Fundamentals of Heat Exchanger DesignWarmeaustauschersysteme mit zwei Fluiden: Dieses Handbuch beantwortet Ihnen jede Frage zum thermischen und hydraulischen Design! Ausfuhrlich behandelt werden sowohl Rekuperatoren als auch Regeneratoren; ebenfalls breiten Raum nimmt die Erlauterung unterschiedlicher Bauweisen ein. Unentbehrlich fur Ingenieure! |
Contents
I | 1 |
IV | 3 |
V | 8 |
VII | 12 |
VIII | 56 |
IX | 73 |
X | 78 |
XII | 93 |
L | 426 |
LI | 441 |
LII | 450 |
LIII | 473 |
LIV | 511 |
LV | 529 |
LVI | 532 |
LVII | 537 |
XIII | 97 |
XV | 98 |
XVI | 100 |
XVII | 114 |
XVIII | 121 |
XIX | 139 |
XX | 142 |
XXI | 186 |
XXII | 190 |
XXIII | 207 |
XXIV | 210 |
XXV | 212 |
XXVI | 216 |
XXVII | 232 |
XXIX | 244 |
XXX | 258 |
XXXI | 291 |
XXXII | 308 |
XXXIV | 316 |
XXXV | 337 |
XXXVI | 348 |
XXXVII | 355 |
XXXVIII | 360 |
XXXIX | 366 |
XL | 378 |
XLII | 381 |
XLIII | 392 |
XLIV | 393 |
XLV | 397 |
XLVI | 399 |
XLVII | 412 |
XLVIII | 418 |
XLIX | 425 |
LVIII | 563 |
LX | 569 |
LXI | 574 |
LXII | 585 |
LXIII | 587 |
LXIV | 597 |
LXV | 601 |
LXVIII | 605 |
LXIX | 631 |
LXX | 632 |
LXXI | 646 |
LXXII | 664 |
LXXIII | 673 |
LXXIV | 674 |
LXXV | 680 |
LXXVI | 699 |
LXXVII | 735 |
LXXX | 738 |
LXXXI | 755 |
LXXXII | 763 |
LXXXIII | 771 |
LXXXIV | 775 |
LXXXV | 796 |
LXXXVI | 809 |
LXXXIX | 837 |
XC | 844 |
XCI | 845 |
XCII | 863 |
XCIV | 866 |
XCV | 881 |
XCVI | 890 |
XCVII | 893 |
Other editions - View all
Common terms and phrases
analysis baffle boundary conditions calculated Cmin cold fluid compute constant convection core correlation corrosion counterflow exchanger crossflow density determine dimensionless dimensionless groups duct energy entropy equation exchanger effectiveness F factor Fanning friction factor fin efficiency flow arrangement flow length flow maldistribution flow passages fluid flow fluid side fluid streams fouling resistance friction factor geometry header heat capacity rate heat conduction heat exchanger heat exchanger design heat transfer coefficient heat transfer rate heat transfer surface Hence hot fluid hydraulic diameter increase inlet temperature kg/m³ kg/s laminar flow leakage liquid mass flow rate matrix multipass NTU₁ Nusselt number outlet temperatures P₁ parallelflow pressure drop problem R₁ ratio Reynolds number rotary regenerator Shah shell fluid shell-and-tube exchanger shell-side shown in Fig single-pass specific TEMA temperature difference temperature distributions thermal conductivity thermal resistance thermodynamic transfer surface area turbulent flow velocity viscosity W/m²