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Tubular Exchanger Manufacturers Association

TEMA Numbering and Type Designation Recommended practice for the designation of TEMA-style shell-and-tube heat exchangers by numbers and letters has been established by the Tubular Exchanger Manufacturers Association (TEMA). This information from the sixth edition of the TEMA Standards is reproduced in the following paragraphs. [Pg.1063]

FIG. 11-35 TEMA-type designations for shell-and-tube beat exchangers. (Standards of Tubular Exchanger Manufacturers Association, 6tb ed., 1978.)... [Pg.1064]

FIG. 11 -36 (Continued) Heat-exchanger-component nomenclature, (c) Outside-packed floating-head exchanger. Type AEP. (d) U-tuhe heat exchanger. Type CFU. (e) Kettle-type floating-head rehoder. Type AKT. (Standard of Tubular Exchanger Manufacturers Association, 6th ed., 1978. )... [Pg.1067]

Standards of Tubular Exchanger Manufacturers Association (TEMA), 7th Edition. [Pg.24]

Standards of Tubular Exchanger Manufacturers Association (latest edition) Tubular Exchanger Manufacturers Association, Inc. (TEMA), 707 Westchester Ave., White Plains, New York 10604. [Pg.222]

Standards of the Tubular Exchangers Manufacturers Association (TEMA Standards, latest edition)... [Pg.31]

Eigures 10-lA-G and Table 10-1 from the Standards of Tubular Exchanger Manufacturers Association give the nomenclature of the basic types of units. Note the nomenclature type designation code letters immediately below each illustration. These codes are assembled from Table 10-1 and Eigures 10-lA-G. [Pg.3]

Used by permission Standards of the Tubular Exchanger Manufacturers Association, 7 Ed., Table D-7, <... [Pg.22]

Figure 10-39. Chart for determining U-dirty from values of U-clean and the sum of tube-side and shell-side fouling resistances. Note Factors refer to outside surface. Fouling resistance is sum of (r + rj, as hr-ft -°F/Btu. (Used by permission Standards of Tubular Exchanger Manufacturers Association 1959 and 1968. Tubular Exchanger Manufacturers Association, Inc. All rights reserved.)... Figure 10-39. Chart for determining U-dirty from values of U-clean and the sum of tube-side and shell-side fouling resistances. Note Factors refer to outside surface. Fouling resistance is sum of (r + rj, as hr-ft -°F/Btu. (Used by permission Standards of Tubular Exchanger Manufacturers Association 1959 and 1968. Tubular Exchanger Manufacturers Association, Inc. All rights reserved.)...
Figure 10-137. Heating and cooling in tube bundles—tube-side friction factor. (Used by permission Kern, D. Q. Process Heat Transfer, 1 Ed., p. 836, 1950. McGraw-Hill, Inc. All rights reserved. Using nomenclature of Standards of Tubular Exchanger Manufacturers Association.)... Figure 10-137. Heating and cooling in tube bundles—tube-side friction factor. (Used by permission Kern, D. Q. Process Heat Transfer, 1 Ed., p. 836, 1950. McGraw-Hill, Inc. All rights reserved. Using nomenclature of Standards of Tubular Exchanger Manufacturers Association.)...
See other pages where Tubular Exchanger Manufacturers Association is mentioned: [Pg.494]    [Pg.76]    [Pg.1027]    [Pg.1038]    [Pg.1054]    [Pg.180]    [Pg.184]    [Pg.232]    [Pg.24]    [Pg.24]    [Pg.26]    [Pg.48]    [Pg.487]    [Pg.1]   
See also in sourсe #XX -- [ Pg.30 , Pg.31 , Pg.32 , Pg.33 ]

See also in sourсe #XX -- [ Pg.479 ]

See also in sourсe #XX -- [ Pg.942 ]



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