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Chemical Process Technology

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Chemical & Process Technology

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Friday, May 25, 2007


Carbon Dioxide (CO2) is known as one of industrial waste gas causing global warming...there are number of measures are implemented to reduce global warming. CO2 reduction measures are CO2 capturing, reinjection into aquifer, injection into reservior for well maintenance, gas injection for enhanced oil recovery (EOR), etc.



Above efforts will reduce CO2 release into atmosphere. However, recycling CO2 will increase quantity of CO2 in oil and result serious corrosion problem. Hence it needs to be removed from the flashed gas (from unstabilised oil). CO2 removal technology using amine absorption has been used for many years. Recently i found a website (OGT) where the founders, Ralph Weiland and Jack Dingman are those experts in this technology.



Optimized Gas Treating, Inc. (OGT) was established in 1992 by Ralph Weiland and Jack Dingman for the single purpose of providing a commercial version of a Windows-based software package for simulating acid gas removal with aqueous alkanolamines that uses a fundamental mass and heat transfer rate approach to column modeling. ProTreat™ is the culmination of more than 30 years of research in gas treating supported by government and industry in both academic and commercial environments. ProTreat is our sole product. Consequently, it receives our undivided attention in maintaining and enhancing its capabilities so that it remains the premier software package for gas treating with amines. OGT’s principals are recognized world experts in most aspects of gas treating — they offer a total of nearly 60 years of relevant experience.



Some FREE articles offered by OGT :

Column related

- Column Design Using Mass Transfer Rate Simulation (paper presented in GPSA)

- Column Design Using Mass Transfer Rate Simulation (PetroChemical & gas Processing)

- Packed Column Simulation Tracks Plant Performance

- Effect of Heat-Stable Salts on Amine Absorber and Regenerator Performance



WebWorm


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posted by Webworm, 6:15 AM | link | 0 Comments |

Tuesday, May 22, 2007





By change found this website...Wow ! Pretty good site for refinery engineer. Let see what is GTC...


GTC is a proprietary licensed technology to processing industries from naphtha processing to terephthalic acid purification. Success built around production of chemicals and the refining of petroleum worldwide. Notion applied to production of dimethyl terephthalate (DMT), aromatics recovery, replacing LLE with ED, technologies for paraxylene production and fuel gas desulphurization.



GTC offers some FREE articles for download...


- Extractive Distillation Applied


- Succeed at Plant Debottlenecking


- Latest Desulphurization Technology Information



WebWorm


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posted by Webworm, 5:23 AM | link | 0 Comments |

Tuesday, May 1, 2007





ChemSep is a software system for simulation of distillation, absorption, and extraction operations.


Built in features
- integrates flash calculations
- classic equilibrium stage column model
- non-equilibrium or rate-based column model
- export results to spreadsheet, text, and html.
- stand-alone mode as well as in flowsheet via CAPE-OPEN
- liquid-liquid extraction and three phase distillation column models



Special features ChemSep 6 for Windows

FREE download
ChemSep-LITE is available for FREE download and is now CAPE-OPEN compliant (article in NPT). It can be used as a stand-alone column simulator or as a unit operation model inside any CO compliant flowsheet simulation program such as ASPEN Plus or COCO. ChemSep-LITE includes the equilibrium column model and is limited to 5 components and 50 stages.
ChemSep book is available FREE for download

"Performance of a commercial scale 14% hole area sieve tray"
, Ind. Eng. Chem. Proc. Des. Dev., Vol. 21 (1982) pp. 712-717. FRI total reflux experiments published by T. Yanagi, M. Sakata
[Excel]
Note :Installed ChemSep LITE in order to be able to recalculate the spreadsheet.
PhD. thesis of Harry Kooijman,
Dynamic Nonequilibrium Column Simulation,
PhD. thesis of Arnoud Higler,
A Nonequilibrium Model for Reactive Distillation.
PhD. thesis of Richard Baur,
Modeling Reactive Distillation Dynamics.



WebWorm

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posted by Webworm, 4:12 AM | link | 0 Comments |