks isothermal analysis. IEEE Trans Comp Packag Manuf Technol A 20 96-102 Dupont V, Thome JR, Jacobi AM (2004) Heat transfer model for evaporation in microchannels. [Pg.93]

ReveUin R, Dupont V, Ursenbacher T, Thome JR, Zun I (2006) Characterization of diabatic two-phase flows in microchannels flow parameter results for R-134a in a 0.5 mm channel. Int J Multiphase Flow 32 755-774... [Pg.97]

Sobhan CB, Garimella SV (2001) A comparative analysis of studies on heat transfer and fluid flow in micro-channels. Microscale Thermophys Eng 5 293-311 Steinke M, Kandlikar SG (2003) Flow boiling and pressure drop in parallel flow micro-channels. In Kandlikar SG (ed) Proceedings of 1st International Conference on Micro-channels and Mini-channels, Rochester, 24-25 April 2003, pp 567-579 Thome JR (2006) State-of-the-art overview of boiling and two-phase flows in microchannels. Heat Transfer Eng 27(9) 4-19... [Pg.97]

Thome JR, Dupont V, Jacobi AM (2004) Heat transfer model for evaporation in microchannels. [Pg.97]

Wojtan L, ReveUin R, Thome JR (2006) Investigation of saturated critical heat flux in a single, uniformly heated microchannel. Exp Thermal Fluid Sd 30 765-774... [Pg.98]

Quiben and Thome (2007a,b) presented an experimental and analytical investigation of two-phase pressure drops during evaporation in horizontal tubes. Experiments were performed under diabatic conditions in tubes of d = S and 13 mm in the range of vapor quality x = 0—1, mass velocity G = 70—700kg/m s, heat flux q = 6.0—57.5 kW/m. The test fluids were R-134a, R-22 and R-410A. The results... [Pg.299]

A theoretical model for the prediction of the critical heat flux of refrigerants flowing in heated, round micro-channels has been developed by Revellin and Thome (2008). The model is based on the two-phase conservation equations and includes the effect of the height of the interfacial waves of the annular film. Validation has been carried out by comparing the model with experimental results presented by Wojtan et al. (2006), Qu and Mudawar (2004), Bowers and Mudawar (1994), Lazareck and Black (1982). More than 96% of the data for water and R-113, R-134a, R-245fa were predicted within 20%. [Pg.309]

Agostini B, Revellin R, Thome J (2008) Elongated bubbles in micro-channels. Part I Experimental study and modeling of elongated bubble velocity. Int. J. Multiphase Flow 34 590-601 Bankoff SG, Haute T (1957) Ebullition from solid surfaces in the absence of pre-existing gaseous phase. Trans ASME 79 735-740... [Pg.319]

Collier G, Thome J (1994) Convective Boiling and Condensation, 3rd edn. Oxford University... [Pg.320]

Qu W, Mudawar I (2002) Prediction and measurement of incipient boiling heat flux in micro-channel heat sinks. Int J Heat Mass Transfer 45 3933-3945 Qu W, Mudawar I (2004) Measurement and correlation of critical heat flux in two-phase micro-channel heat sinks. Int J Heat Mass Transfer 47 2045-2059 Quiben JM, Thome JR (2007a) Flow pattern based two-phase pressure drop model for horizontal tubes. Part I. Diabatic and adiabatic experimental study. Int. J. Heat and Fluid Flow. 28(5) 1049-1059... [Pg.323]

ReveUin R, Thome J. (2008) A theoretical model for the prediction of the critical hat flux in heated micro-channel. Int. J. Heat and Mass Transfer 51 1216-1225 Roach GM, Abdel-Khahk SI, Ghiaasiaan SM, Dowling MF, Jeter SM (1999) Low-flow critical heat flux in heated microchannels. Nucl Sd Eng 131 411 25 Robinson AJ, Judd RL (2001) Bubble growth in a uniform and spatially distributed temperature field. Int J Heat Mass Transfer 44 2699-2710... [Pg.323]


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