Chemical process design and integration

=001  21666=003  OCoLC=005  20050318211336.0=008  050318s2005    enka          001 0 eng=010  ##$a2004014695=020  ##$a0471486809 (acid-free paper)=020  ##$a0471486817 (pbk. : acid-free paper)=041  0#$aeng=042  ##$apcc=050  00$aTP155.7 $b.S573 2005=082  00$a660 $222=092  ##$a660.2812 $bS6=100  1#$aSmith, R. $q(Robin)=245  10$aChemical process design and integration / $cRobin Smith.=260  ##$aChichester, West Sussex, England ; $aHoboken, NJ : $bWiley, $c2005=300  ##$axxiii, 687 p. : $bill. ; $c29 cm.=504  ##$aIncludes bibliographical references and index.=520  1#$a"The book is intended to be textbook for undergraduate and postgraduate students of chemical engineering, and to be a practical guide for practicing process designers and chemical engineers and applied chemists working in process development." "Chemical Process Design and Integration deals in detail with the design and integration of chemical processes, emphasizing the conceptual issues. Chemical process design requires the selection of a series of processing steps and their integration to form a complete manufacturing system. The text emphasizes both the design and selection of the steps as individual operations and their integration."--BOOK JACKET.=650  #0$aChemical processes.=970  11$lApp. A $tAnnualization of capital cost $p653=970  11$lApp. B $tGas compression $p655=970  11$lApp. C $tHeat transfer coefficients and pressure drop in shell-and-tube heat exchangers $p661=970  11$lApp. D $tThe maximum thermal effectiveness for 1-2 shell-and-tube heat exchangers $p667=970  11$lApp. E $tExpression for the minimum number of 1-2 shell-and-tube heat exchangers for a given unit $p669=970  11$lApp. F $tAlgorithm for the heat exchanger network area target $p671=970  11$lApp. G $tAlgorithm for the heat exchanger network number of shells target $p673=970  11$lApp. H $tAlgorithm for heat exchanger network capital cost targets $p677=970  11$lCh. 1 $tThe nature of chemical process design and integration $p1=970  11$lCh. 10 $tChoice of separator of homogeneous fluid mixtures II - other methods $p181=970  11$lCh. 11 $tDistillation sequencing $p211=970  11$lCh. 12 $tDistillation sequencing for azeotropic distillation $p235=970  11$lCh. 13 $tReaction, separation and recycle systems for continuous processes $p259=970  11$lCh. 14 $tReaction, separation and recycle systems for batch processes $p291=970  11$lCh. 15 $tHeat exchanger networks I - heat transfer equipment $p317=970  11$lCh. 16 $tHeat exchanger networks II - energy targets $p357=970  11$lCh. 17 $tHeat exchanger networks III - capital and total cost targets $p387=970  11$lCh. 18 $tHeat exchanger networks IV - network design $p399=970  11$lCh. 19 $tHeat exchanger networks V - stream data $p429=970  11$lCh. 2 $tProcess economics $p17=970  11$lCh. 20 $tHeat integration of reactors $p439=970  11$lCh. 21 $tHeat integration of distillation columns $p445=970  11$lCh. 22 $tHeat integration of evaporators and dryers $p459=970  11$lCh. 23 $tSteam systems and cogeneration $p465=970  11$lCh. 24 $tCooling and refrigeration systems $p513=970  11$lCh. 25 $tEnvironmental design for atmospheric emissions $p551=970  11$lCh. 26 $tWater system design $p581=970  11$lCh. 27 $tInherent safety $p625=970  11$lCh. 28 $tClean process technology $p635=970  11$lCh. 29 $tOverall strategy for chemical process design and integration $p649=970  11$lCh. 3 $tOptimization $p35=970  11$lCh. 4 $tThermodynamic properties and phase equilibrium $p57=970  11$lCh. 5 $tChoice of reactor I - reactor performance $p77=970  11$lCh. 6 $tChoice of reactor II - reactor conditions $p97=970  11$lCh. 7 $tChoice of reactor III - reactor configuration $p121=970  11$lCh. 8 $tChoice of separator for heterogeneous mixtures $p143=970  11$lCh. 9 $tChoice of separator for homogeneous fluid mixtures I - distillation $p157=LDR  04351pam a22007334a 45x0