What is a good relation to use for calculating tube bundle diameter?
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When specifying a cooling tower, should I look up historic wet bulb temperatures for my area or should I take measurements?
How 'saltation velocity' is used in designing pneumatic conveying systems?
Are there any alternatives to scraping a shell and tube if a capacity increase will make the pressure drop across the exchanger too large?
HOw to derive reynolds equation?
A concentric, counter-current heat exchanger is used to cool lubricating oil. Water is used as the coolant. The mass flow rate of oil into the heat exchanger is 0.1 kg / s = FO. For oil, the inlet temperature TIO = 100 degree Celsius and the outlet temperature TOO = 55 degree Celsius. For water, the inlet temperature TIW = 35 degree Celsius and the outlet temperature TOW = 42 degree Celsius. What is the mass flow rate of water in kg / s, FW needed to maintain these operating conditions? Constant for heat capacity of oil is CO = 2131 J /(kg K) and for water is CW = 4178 J /(kg K). Use the equation (FO)(CO)(TIO – TOO) = (FW)(CW)(TOW – TIW).
Which part of oil creates smoke? ( aliphatic, aromatic, paraffin)
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What is the significance of the minimum flow required by a pump?
What compounds are responsible for the odours that come from wastewater treatment plants?
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What is some good advice for specifying allowable pressure drops in shell and tube exchangers for heavy hydrocarbons?