Please use this identifier to cite or link to this item:
https://etd.cput.ac.za/handle/20.500.11838/1923
DC Field | Value | Language |
---|---|---|
dc.contributor.advisor | Coetzee, J.W. | en_US |
dc.contributor.author | Deist, Heino | en_US |
dc.date.accessioned | 2013-05-07T10:50:28Z | - |
dc.date.accessioned | 2016-02-26T06:16:16Z | - |
dc.date.available | 2013-05-07T10:50:28Z | - |
dc.date.available | 2016-02-26T06:16:16Z | - |
dc.date.issued | 2008 | - |
dc.identifier.uri | http://hdl.handle.net/20.500.11838/1923 | - |
dc.description | Thesis (Masters Degree(Chemical Engineering))--Cape Peninsula University of Technology, 2008 | en_US |
dc.description.abstract | ABSTRACT Carbon-in-pulp (CIP) technology is firmly entrenched in the mining sector due to numerous advances in the last few decades. CIP technology recovers complexed gold in solution from slurry streams by contacting the pulp with carbon and separating the two by screening. The carbon-in-leach (CIL) process, where the pulp contains free cyanide, is closely related to CIP. Both these processes, especially CIL, are complex and are governed by a number of interacting unit processes. The overall process efficiency is dependant on a large number of variables, making the process difficult to optimize. This study uses simple adsorption and leaching rate equations in order to predict dynamic CIL/CIP plant performance under varying operating conditions. This will assist plant metallurgists to achieve optimum efficiency, highlight plant sensitivity to certain variables and will ultimately result in proactive process control. Various assumptions were made in order to keep the modeling considerations as simple and realistic as possible. The process was assumed to have linear kinetic and equilibrium operation. The process was simulated using Simulink in Matlab. Variables are solved on a time step basis by Matlab’s built in optimization algorithms. Simulation results illustrated that the use of simple leaching and adsorption rate expressions are effective for investigating dynamic plant behavior under changing operating conditions. | en_US |
dc.language.iso | en | en_US |
dc.publisher | Cape Peninsula University of Technology | en_US |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-sa/3.0/za/ | - |
dc.subject | Carbon Activated | en_US |
dc.subject | MATLAB | en_US |
dc.subject | SIMULINK | en_US |
dc.title | A dynamic CIP/CIL process simulation using MATLAB SIMULINK | en_US |
dc.type | Thesis | en_US |
Appears in Collections: | Education - Masters Degrees |
Files in This Item:
File | Description | Size | Format | |
---|---|---|---|---|
thesis3.pdf | A Thesis submitted in fulfillment of the requirements for the Masters Degree in Technology (Chemical Engineering) at the Cape Peninsula University of Technology | 950.91 kB | Adobe PDF | View/Open |
Page view(s)
600
Last Week
5
5
Last month
13
13
checked on Nov 17, 2024
Download(s)
1,032
checked on Nov 17, 2024
Google ScholarTM
Check
This item is licensed under a Creative Commons License