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msam → shail007

well ur question is absurd:
firstly, steam at what temp and press r u talking of ? saturated or superheated ?
and water to be vaporized at what pressure ?
Mar 15 2008 03:42 AM

kandan → Art Montemayor

Dear Mont,
I am amazed by your wealth of knowledge..and the willingness to share it to younsters.. ur patiene in explaining your experience ..I admire..
Keep it up..
May u live long to continue this service..
Mar 14 2008 11:52 PM

dinda → Art Montemayor

hello..i'm new here, but i've already seen several of your information..i thought it's very useful. i hope someday you can help me too..thanks.
Mar 12 2008 08:14 PM

→ Art Montemayor

Dear Art Montemayor,
Wish you Many Happy Returns of the day.
Thank you very much for all your feedbacks and knowledge that you share with all of us.
I am currently in Hosuton TX. I sure would like to mee you whenever you have time.
Thanks a Lot.
Mar 12 2008 07:03 AM


how to calculate quantity of steam to vaporise 1 kg water completely?
Mar 05 2008 04:16 AM


I want handbook pressure vessel
Feb 29 2008 09:49 AM

meisameh → fallah

Dear Sir
please let me know if there is a book about flare?
Feb 16 2008 06:02 AM

→ striker

Wish you many more happy returns of the day my dear frnd.
Feb 11 2008 10:50 PM

→ Art Montemayor

Me he tomado el tiempo para leer la mayoría de los foros que me han interesado. En todos ellos observo un aporte técnico muy fuerte de su parte. Desde Chile, lo aplaudo calurosamente.
Gracias por su entrega.
Jan 18 2008 09:13 AM

→ talvi

Gracias, Talvi por tu predisposición y tu espíritu de servicio.
Jan 14 2008 02:29 PM

Zauberberg → Art Montemayor

Along with Norman Lieberman, definitely the strongest ChE authority I had ever met in my life. I wish I could meet him somewhere, face to face... Maybe in my future beach cafe-bar, somewhere in Greek islands...
Jan 05 2008 01:38 PM


I need help on LPG plant operation
Jan 03 2008 10:58 PM

Normally you need a bypass valve (2in or bigger)for start-up when there is a big pressure difference across the main valve. This will allow you to pressurised the system slowly untill the differential pressure across the main valve is acceptable (to prevent valve damage) before you open the main valve. For high pressure gas system, depending on gas composition and intial pressure drop across the b
Jan 03 2008 01:33 AM


Iam searching for Separation of methanol from Acetone and Methanol mixture(30:70).Any one can help in this regard
Nov 14 2007 08:47 AM

swat → aileh

did you how to perform simulation by aspen adsim
used for simulating pressure swing adsorption
also help me in this regards
Nov 09 2007 04:57 AM