Garantie de satisfaction à 100% Disponible immédiatement après paiement En ligne et en PDF Tu n'es attaché à rien
Recherché précédemment par vous
Exam (elaborations) TEST BANK FOR Analysis, Synthesis and Design of Chemical Processes 3rd Edition By Richard Turton, Richard C. Bailie, Wallace B. Whiting and Joseph A. Shaeiwitz (Solution Manual) 15,19 €
TEST BANK FOR Analysis, Synthesis and Design of Chemical Processes 3rd Edition By Richard Turton, Richard C. Bailie, Wallace B. Whiting and Joseph A. Shaeiwitz
Examen
Exam (elaborations) TEST BANK FOR Analysis, Synthesis and Design of Chemical Processes 3rd Edition By Richard Turton, Richard C. Bailie, Wallace B. Whiting and Joseph A. Shaeiwitz (Solution Manual)
TEST BANK FOR Analysis, Synthesis and Design of Chemical Processes 3rd Edition By Richard Turton, Richard C. Bailie, Wallace B. Whiting and Joseph A. Shaeiwitz
Établissement
Harvard University
Book
Analysis, Synthesis and Design of Chemical Processes
Exam (elaborations) TEST BANK FOR Analysis, Synthesis and Design of Chemical Processes 3rd Edition By Richard Turton, Richard C. Bailie, Wallace B. Whiting and Joseph A. Shaeiwitz (Solution Manual)
Chapter 1
1.1 Block Flow Diagram (BFD)
Process Flow Diagram (PFD)
Piping and Instrument Diagrams...
synthesis and design of chemical processes 3rd edition by richard turton
richard c bailie
wallace b whiting and joseph a shaeiwitz
test bank
Livre connecté
Titre de l’ouvrage:
Auteur(s):
Édition:
ISBN:
Édition:
École, étude et sujet
Harvard University
TEST BANK FOR Analysis, Synthesis and Design of Chemical Processes 3rd Edition By Richard Turton, Richard C. Bailie, Wallace B. Whiting and Joseph A. Shaeiwitz
Tous les documents sur ce sujet (1)
1
vérifier
Par: joeweldon8 • 1 année de cela
Par: Expert001 • 1 année de cela
Thank you for the review. It helps us gauge the quality of the document and make necessary edits for maximum student satisfaction. Any requests can be made via message.
Vendeur
S'abonner
Expert001
Avis reçus
Aperçu du contenu
,
, Chapter 1
1.1 Block Flow Diagram (BFD)
Process Flow Diagram (PFD)
Piping and Instrument Diagrams (P&ID)
(a) PFD
(b) BFD
(c) PFD or P&ID
(d) P&ID
(e) P&ID
1.2 P&ID
1.3 It is important for a process engineer to be able to review a 3-dimensional model prior to
the construction phase to check for clearance, accessibility, and layout of equipment,
piping, and instrumentation.
1.4 (1) Clearance for tube bundle removal on a heat exchanger.
(2) NPSH on a pump – affects the vertical separation of feed vessel and pump inlet.
(3) Accessibility of an instrument for an operator – must be able to read a PI or
change/move a valve.
(4) Separation between equipment for safety reasons – reactors and compressors.
(5) Crane access for removing equipment.
(6) Vertical positioning of equipment to allow for gravity flow of liquid.
(7) Hydrostatic head for thermosiphon reboiler – affects height of column skirt.
1.5 Plastic models are no longer made because they are too expensive and difficult to
change/revise. These models have been replaced with virtual/E-model using 3-D CAD.
Both types of model allow revision of critical equipment and instrument placement to
ensure access, operability, and safety.
1.6 Another reason to elevate the bottom of a tower is to provide enough hydrostatic head
driving force to operate a thermosiphon reboiler.
1-1
, 1.7 (a) PFD or P&ID
(b) PFD
(c) PFD
(d) P&ID
(e) BFD (or all PFDs)
1.8 A pipe rack provides a clear path for piping within and between processes. It keeps piping
off the ground to eliminate tripping hazards and elevates it above roads to allow vehicle
access.
1.9 A structure – mounted vertical plant layout is preferred when land is at a premium and the
process must have a small foot print. The disadvantage is that it is more costly because of
the additional structural steel.
1.10 (a) BFD – No change
PFD – Efficiency changed on fired heater, resize any heat exchanger used to extract
heat from the flue gas (economizer)
P&ID – Resize fuel and combustion air lines and instrumentation for utilities to fired
heater. Changes for design changed of economizer (if present)
(b) BFD – Change flow of waste stream in overall material balance
PFD – Change stream table
P&ID – Change pipe size and any instrumentation for this process line
(c) BFD – No change
PFD – Add a spare drive, e.g. D-301 → D-301 A/B
P&ID – Add parallel drive
(d) BFD – No change
PFD – No change
P&ID – Note changes of valves on diagram
1.11 (a) A new vessel number need not be used, but it would be good practice to add a letter to
donate a new vessel, e.g. V-203 → V-203N. This will enable an engineer to locate the
new process vessel sheet and vendor information.
(b) P&ID definitely
PFD change/add the identifying letter.
1-2
Les avantages d'acheter des résumés chez Stuvia:
Qualité garantie par les avis des clients
Les clients de Stuvia ont évalués plus de 700 000 résumés. C'est comme ça que vous savez que vous achetez les meilleurs documents.
L’achat facile et rapide
Vous pouvez payer rapidement avec iDeal, carte de crédit ou Stuvia-crédit pour les résumés. Il n'y a pas d'adhésion nécessaire.
Focus sur l’essentiel
Vos camarades écrivent eux-mêmes les notes d’étude, c’est pourquoi les documents sont toujours fiables et à jour. Cela garantit que vous arrivez rapidement au coeur du matériel.
Foire aux questions
Qu'est-ce que j'obtiens en achetant ce document ?
Vous obtenez un PDF, disponible immédiatement après votre achat. Le document acheté est accessible à tout moment, n'importe où et indéfiniment via votre profil.
Garantie de remboursement : comment ça marche ?
Notre garantie de satisfaction garantit que vous trouverez toujours un document d'étude qui vous convient. Vous remplissez un formulaire et notre équipe du service client s'occupe du reste.
Auprès de qui est-ce que j'achète ce résumé ?
Stuvia est une place de marché. Alors, vous n'achetez donc pas ce document chez nous, mais auprès du vendeur Expert001. Stuvia facilite les paiements au vendeur.
Est-ce que j'aurai un abonnement?
Non, vous n'achetez ce résumé que pour 15,19 €. Vous n'êtes lié à rien après votre achat.
