You're right, I'm not being specific because I was hoping (ideally) for general guidance. Some utilities fall out of your design naturally (e.g. cooling water), and some I have rules of thumb for, but nitrogen and waste water loads are proving intractable.
It's a 75kBPSD heavy middle eastern...
Here are some techniques I've seen schools adopting, and other ideas that are worth chewing on:
-We want courses on design taught by experienced engineers but are worried about finding the instructors. Have a few multi-discipline "Design Courses" taught by generalists from industry; people who...
BUMP.
If no one knows, does anyone know someone that would know?
I mean some major companies must have design procedures for this sort of thing, right? Are any willing to sell these kinds of procedures, or perhaps be hired for a one-day consultation?
CHD01, thank you for the excellent reply. I believe I understand what you are saying. Even though w3 > w2, scenario 2 controls because a2_req > a3_req. The lines will be sized using wreq = w2 * a_act/a2_req = 1085 lb/hr.
The flare header will be sized assuming w1, w2, or w3, is relieved...
Hello,
I've just started working through my first relief project and am getting conflicting advice sizing relief valve lines. Allow me to explain with a hypothetical example, because I'd like to learn the general principle/approach instead of just getting through a single problem:
Say I have...
I'm working on basic engineering (P&ID-level initial design) of a proposed new refinery. We will need a nitrogen plant to generate N2 for start-up/shutdown/continuously purging some lines/etc.
I've had no problems finding information and vendors to get a nitrogen plant to SUPPLY the N2.
But I...
I believe that you can just use the steam equation in API 520 Section 3.7 to size the PSV orifice, taking the maximum operating turbine steam feed for the load W (lb/hr).
I'm not 100% certain, though. It would be great if someone with more experience could comment.
At work I get passed around to different bosses and even departments, and one point of contention is the "calculation record" - also called a design brief or design calculation. Datasheets and technical drawings have a really defined structure, but calc. records do not. It seems that everyone...
There is a similar rule where I work, and it cheesed me off too. Why can't a client get their own independant review whenever they want? And what exactly is meant by "terminated?" Do I have go tell my coworker who got moved to a different project that I'm looking at his calcs?
This thread has...
Yeah, MortenA is correct. Right now UniSim is 99% identical to Hysys because they have almost the same code, and UniSim can open and save as Hysys files. But both are being supported and both will develop in different directions.
JAIFAR,
I have attached my old calculation to this post. It may help you formulate a strategy to tackle your problem. Please note the disclaimer.http://files.engineering.com/getfile.aspx?folder=a2627c65-0aa4-4b77-8ee4-ebc421d0bbf5&file=Equilibrium_Flash_Calculation.xls
Back in school, 3rd year thermo, I did a L+V=1 calculation using Smith/Van Ness/Abbott and the Wilson method. I'm pretty sure you're trying to do the same kind of calculation. So you can do it. But it took ages to do for a simple three-component mixture when I was given the correct pressure to...
Try looking up UniSim Design by Honeywell as an alternative to Hysys. It's almost identical and may be cheaper.
For the programs you consider, you should find out what support is available at what price. Can you call a support line for help? Can you hire some experts (from the software people...
Thank you all for the great advice.
After browsing a catalog or two using vzeos' suggested equation, it looks like K~4.5 is the right number. I may be able to replace the valve with a larger line to cut down the velocity/corrosion. If not, I'll use 4.5 + some fat.
Hi folks,
To empty a tank on occasion, I'm planning to install a PD pump, pumping about 30-60 gpm of warm water through a 2" line. At the end of the line my circuit will join into a larger 50 psig line. I'll add a check valve for when my line's not in use. Right now I'm doing the hydraulics and...
