shvet's latest activity

This is the prompt you to start with the basics and rely less on the beliefs of unknown people. This is chemical engineering, which is...

Testing at a lab or pilot scale. Your case is unique. You are mixing two immiscible liquids 1:50 and one of them is highly viscous at...

Displacing a hazardous gas with an inert foam, often called nitrogen foam inerting.

Given 7kPa per 1 element I bet on those are not coated with plastic but made of instead as buckling is not an issue. The perforated...

On homogenity of the mix downstream. The cost of the most expensive static mixer is negligible compared to the risk of potential profit...

Let me express in another words No a straight run => swirl at the suction nozzle => flow maldistribution or assymetric at an impeller...

How is the swirl oriented relative to the impeller(s)? Was this pump tested for uneven flow? Was the impact on NPSHR and bearing&seal...

Is there a need in theorizing of the fluid properties? How are you going to prove those are relevant? Why can't you provide a simple...

https://datatool.pumps.org/tools/frictional-losses https://www.lmnoeng.com/ https://checalc.com/fluid_flow.html...

@mohamed The question is definetly unclear. Describe what is an issue and our concerns.

Just stumble upon the ASME's report. Maybe it can help ASME STP-PT-049 Investigation of Temperature Derating Factors for High-Strength...

You want to know the allowable accumulation in the boiler as per Sweden jurisdiction codes, correct? 3% or 6% or 10% or 15% or whatever...

@LittleInch See below and bolded in CCPS above . Note that ExxonMobil and CCPS do not distinguish hydrogen and hydrogen-hydrocarbons as...

@AutoDirt some pointers can be found at the EIGA's guide https://www.eiga.eu/uploads/documents/DOC211.pdf The snuffing steam design can...

(1) a very expensive, (2) complicated, (3) occupied a lot of space, (4) requiring a personnel attention, and (5) not a robust mean...