dear ak1965,
this arrangement is commomly used in the industry. I am tempted to assume there is a design flaw. I recommend you to search for profesional help. The situation could easily get very dangerous. Eng-tips is a great place to search for information but probably not ideal in your case.
rgs
Dear RR79,
I found some information with similar values as you posted but I am interested in lower steam pressure (< 20 bar, water around the tubes)
In some text they had a formula (but not a reference):
max Steam volume load =
0,264*10E3 * pE-0,7 * C exp -0,61
p pressure (bar)
C...
Dear RMW,
the link contain some information but is not enough detailed, thks.
Chicopee,
as I already wrote to RMW I have the book and by the way it is not a so great reference for this problem.
RGS
Dear Sirs,
I am trying to review some steam evaporators (HRSG) installed in our plant. Some operators suggest that the systems are prone to carry-over leading to flooding of the steam line.
I would ask for some design recomendations (Book references, articles or WWW-pages). There is an earlier...
Dear RMW,
as posted I check already the posting in this site and googled more than 5 pages. I have too the "Steam Book" from B&W but they only offer descriptional information of the factors affecting the steam separators. If you have useful information please comment.
RGS
Dear Sirs,
I am trying to review some steam evaporators (HRSG) installed in our plant. Some operators suggest that the systems are prone to carry-over leading to flooding of the steam line.
I would ask for some design recomendations (Book references, articles or WWW-pages). There is an earlier...
Dear Mr. Dias,
if you visit the site www.spiraxsarco.com you will find some information about heat tracing.
In some contries with high labor cost the tendence is to install electrical heat tracing but also to use metallic hoses...
To liquify and store N2 is a feasible task. If you want to design it yourself, well good luck.
If you want a straigth forward solution perhaps you should contact the usual suspects in the liquid nitrogen scene (Liquid Air, Praxair, Linde ect). they have standarized solutions which can be...
The problem here is that the lack of context makes the search for the proper answer more difficult. If you give more information perhaps the answer will be better.
There are several kinds of blowdowns:
1. Steam Boiler. two blowdonwns here
continious blowdown. the goal is to reduce the...
Dear Sir,
I assume that you already got information like "Calculation of overall heat transfer coefficients in a triple tube heat exchanger", Batmaz, Ediz; Sandeep, K. P.
What is specifically your problem? If you are a bit more specific perhaps you would get an answer.
Rgs
Hello,
I am looking for information regarding freezing/ solidification fouling like a published articles (internet) or Books handling this matter. Important would be recommendations and design guidelines.
Most of the book have only three to four sentences about this :-((see google books)
kind...
Clindeman,
a CIP process depends strongy on many factors like:
a) Product
b) degree of dirtiness at the begining
c) degree of cleanness needed
d) geometry of the vessel
There is a lot of "trial and error" involved. The flow you mention is probably for only one set of conditions. That is why to...
