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Messages 2831 - 2861 of 4489   Oldest  |  < Older  |  Newer >  |  Newest
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2831
Hi Leila, Here's a web page from Lubrizol who manaufactures AMPS. http://www.lubrizol.com/AMPS/ -Doug ... From: leila leila [mailto:leila_kian2000@...] ...
Doug Morgan
dmorgan@...
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Mar 1, 2004
4:04 pm
2832
Hello, We are performing LCA of air pollution control technologies. Does anyone know of studies/sources containing LCA information/data about granular...
Amit Kaldate
a_kaldate@...
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Mar 1, 2004
4:44 pm
2833
hi friends! i am student of final year computer science as our final year project we are working on simulation of multicomponent distillation( process...
uha_2004
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Mar 2, 2004
3:30 pm
2834
... I wouldn't think your prof is interested in the property estimation or efficiency aspect of things, just the raw vapor-liquid equilibrium (VLE) solution...
Doug Morgan
dmorgan@...
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Mar 2, 2004
7:05 pm
2835
===== Manish Dalal Head - Business Development ''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''''' Manpurv Marketing Inc. India. email:...
manish dalal
m_zone2k
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Mar 2, 2004
8:07 pm
2836
if u can read this reply for me ur answer salam shoma kodam danesh gah dars mikhoonid? man khodam ro in made kar nakardam vali mipprsam age toonestam baratoon...
behrad montazeri
behrad_79
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Mar 3, 2004
7:48 am
2837
C A R B O N S Manufacturers of Diamonds & Exclusive Diamond Jewellery Phone: (m) 0261 3116000 Email: manishdalal@......
manish dalal
m_zone2k
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Mar 4, 2004
5:53 am
2838
thankx for the help few things more that confuse are 1 . abt side streams how the calculations for minimum no of stages, dewpoint ,buble point,composition...
uha_2004
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Mar 4, 2004
7:28 pm
2839
You seem to be on the right track as those are all good questions. When I suggested writing an application that works through that example (15.1), I was...
Doug Morgan
dmorgan@...
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Mar 4, 2004
8:04 pm
2840
BTW: Adding more stages is not a trivial matter because it changes the size of the tridiaganol matrix. Also, you'll need extra K-Values. K-Values are the...
Doug Morgan
dmorgan@...
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Mar 4, 2004
9:31 pm
2841
Hello Mr Doug Morgan, I am also doing the simulation of a crude distillation column with side strippers and pump arounds. I am using steam as a heating source...
nm shah
mktmshah
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Mar 5, 2004
9:11 am
2842
Good question. Steam injection does provide a driving force to get more material in the vapor phase. It's like adding more water to a saturated salt...
Doug Morgan
dmorgan@...
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Mar 5, 2004
4:02 pm
2843
thankx for the help a lot but i am unable to locate the book u r mentioning and as u mentioned that example could help a lot it would be very kind if u can...
uha_2004
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Mar 6, 2004
4:22 am
2844
Hi Doug!!!!!!!! If steam injection is there in the distillation column.... As we know that y=Kx and y is the mole fraction in the vapor phase. Steam injection...
Sourabh Gupta
sourabh1002000
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Mar 6, 2004
7:14 am
2845
The K-value in vapor-liquid equilibrium is an equilibrium thermodynamic property. It is defined as the activity coefficient of the species in the liquid...
Bruce A. Finlayson
finlayson@...
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Mar 8, 2004
4:15 pm
2846
You can have the Linda Hall Library scan and email you the pages of interest for a small fee. Here is a link to the search page results that show the book....
Doug Morgan
dmorgan@...
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Mar 8, 2004
4:27 pm
2847
That's what I was suggesting. It's been a while since I utilized a package designed for crude distillation so I don't recall the specific effect on K-values. ...
Doug Morgan
dmorgan@...
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Mar 8, 2004
7:49 pm
2848
I will be out of the office starting 03/09/2004 and will not return until 03/21/2004. I will respond to your message when I return. __ IMPORTANT NOTICE: This...
kapil.goswami@...
kapil6dl
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Mar 9, 2004
7:33 pm
2849
hi, Could anyone pls. provide me with links or algorithm or solving the ADI method for 2 dimentional diffusion equation Regards, Namit Roy ...
namit roy
namit_roy
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Mar 14, 2004
7:12 pm
2850
Namit Roy, If you are only interested in a subroutine Numerical Recipes has one. Paul Safier ...
paul safier
angrysamoan72
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Mar 14, 2004
7:45 pm
2851
Dear Paul, What i need to know is this. I am really confused with the iterations that we need to do in each time step. What I have understood is this, if I...
namit roy
namit_roy
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Mar 15, 2004
1:58 am
2852
... The ADI method was developed in the oil industry, and the best information about the convergence is in Peaceman's book, "Fundamentals of Numerical...
Bruce A. Finlayson
finlayson@...
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Mar 15, 2004
4:39 pm
2853
what's the problem write me in detail i am also working on this project but just modelling and simulation. ... equilibrium ... Engineering", ... year ... ...
vipin_iu
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Mar 18, 2004
9:47 am
2855
Hi, I am modeling one RD column (70 trays and 14 components)in gPROMS. What i have done so far is built the model by taking smaller number of trays initially....
arnabchakrabarty
arnabchakrab...
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Mar 19, 2004
9:24 pm
2856
Hi Arnab, I guess u might be using the concept of High Level model and Primitive model of gPROMS and using the stream concept to link different instances of...
Ravi Chandra
chandu822
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Mar 22, 2004
2:51 am
2857
HI , Can anyone tell me abt the industrial uses of Esterification and Hydrolysis as in What are the main methods for esterification and hydrolysis in the ...
gopi p
pgkkumar
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Mar 22, 2004
2:38 pm
2858
Hi fellows May any one provide me information on kinetics of CaO with water vapour( mole fraction of water vapour~0,1) or clue to it. Best Regards Mahmood...
Mahmood Saleem
ms67m
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Mar 23, 2004
1:10 pm
2859
Hii All, One of my friends has just joined this group but not got the confirmation but she needs help urgently. So I am forwarding her problem to you all. ...
nm shah
mktmshah
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Mar 26, 2004
11:16 am
2860
hello everyone, i am a new member of the group, and have just joined it. i am doing my post graduation in chemical engineering with a specialisation in...
neha soni
neha_chemical
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Mar 26, 2004
11:38 am
2861
Dear members At the outset,let me apologise for cross posting.We have a problem of high stack temp in our HRSG.The relevant details(pretty long) are enclosed ...
Sridhar V
VSridhar@...
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Mar 26, 2004
1:06 pm
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