Recent content by Zion309

Problem solve through the use of gas dispersion modeling software. Sorry for creating this thread that goes nowhere. Lesson learned: Lot of talks will not solve the problem. Got more work to do. Thanks

Leak scenar I understand your concern. HAZOP study was done by a team of subject matter expert from research, technology, EHS including the designer of bench scale reactor.

Hood Specification: NFPA 45 / ASHRAE 110 / ASTM E84 to comply with NEC / NFPA 70, Class I locations where flammable gasses or vapors may be present in the air in quantities sufficient to produce explosive or ignitable mixtures.

In the profile question, there are no alternative answer in the dropdown list for "Education in Progress" and "Completed Educational Background".

Sorry for not putting all the information which I admit is my mistake of not reading thoroughly the forum rules. My inquiry is the result of Hazard Operability Study (HAZOP) conducted on bench scale reactor inside the walk-in fume hood. HAZOP team raised a recommendation to verify if the fume...

Thanks for the comment. Would love to hear from you what formula to use wherein only line pressure and diameter is given.

To verify if the walkin fumehood is capable to exhaust the hydrogen gas in case of leak. Thank you.

Hi. I'm a mechanical engineer, but working as Safety Engineer. I have a question how to calculate the flow rate of hydrogen gas before a flow controller in case of leak through a 4.5 mm line at 35 bar pressure. Thanks in advance.