Hi all, i'm new here and I would like to seek the help of all the members regarding the problem posted in the title of this thread. I'm a third year undergrad and am currently doing a design project regarding coal gasification and I need to simulate the gasification plant on Aspen. I could not complete the flowsheet as i'm having difficulties setting up the SRU. In general, the SRU that i'm using will convert all the SO2 gases to saleable gypsum. The followings are the specifications I made on Aspen:
Block : RStoic
Pressure : 4000 kPa
Temperature : 40 deg C
Feed : 1. CaSO3, 2. Air, 3. Syngas
Reactions : 1. S + O2 --> SO2
2. CACO3 + SO2 + 2 WATER + .5 O2 --> gypsum + CO2
The problem is, I could not run it with any other block properties except for NRTL. And NRTL is not a suitable property for this case. I've tried increasing the temperature of the block as it might not be suitable for the oxidation of sulfur and also changing the block to RGibbs but to no avail.
Hopefully my description of my problem is clear enough to aid in the understanding of the problem. If any member thinks that it is too vague, feel free to point out any information that is required inorder to assist me in solving this problem. All opinion are accepted. Thank You.
|
|
Sulfur Recovery Unit(sru) Simulation With Aspen
Started by jacko1986, Sep 25 2007 12:07 PM
No replies to this topic
Share this topic:
#1
Posted 25 September 2007 - 12:07 PM
Similar Topics
Sulfuric Acid Plant Aspen Hysys HelpStarted by Guest_kazuki222_* , 29 Apr 2026 |
|
|
||
Aspen Plus Conceptual Mof Synthesis Model: Elecnrtl, Ionic Leachate, PStarted by Guest_Momo_212_* , 16 Apr 2026 |
|
|
||
Energy Analysis In Aspen Plus 14.2Started by Guest_Sarishma_* , 23 Mar 2026 |
|
|
||
Aspen Plus Rcstr Convergence Issue – Mass Balance Error In Anaerobic DStarted by Guest_Marie26_* , 05 Apr 2026 |
|
|
||
Beginner Question: Inlet Separator Design In Aspen Hysys (Natural Gas,Started by Guest_NewEng2030_* , 12 Feb 2026 |
|
|

FB





