Does anyone have a good cost manual reference for "percent of delivered equipment cost". I need it for process equipment and not environmental equipment(i.e. reactors, tanks, process equipment).
Always work smarter, not harder. Check out eaton for vapor liquid separators, and I bet your process requirments are orders of magnitude smaller than their smallest units. Check out the link as follows:
http://www.eaton.com/Filtration/USA/Products/SeparatorProducts/index.htm
I have the narrative for why as follows:
http://files.engineering.com/getfile.aspx?folder=dcdeccc4-9e5a-46a4-8326-3ca10ae3a18e&file=BizHub35020110928125442_Rev.jpg
http://files.engineering.com/getfile.aspx?folder=dcdeccc4-9e5a-46a4-8326-3ca10ae3a18e&file=BizHub35020110928125442_Rev.jpg
First, Good news. I found the information in Perry's.
But I am working on a secret project, and the model is analogous to chemical engineers as a square tank with a square orifice. Same paradigm, but my model could have confused everyone.
I find that posting a question takes a few days...
Does anyone know the equation to calculate the area of an square orifice? The model is a closed pressurized square tank with a square orifice, and the fluid is steam. I need to control the pressure in the tank by determining the square orifice area.
Does anyone know the Water Reactive 3 explosion venting design criteria for in a H2/H4 occupancy? We need to meet the 2009 IFC 4404.1.6.
So far, NFPA 68 regulates deflagration venting for flammable gases, dusts, and liquids. However it isn't used for Water reactive 3 materials. That's were I...
I need to specify laboratory fume hood exhaust duct for intermittent usage 25% hydrochloric acid solution. Basically the fume hood and exhaust duct system is for flammable solvents, and the everyone wants to save money. I specified a ETFE lines 304 stainless steel duct however the client wants...
Good news, I notice the Perry's pipe friction loss equation has a 4 coefficient, and the chart is 4 time less than Crane # 410. Now Crane #410's chart is 400% larger, but their friction loss equation drops the 4 coefficient. Therefore, both ways produce the same numbers in the end.
They...
Crane #410 has 400% more friction factor in the "fiction factors versus Reynold #" table. Does anyone know why?
I compared the Crane #410 table to the Moody, Trans. ASME 66, 671 [1944] friction factor table. This table is located in the Perry's Chemical Engineering Handbook in the Fluid and...
According to the msds, chlorine dioxide LEL is 10%. In your product conveying duct design, you need to keep the exhaust below 25% of the LEL which is 2.5% in accordance with 2007 CMC 506.
I live in California, so we use the 2007 California Plumbing Code to size natural gas pipe. For natural gas, we calculate the natural gas pipe size using an equation in the natural gas section of the 2007 California Plumbing Code. Usually it's medium pressure which means greater than 2 psig...
