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Plate and fin heat exchangers

Lowe, R. E. (1987) Chem. Eng., NY 94 (Aug. 17th) 131. Plate-and-fin heat exchangers for cryogenic service. [Pg.783]

Comparison on a Larger Scale Between a Shell and Tube Heat Exchanger, a Porous Metal Structure and a Plate and Fin Heat Exchanger Applied to Preferential CO Oxidation... [Pg.382]

The performance of a micro structured plate and fin heat exchanger (0.25 dm3 reactor volume), wash coated with 2.0 g of catalyst, was assessed in comparison with similar alternative technologies by Dudfield et al. [88], The first was a shell and tube heat exchanger filled with 4.66 g of catalyst microspheres (0.25 dm3 reactor... [Pg.382]

Takeda et al. [141] described the conditions applied for the diffusion bonding of nickel-based alloys (Hastelloy). A test piece of a plate and fin heat exchanger (dimensions 40 mm x 40 mm x 3 mm, channel dimensions 1000 pm x 1000 pm) was first cleaned with a 1% solution of nitric acid and hydrogen fluoride to remove the oxidation layer. A pressure as low as 6 mPa was necessary to run the process. For NiCrFe and other materials, other authors claim that an even lower pressure of 1 pPa is required. A welding temperature of 1 150 °C and a contact pressure of... [Pg.390]

A common type of heat exchanger used in industrial ventilation is the plate fin-and-tube heat exchanger (Fig. 9.7). Liquid or gas flows in the tubes, with a gas or a liquid circulating outside the tubes between the plates. [Pg.698]

Kim, N.-H, Yun, f.-H., and Webb, R. L. Heat transfer and friction correlations for wavy plate fin-and-tube heat exchangers. Journal of Heat Transfer 119 (1997) August, pp. 560-567,... [Pg.707]

Siegel, R. and Howell, J. R. Thermal Radiation Heat Transfer, 2nd edn (McGraw-Hill, New York, 1981) Sparrow, E. M. and Cess, R. D. Radiation Heat Transfer (Hemisphere Publishing, New York, 1978) Taylor, M. (ed.). Plate-fin Heat Exchangers Guide to their Specification and Use (HTFS, Harwell, 1987). Tohloukian, Y. S. Thermophvsical Properties of High Temperature Solid Materials (Macmillan, New York. 1967)... [Pg.562]

Compact (plate and fin) exchangers have 350 sqft/cuft, and about 4 times the heat transfer per cuft of shell-and-tube units. [Pg.12]

Fig. 9. Plate heat exchangers (a) plate—frame heat exchanger when hot fluid from the heat source enters the heat exchanger through connections in the stationary frame plate and is channeled over one side of each plate. Cold fluid enters through different frame plate connections and flows on the other side of each plate in a direction opposite to the hot fluid direction. Courtesy of Bell Gosset. (b) Limco model 6502 plate—fin heat exchanger having compact plate—fin aluminum brazed liquid-to-aii construction. The brazed plate—fin construction provides the most efficient heat-exchanger system in terms of size,... Fig. 9. Plate heat exchangers (a) plate—frame heat exchanger when hot fluid from the heat source enters the heat exchanger through connections in the stationary frame plate and is channeled over one side of each plate. Cold fluid enters through different frame plate connections and flows on the other side of each plate in a direction opposite to the hot fluid direction. Courtesy of Bell Gosset. (b) Limco model 6502 plate—fin heat exchanger having compact plate—fin aluminum brazed liquid-to-aii construction. The brazed plate—fin construction provides the most efficient heat-exchanger system in terms of size,...

See other pages where Plate and fin heat exchangers is mentioned: [Pg.336]    [Pg.550]    [Pg.552]    [Pg.566]    [Pg.383]    [Pg.88]    [Pg.550]    [Pg.552]    [Pg.353]    [Pg.57]    [Pg.279]    [Pg.279]    [Pg.363]    [Pg.286]    [Pg.336]    [Pg.550]    [Pg.552]    [Pg.566]    [Pg.383]    [Pg.88]    [Pg.550]    [Pg.552]    [Pg.353]    [Pg.57]    [Pg.279]    [Pg.279]    [Pg.363]    [Pg.286]    [Pg.335]    [Pg.696]    [Pg.206]    [Pg.502]    [Pg.1250]    [Pg.179]    [Pg.166]    [Pg.493]    [Pg.493]    [Pg.327]    [Pg.331]    [Pg.1131]    [Pg.678]    [Pg.698]    [Pg.553]    [Pg.347]    [Pg.528]    [Pg.226]    [Pg.493]   
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