Exchanger Type

A floating head-type shell-and-tube heat exchanger is recommended for this application because of the need to provide capacity for thermal expansion of the tube bundle. The floating head also enables easy withdrawal of the tube bundle for cleaning purposes. This factor may be very advantageous, not because the streams are subjected to fouling, but because of the possibility that platinum carryover from the reactor will be deposited on the walls of the tubes. Platinum recovery is improved by providing easy access. 

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Hall, S. G., Ahmad, S., and Smith, R., Capital Cost Target for Heat Exchanger Networks Comprising Mixed Materials of Construction, Pressure Ratings and Exchanger Types, Computers Chem. Eng., 14 319, 1990. 

Frequently, the difference ia exchanger type does not influence the desired topology to any significant extent. For iadustrial problems, however, it is necessary to consider iadividual heat-exchanger shells rather than just the match that is called the heat exchanger. If a high level of heat recovery is desired, the effect of the F factor can be important. This problem has been solved but is beyond the scope of this article. 

Medium Pressure Synthesis. Pressures of 500—2000 kPa (5—20 atm) were typical for the medium pressure Fischer-Tropsch process. Cobalt catalysts similar to those used for the normal pressure synthesis were typically used at temperatures ranging from 170 to 200°C ia tubular "heat exchanger" type reactors. 

FIG. 11-36 Heat-exchanger-component nomenclature, (a) Internal-floating-head exchanger (with floating-head hacking device). Type AES. (h) Fixed-tiihe-sheet exchanger. Type BEM. (Standard of Tiihiilar Exchanger Manufacturers Association, 6th ed., 1978. )... 

Heat transfer equipment has a great variation in heat transfer area per unit of material volume. Table 4.4 compares the surface compactness of a variety of heat exchanger types. Falling film evaporators and wiped film heat exchangers also reduce the inventory of material on the tube side. Process inventory can be minimized by using heat exchangers with the minimum volume of hazardous process fluid for the heat transfer area required. 

Heat exchanger type and number of tubes Choose TEMA R because of large size. 

Exchange type matrix elements in semi-empirical theory (x,y = s,p,d)... 

Or Other Cation-Exchange Type, e.g., Ion Exchange Resin, or Active Carbon ... 

Many boilers are fitted with a heat exchanger-type water sampling coil that permits the collection of a representative and cooled BW sample. The design generally provides for a coil of copper or stainless steel (SS) fitted inside a small SS shell. The unit is fitted with gate valves to control the flow of cooling water and BW. 

Table 9.23. Performance of plate-type exchanger type HF ...

Cluster Exchange Type Fluxiona] Process (Exchange Banicr) Ref. 

Heat-exchanger type PROX system with non-pellet catalyst... 

A small-scale PROX system was manufactured in a type of heat exchanger using non-pellet catalyst. Pt-Ru catalyst screened was impregnated on the support sheet. The support sheet was made by coating y-AlaOs on porous SUS-mesh plate (thickness 1.0 mm). The surface area of the catalyst sheet was 96 mVg. The catalyst sheet was applied to a heat exchanger type reactor of PROX as shown in Fig. 2. The PROX reactor was manufactured as a unit module and tested. Fig. 3 is the test-set of the PROX. Air was applied as the coolant. 

Group Na /H exchanger type Reagent Effect" Protectant" Ref. 

Roothaan open-shell treatments involving a closed-shell subsystem and outer unpaired electrons interacting through two-index integrals of Coulomb and exchange type only [43],... 

Neutrons of the molluse, Aplusia californica Ca " liquid membrane micropipet (ion-exchanger type with PVC added) Ca + 540nA/ 139)... 

Lammerhofer, M., Maier, N. M., and Lindner, W., Chiral anion exchange-type stationary phases based on cinchonan alkaloids, Am. Lab., 71, April 1998. 

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