|
Figure |
Title |
Page |
|
2 - 1 |
Feed fractionator with preheat |
2 - 6 |
|
2 - 2 |
Depropanizer unit |
2 - 7 |
|
3 - 1 |
Centrifugal pump characteristics and system curve |
3 - 17 |
|
3 - 2 |
Expansion of pumping system |
3 - 18 |
|
4 - 1 |
Heat availability and requirements for crude tower |
4 - 72 |
|
4 - 2 |
Heat cascading distillation tower |
4 - 73 |
|
4 - 3 |
Split tower arrangement |
4 - 74 |
|
4 - 4 |
McCabe-Thiele diagram for system with intermediate condenser
and reboiler |
4 - 75 |
|
4 - 5 |
Recirculating reflux or pumparound tower |
4 - 76 |
|
4 - 6 |
Example of conventional distillation column, no side draw |
4 - 77 |
|
4 - 7 |
Vapor recompression example |
4 - 78 |
|
4 - 8 |
Example of heat pump system |
4 - 79 |
|
4 - 9 |
The refrigeration and Carnot cycles |
4 - 80 |
|
4 - 10 |
Column using vapor recompression |
4 - 81 |
|
4 - 11 |
Hot columns with vapor recompression |
4 - 82 |
|
4 - 12 |
Refrigerated columns with vapor recompression |
4 - 83 |
|
4 - 13 |
Propane propylene splitter |
4 - 84 |
|
4 - 14 |
Results of example of propane propylene splitter |
4 - 85 |
|
4 - 15 |
Splitter with bottoms vapor condenser |
4 - 86 |
|
4 - 16 |
Splitter of Figure 4 - 15 with data |
4 - 87 |
|
4 - 17 |
Vapor pressure of olefin hydrocarbons |
4 - 88 |
|
4 - 18 |
Vapor pressure of normal paraffin hydrocarbons |
4 - 89 |
|
4 - 20 |
Enthalpy temperature diagram for propylene |
4 - 90 |
|
4 - 21 |
Control of colum reflux to maximize profit and energy conservation |
4 - 91 |
|
5 - 1 |
Revenue and expense variation with production - ideal case |
5 - 17 |
|
5 - 2 |
Variation of profit with production |
5 - 17 |
|
5 - 3 |
Revenue and expense variation with production - real economic
case |
5 - 18 |
|
7 - 1 |
Work problem |
7 - 17 |
