Optimization of Energy Recovery Systems
Optimization of Energy Recovery Systems
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In our eReader you can find the full English version of the book. Read Optimization of Energy Recovery Systems Online - link to read the book on full screen. Our eReader also allows you to upload and read Pdf, Txt, ePub and fb2 books. In the Mini eReder on the page below you can quickly view all pages of the book - Read Book Optimization of Energy Recovery Systems
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80 697.60 697.80 1786.368 697.80 1628.20 1395.60 Inlet Vapor fraction 0.00 0.00 0.00 o.oo 0.00 1.00 1.00 Dutlet Vapor Fraction i — _ 0.00 0.00 0.00 0.00 0.00 o.co O.CO Approach Temperature = 2.78 K Beat exchanger coot equation = (a A ) where = arum-vl rata of return = 0.1 a = 350 b = 0.6 Equijwiont down tins = 280 hr./yr.
The cost of the network is the cost of utility streams +■ tho cost of the exchangers, In l/yr.
Ill heat archangel's are ausuaed to bo counter-current 80 between the inlet hot ...stream and the outlet cold stream (T > 533.33° + D, where D is a minimum allowed approach temperature of, say, 2.78K). By numerical computation one finds that the overall cost can be lowered if a is increased (see Figure 21). This increase in a„, £D 26 lowers the flows of cooling utilities IV and VII. Ultimately, when the flow of cooling utility IV is zero, an optimal structure is obtained with a cost of $16,945/yr. At this point a_, = 0.688.
26 Note, however, that when the flow of the cold stream through exchanger 2 is zero, and the heat exchanger 2 is totally neglected, a network with a cost of $6864/yr.
What to read after Optimization of Energy Recovery Systems?
You can find similar books in the "Read Also" column, or choose other free books by Shah, Jigar Vinubhai to read onlineMoreLess
To quickly assess the difficulty of the text, read a short excerpt:
80 697.60 697.80 1786.368 697.80 1628.20 1395.60 Inlet Vapor fraction 0.00 0.00 0.00 o.oo 0.00 1.00 1.00 Dutlet Vapor Fraction i — _ 0.00 0.00 0.00 0.00 0.00 o.co O.CO Approach Temperature = 2.78 K Beat exchanger coot equation = (a A ) where = arum-vl rata of return = 0.1 a = 350 b = 0.6 Equijwiont down tins = 280 hr./yr.
The cost of the network is the cost of utility streams +■ tho cost of the exchangers, In l/yr.
Ill heat archangel's are ausuaed to bo counter-current 80 between the inlet hot ...stream and the outlet cold stream (T > 533.33° + D, where D is a minimum allowed approach temperature of, say, 2.78K). By numerical computation one finds that the overall cost can be lowered if a is increased (see Figure 21). This increase in a„, £D 26 lowers the flows of cooling utilities IV and VII. Ultimately, when the flow of cooling utility IV is zero, an optimal structure is obtained with a cost of $16,945/yr. At this point a_, = 0.688.
26 Note, however, that when the flow of the cold stream through exchanger 2 is zero, and the heat exchanger 2 is totally neglected, a network with a cost of $6864/yr.
What to read after Optimization of Energy Recovery Systems?
You can find similar books in the "Read Also" column, or choose other free books by Shah, Jigar Vinubhai to read onlineMoreLess
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