Process Intensification and Integration for Sustainable Design. Группа авторов
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Название: Process Intensification and Integration for Sustainable Design

Автор: Группа авторов

Издательство: John Wiley & Sons Limited

Жанр: Отраслевые издания

Серия:

isbn: 9783527818723

isbn:

СКАЧАТЬ 2.2 Selected cases.Table 2.3 High acid (HA) gas feed composition.Table 2.4 Parameters used for the techno‐economic analysis.Table 2.5 Price of different commodities.Table 2.6 Effective prices for products ($/gal).Table 2.7 Return on investment for the base case.Table 2.8 Incremental return on investment for high acid case.Table 2.9 Results from modified process route index calculations.Table 2.10 Maximum, minimum, average, and standard deviation for price data.Table 2.11 Description of Cases 1–3 for sensitivity analysis.Table 2.12 Description of cases for sensitivity analysis.Table 2.A.1 Dehydration column parameters for the base case (Feed #3).Table 2.A.2 Makeup composition for the base case (Feed #3).Table 2.A.3 Glycol circulation rate for the base case (Feed #3).Table 2.B.1 Demethanizer column parameters.Table 2.B.2Low temperature separator (LTS) inlet temperature.Table 2.B.3 Outlet pressure for the pressure changing equipment.Table 2.C.1 Fractionation train column parameters for the base case (Feed #3)...Table 2.D.1 Acid gas removal column parameters.Table 2.D.2 Makeup composition.Table 2.D.3 Key heat exchange equipment outlet temperatures.

      3 Chapter 4Table 4.1 Values of constants determined from curve fitting with revised Dool...Table 4.2 Values of physical parameters for solubility–thickness empirical eq...

      4 Chapter 5Table 5.1 Comparative analysis of bubble size and total contact area produced...

      5 Chapter 6Table 6.1 Simulation results of conventional column.Table 6.2 Reboiler and condenser duty of HIDiC basic design.Table 6.3 Temperature profile for rectifying and stripping columns.Table 6.4 Calculation ofQ i and A i for top‐integrated column configuration.Table 6.5 Calculation ofQ i and A i for bottom‐integrated column configuration....Table 6.6 Geometrical analysis of heat panels.Table 6.7 Energy savings and economic evaluation of different column configur...

      6 Chapter 7Table 7.1 Summary of cases 1–7.Table 7.2 Stream data of the process.

      7 Chapter 8Table 8.1 Variation of energy consumptions for exothermic reaction.Table 8.2 Variation of energy consumptions for endothermic reaction.

      8 Chapter 9Table 9.1 Streams data for Case Study 1.Table 9.2 Heat exchangers data for Case Study 1.Table 9.3 Stream split ratio in the base and optimized case (the split ratio ...Table 9.5 Economic efficiency in different cases (Case Study 1).Table 9.4 Cost related data (Case Study 1).Table 9.6 Design and operation parameters for Case Study 2.Table 9.7 Cost and physical related data (Case Study 2).Table 9.8 Optimized cleaning schedules for Scenario 1.Table 9.9 Optimized cleaning schedules for Scenario 3.Table 9.10 Fouling rate of different scenarios at hot end of the network.Table 9.11 Summary of optimized results for selected scenarios.Table 9.12 Cleaning schedule with back‐up heat exchangers.

      9 Chapter 10Table 10.1 The stream data of Example 1.Table 10.2 The IPHI implementation result of Example 1.Table 10.3 The stream data of Example 2.Table 10.4 Comparisons between the designs by utilizing different methods fro...

      10 Chapter 11Table 11.1 The MEN stream data (concentrations given in mass fractions).Table 11.2 The REN stream data (compositions given in mass fractions).Table 11.3 The capital costs of different networks.Table 11.4 Operating costs of lean, regenerating, and utility streams.Table 11.5 The environmental impact of lean and regenerating streams for H2S ...Table 11.6 The HEN stream data for H2S removal process.Table 11.7 NMP lean stream data.Table 11.8 The inert gas stripping stream data.

      11 Chapter 12Table 12.1 Process data for water network.Table 12.2 Economic data for case study.Table 12.3 Summary of results for all scenarios based on case study.Table 12.4 Summary of regeneration cost analysis.Table 12.5 Summary of model characteristics for all scenarios.

      12 Chapter 13Table 13.1 Eco‐points for energy and resources for the proposed system [15].Table 13.2 Eco‐points for the used material in the technologies production.Table 13.3 Parameters to calculate the occupation health.Table 13.4 Utopia and Nadir points for the random scenarios.Table 13.5 Individual and total dissatisfaction for the proposed scenarios.Table 13.6 Individual objective solutions for the scenario with lowest dissat...

      13 Chapter 14Table 14.1 Key performance metrics comparison for the DME‐to‐HOG catalyst.Table 14.2 Primary input data for economic indicator calculation.Table 14.3 Material and energy flows for the syngas conversion process (gate‐...Table 14.4 GREENSCOPE environmental indicators.Table 14.5 GREENSCOPE energy indicators.Table 14.6 GREENSCOPE material efficiency indicators.Table 14.7 GREENSCOPE economic indicators.

      List of Illustrations

      1 Chapter 1Figure 1.1 Safety, sustainability, and economic indicator for different pres...Figure 1.2 Simultaneous phenomena building blocks in a conventional distilla...Figure 1.3 Basic flowsheet for ethylene production from shale/natural gas.

      2 Chapter 2Figure 2.1 Shale gas treatment process.Figure 2.2 Overview of the methodology.Figure 2.3 Glycol dehydration process.Figure 2.4 Turboexpander process (stream 19 shows the recovery of recompress...Figure 2.5 Fractionation train.Figure 2.6 Acid gas removal unit.Figure 2.7 Comparison of gas composition with revenue.Figure 2.8 Economic metrics for the additional cases.Figure 2.9 Phase envelope for Feed #1 before the demethanizer column (genera...Figure 2.10 IROI based on feed probability.Figure 2.11 Revenue for the high acid gas case and base case (MM$/yr).Figure 2.12 Measured contributions to variance on ROI for the inputs.Figure 2.13 Results for Cases 1–3 for the СКАЧАТЬ