- Aspen Plus V10 Tutorial
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- Aspen Plus V10 Book
- Aspen Plus V10 Hardware Requirements
- Aspen Plus Manual
Learn Aspen Plus in 24 Hours Simulation Files
Simulation solution files from the textbook Learn Aspen Plus in 24 Hours by Thomas A. Adams II.Disclaimer: The following simulation files come with no warranty, express or implied, or guarantee of their accuracy or correctness. These files are instructional tools for educational purposes only, and are intended for use in conjunction with the corresponding textbook.
License: These files are free to use for non-commercial purposes only. Any modifications, copies, or derivatives of these files must include a proper citation of the corresponding textbook and/or web site as appropriate.
Download All Files (.zip)
| Tutorial | Files | Software |
|---|---|---|
| Tutorial 01 | Part 1 | Part 2 | Aspen Plus v9.0 |
| Tutorial 02 | Part 1 | Aspen Plus v9.0 |
| Tutorial 03 | Part 1 | Part 2 | Aspen Plus v9.0 |
| Tutorial 04 | Part 1 | Part 2 | Aspen Plus v9.0 |
| Tutorial 05 | Part 1 | Part 2 | Aspen Plus v9.0 |
| Tutorial 06 | Part 1 | Part 2 | Part 3 Part 4 | Part 5 | Part 6 | Aspen Plus v9.0 |
| Tutorial 07 | Part 1 | Part 2 | Part 3 | Aspen Plus v9.0 |
| Tutorial 08 | Part 1 | Aspen Plus v9.0 |
| Tutorial 09 | Part 1 | Part 2 | Aspen Plus v9.0 |
| Tutorial 10 | Part 1 | Part 2 | Aspen Plus v9.0 and Aspen Capital Cost Estimator |
| Tutorial 11 | Part 1 | Part 2 (.hch) Part 2 (.bkp) | Aspen Plus v9.0 and Aspen Energy Analyzer |
| Tutorial 12 | Part 1 | Part 2 | Part 3 | Aspen Plus v9.0 |
CO2 Capture Simulation Examples
Oct 14, 2019 Description. Aspen Plus V10 User Models Manual. This manual is intended for the Aspen Plus user who wants to create custom Fortran subroutines and CAPE-OPEN modules to extend the modeling capabilities of Aspen Plus. Prior programming experience with Fortran, C or Visual Basic is recommended. Similar as with Aspen Plus V10 update, you can now get new databanks! HYSYS V10 includes a new IAPWS-IF97 property package, which uses the IAPWS Industrial Formulation 1997 correlation for thermodynamic properties of water and steam; Properties Enhancements. Bubble Point Pressure is now available as a correlation in both: the Stream and in the. AspenTech ® modules such as Aspen Plus ® or Aspen HYSYS ® were proved to be efficient for process flowsheeting and ensuring plant-wide mass and energy balances 31,35,509,537,538.
From the textbook chapter Process and Simulations for Solvent-based CO2 Capture and Syngas Cleanup by Thomas A. Adams II, Yaser Khojestah Salkuyeh, and Jake Nease, appearing in the book Reactor and Process Design in Sustainable Energy Technology, ed: Fan Shi.Disclaimer: The following simulation files come with no warranty, express or implied, or guarantee of their accuracy or correctness. These files are instructional tools for educational purposes only, and are intended for use in conjunction with the corresponding textbook chapter.
License: These files are free to use for non-commercial purposes only. Any modifications, copies, or derivatives of these files must include a proper citation of the corresponding textbook chapter by Adams et al. and/or web site as appropriate.
