Process technology equipment and systems chapter 3 & 4

. 1 14. 80 .7972 43 . 77 49 . 74 3. 338 STD 40 S .37 5 12.000 14. 58 1 13. 10 .78 54 49.56 49 .00 3. 338 40 .40 6 11. 938 15.77 111. 93 .77 73 53. 52 48 .50 3. 338 12 12.75 XS. 19. 24 108. 43 .7528 65 .42 46 .92 3. 338 60 .562 11.626 21.52 106.16 . 737 2 73. 15 46 .00 3. 338 80 .688 11 .37 4 26. 03 101. 64 .7058 88. 63 44 . 04 3. 338 100 . 844 11.062

Ngày tải lên : 16/08/2013, 15:29

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Process technology equipment and systems chapter 1 & 2

... Compressor systems and operations • Heat exchanger and cooling tower systems and operations • Steam generation and furnace systems and operations • Reactor systems and operations • Key concepts and ... Process Technology Equipment and Systems This page intentionally left blank Process Technology Equipment and Systems Third Edition Charles E. Thomas .....

Ngày tải lên : 15/08/2013, 07:50

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Process technology equipment and systems chapter 5 & 6

. psia Stage Two 47 . 04 psia 3 3.2 5 150.528 psia Stage Three 150.528 psia 3 3.2 5 48 1.689 psia Stage Four 48 1.689 psia 3 3.2 5 1 541 .40 7 psia The basic components. 1, 541 .4 psia. The simple calculation used to calculate the pressure increase on each stage is: Stage One 14. 7 psia 3 3.2 5 47 . 04 psia Stage Two 47 . 04 psia

Ngày tải lên : 19/08/2013, 10:47

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Process technology equipment and systems chapter 7 & 8

. temperature differentials Chapter 7 ● Heat Exchangers 1 64 above 200°F ( 93. 33 C). During operation, one tube sheet is fixed and the other “floats” inside. place and prevent vibration and excessive tube movement. Nozzles and Accessory Parts Shell -and- tube inlet and outlet nozzles are sized for pressure drop and

Ngày tải lên : 20/08/2013, 10:39

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Process technology equipment and systems chapter 9, 10 & 11

. OP% Boiler -40 2 40 2B 40 2A 40 2 40 1 40 0 Pi 4 03 40 2 TE 40 4 TE 4 03 TE 40 0 TE 40 1 45 0ºF 30 5ºF 35 0ºF 600ºF 500ºF 40 2 40 2 I P 40 2A 40 2B 40 2C 35 0ºF TK -40 2 FT LT. FT FE I P I P BA 40 2 40 4 Pi Pi 60 psig 40 2 40 2 40 2 Pi 155 psig 40 1 PA LR LAL I P CASC Hi Low 40 4 PA Hi Low 40 2 40 2 LR LAL 40 1 40 1 35 % 35 % Ai AA Hi Low

Ngày tải lên : 21/08/2013, 10:47

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Process technology equipment and systems chapter 12&13

. W E S 6 4& apos; 0" 28' 0" 28' 0" 6' 0" 8' 0" 10' 0" 6-8-10 Method 2' x 6 4& apos; x 18" Load-Bearing. 8' 0" 6' 0" 18' 0" 8' 0" 16' 0" 20' 0" TK -30 0 TK -40 0 TK-200 C-200 TK-1 TK-2 TK -3 TK -4 Chapter

Ngày tải lên : 23/08/2013, 14:30

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Process technology equipment and systems chapter 14&15

. HYDROGEN 3 4 6. 941 9.0126 LITHIUM BERYLLIUM 11 12 22.99 24 .30 SODIUM MAGNESIUM 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 . 18 32 20 9 2 2 8 18 20 8 2 2 8 18 32 18 10 2 1s 2s 3d 3d 3d 3d 3d 3d 3d 3d 3d 3d 3s 4f 4d 4d 4d 4d 4d 4d 4d 4d 4d 4d 4s 5f 5d 5d 5d 5d 5d 5d 5d 5d 5d 5d

Ngày tải lên : 23/08/2013, 14:47

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Process technology equipment and systems chapter 16&17

. Solvent Figure 16 .4 Countercurrent Extraction Chapter 16 ● Extraction and Other Separation Systems 40 4 and extract to settle out. There are three main. from the extract; (3) separate the solvent and the solute. Step 3, recovery of the solvent and solute, is left to be done by some other process such as distil-

Ngày tải lên : 27/08/2013, 07:28

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The Complete Guide to Buying and Selling Apartment Buildings Chapter 3-4

... 1 ,35 0,5 24 14 166,507 160,1 03 1 53, 945 148 ,0 24 142 ,33 1 136 ,857 131 ,5 93 126, 532 121,665 116,986 1 ,40 4, 545 15 1 73, 168 166,507 160,1 03 1 53, 945 148 ,0 24 142 ,33 1 136 ,857 131 ,5 93 126, 532 121,665 1 ,46 0,727 16 ... 1 04, 000 1, 248 , 635 12 1 53, 945 148 ,0 24 142 ,33 1 136 ,857 131 ,5 93 126, 532 121,665 116,986 112 ,48 6 108,160 1,298,581 13 160,1 03 1 53,...

Ngày tải lên : 07/11/2013, 14:15

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