Heat exchanger chemical

From the APV heat-transfer handbook—Design Plate Heat Exchangers and J. Marriott s article, Where and How To Use Plate Heat Exchangers, Chemical Engineering, April 5, 1971, there are the following equations for plate heat transfer. 

Fanaritis, J. P. and Bevevino, J. W., How to Select the Optimum Shell and Tube Heat Exchanger, Chemical Engineering, July 5, 1976, pp. 62-71. 

Purohit, G. R, Estimating Costs of Shell and Tube Heat Exchangers, Chemical Engineering, Aug. 22,... 

A detailed characterization of micro mixing and reaction performance (combined mixing and heat transfer) for various small-scale compact heat exchanger chemical reactors has been reported [27]. The superior performance, i.e. the process intensification, of these devices is evidenced and the devices themselves are benchmarked to each other. 

Lord, R.C., Minton, P.E., Slusser, R.G. Guide to Trouble-Free Heat Exchangers, Chemical Engineering, June 1, 1970, p. 153. 

Lohrisch, F.N. What Are Optimum Conditions for Air-Cooled Heat Exchangers, Chemical Engineering, June 1966, p. 131. 

Jones, W. E and Wilson, J. A. An Introduction to Process Flexibility. 1. Heat Exchange, Chemical Engineering Education, 31, 172-177, Summer (1997). 

G.P. Purohit, Costs of shell-and-tube heat exchangers. Chemical Engineering, 22 (August 1983, 4 March 1985, 18 March 1985). 

Fluidized beds have been used extensively for physical operations (e.g., adsorption and heat exchanger), chemical synthesis (e.g., acrylonitrile synthesis and maleic anhydride synthesis), metallurgical and mineral processes (e.g., roasting of sulfide ores, resid hydro-treating, and reduction of iron oxide), and other applications, such as coal combustion and microorganism cultivation. 

Such systems present the drawback of incurring high material and energy losses, associated with the irreversibilities encountered, particularly in heat exchanges, chemical reactions and separations. 

FIGURE 15.7. Schematic diagram of the action of scraped surface heat exchangers Chemical cleaning... 

The values of all exeigetic and thermoeconomic variables depend on the eomponent lype (e.g., tuibine, heat exchanger, chemical reactor). For instance, the value of the exergoeconomie factor is typically between 25 and 65% for compressors and turbines. 

Fijas DF (1989) Getting top performance from heat exchangers. Chemical Engineering, pp. 141-145, December. 

W. Bier, W. Keller, G. Linder, D. Seidel, K. Schubert and H. Martin, Gas to gas heat-transfer in micro heat-exchangers. Chemical Engineering Processing, 1993, 32 (1), 33-43. 

Minton, P, E. Lord, R. C Slusser, R. P., "Design of Heat Exchangers", Chemical Engi-... 

Huckaba, C. E., Master, N., Santoleri, J J., "Performance of Novel Sub-X Heat Exchanger", Chemical Engineering Progress, July, 1967,pp. 74-BO. 

Sanders, C, W., "Better Control of Heat Exchangers", Chemical Engineering. Sept. 21,... 

Development of the Heat-Exchanger / Chemical-Reactor Is a Major Challenge... 

Example A Thermal-Radiation Heat Exchanger/Chemical Reactor for Heat Transfer, Independent Sizing of the Chemical Reactor, and Isolation)... 

Micro-heat exchangers Chemical etching, spark erosion, UV LIGA techniques Lab-on-a-chip , microelectronics thermal control 4... 

Welded plate heat exchangers Chemicals and petrochemicals Food and drink Oil and gas processing... 

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