Download All Files (.zip)
| File | Software | Solvent | Removes | Application |
|---|---|---|---|---|
| MDEA-H2S.pmx | ProMax 3.1 | MDEA | H2S | Removal from coal-derived 1:1 syngas for coal-to-liquid applications |
| MDEA-CO2.bkp | Aspen Plus 8.2 | MDEA | CO2 | Removal from natural gas-derived 2:1 syngas for gas-to-liquid applications |
| MDEA-CO2.pmx | ProMax 3.1 | MDEA | CO2 | Removal from natural gas-derived 2:1 syngas for gas-to-liquid applications |
| MDEA-H2S-CO2.pmx | ProMax 3.1 | MDEA | H2S and CO2 | oval from coal-derived 2:1 syngas for coal-to-liquid applications |
| MDPZ-CO2-27.pmx | ProMax 3.1 | MDEA/ Piperazine | CO2 | Removal from natural gas-derived 2:1 syngas for gas-to-liquid applications, absorber @ 27 bar |
| MDPZ-CO2-52.pmx | ProMax 3.1 | MDEA/ Piperazine | CO2 | Removal from natural gas-derived 2:1 syngas for gas-to-liquid applications, absorber @ 52 bar |
| MEA-NG-Amines.bkp | Aspen Plus 8.2 | MEA | CO2 | Removal from natural gas power plant combustion exhaust using the Amines physical property model |
| MEA-NG-ElecNRTL.bkp | Apen Plus 8.2 | MEA | CO2 | Removal from natural gas power plant combustion exhaust using the ElecNRTL physical property model |
| MEA-Coal-ElecNRTL.bkp | Aspen Plus 8.2 | MEA | CO2 | Removal from coal power plant combustion exhaust using the ElecNRTL physical property model |
| MEA-IGCC-Amines.bkp | Aspen Plus 8.2 | MEA | CO2 | Removal from IGCC power plant pre-combustion syngas using the Amines physical property model |
| MEA-IGCC-ElecNRTL.bkp | Aspen Plus 8.2 | MEA | CO2 | Removal from IGCC power plant pre-combustion syngas using the ElecNRTL physical property model |
| DGA-NG-Amines.bkp | Aspen Plus 8.2 | DGA | CO2 | Removal from natural gas power plant combustion exhaust using the Amines physical property model |
| DGA-NG-ElecNRTL.bkp | Aspen Plus 8.2 | DGA | CO2 | Removal from natural gas power plant combustion exhaust using the ElecNRTL physical property model |
| DGA-Coal-ElecNRTL.bkp | Aspen Plus 8.2 | DGA | CO2 | Removal from coal power plant combustion exhaust using the ElecNRTL physical property model |
| DGA-IGCC-Amines.bkp | Aspen Plus 8.2 | DGA | CO2 | Removal from IGCC power plant pre-combustion syngas using the Amines physical property model |
| DGA-IGCC-ElecNRTL.bkp | Aspen Plus 8.2 | DGA | CO2 | Removal from IGCC power plant pre-combustion syngas using the ElecNRTL physical property model |
| Selexol-IGCC-Air-DBRAmines.hsc | Aspen HYSYS 8.2 | Selexol | CO2 | Removal from IGCC power plant pre-combustion syngas generated from air gasification using the DRMAmines physical property model |
| Selexol-IGCC-OXY-DBRAmines.hsc | Aspen HYSYS 8.2 | Selexol | CO2 | Removal from IGCC power plant pre-combustion syngas generated from high-purity oxygen gasification using the DRMAmines physical property model |
| Rectisol-IGCC-Air.prz | Pro/II v9.1 | Rectisol | CO2 | Removal from IGCC power plant pre-combustion syngas generated from air gasification using the SRK-PR physica property model |
| Rectisol-IGCC-Air-SourPRLK.hsc | Aspen HYSYS 8.2 | Rectisol | CO2 | Removal from IGCC power plant pre-combustion syngas generated from air gasification using the SourPRLK physical property model |
Biomass-Gas-and-Nuclear-To-Liquids Simulation Files
These are Aspen Plus files associated with the article by James Scott and Thomas A. Adams II entitled 'Biomass-Gas-and-Nuclear-To-Liquids (BGNTL) Processes Part I: Model Development and Simulation' published in the Canadian Journal of Chemical Engineering (in press), 2018.Aspen Plus V10 Tutorial
License: The simulation models are licensed for non commercial use. All references to the work must include a citation of the above article. They are provided as-is with no guarantee or warantee for accuracy or completeness.Aspen Plus V10 Download
Aspen Plus V10 Book
Models Included: Two simulations are included. See the above work for a detailed and peer-reviewed description of the model. The processes contain various sections including:
Aspen Plus V10 Hardware Requirements
- Biomass Gasification
- Natural Gas Reforming (with and without integration with the gasifier)
- Solid Oxide Fuel Cell systems
- Heat Recovery and Steam Generation
- Cooling Towers
- Carbon Dioxide Capture and Compression (from SOFC anode exhaust)
- Water Gas Shift
- Autothermal Reforming
- Fischer-Tropsch Synthesis
- Methanol Synthesis
- Dimethyl Ether Synthesis
Aspen Plus Manual
| File Name | File Type and Size | Description |
|---|---|---|
| Case1.1_v10_c07.bkp | Aspen Plus v10 Backup File (10.6 Mb) | (Version 7) Case 1.1 from the above paper, in which the heat from the gasifier is used to power a steam methane reformer. |
| Case1.1_v10_c07.apw | Aspen Plus v10 Workbook File, Converged (31.4 Mb) | (Version 7) Case 1.1 from the above paper, in which the heat from the gasifier is used to power a steam methane reformer. |
| Case1.2_v10.bkp | Aspen Plus v10 Backup File (4.3 Mb) | (Version 1) Case 1.2 from the above paper, in which steam methane reforming is done in a traditional manner. |
| Case1.2_v10.apw | Aspen Plus v10 Workbook File, Converged (29.7 Mb) | (Version 1) Case 1.2 from the above paper, in which steam methane reforming is done in a traditional manner. |