I need the answer as soon as possible Q2: 1- A centrifugal pump is to be operated with discharge 2.5 m3/min. If the power needed for the motoris 15 KW, compute the total head of the pump if the efficiency of the motor is 70% and the pump efficiencyis 80%.Pali2- For the above question, if you know the atmospheric pressure is 96 kpa, vapor pressure is 15.3 kpa andthe required NPSH is 48 kpa, what will be position of the pump such to avoid cavitation. Neglect losses.

Compute the total head of the pump,H=?

Q2: 1- A centrifugal pump is to be operated with discharge 2.5 m3/min. If the power needed for the motor is 15 KW, compute the total head of the pump if the efficiency of the motor is 70% and the pump efficiency is 80%.

Q2: 1- A centrifugal pump is to be operated with discharge 2.5 m3/min. If the power needed for the motor is 15 KW, compute the total head of the pump if the efficiency of the motor is 70% and the pump efficiency is 80%.

Solid Waste Engineering

3rd Edition

ISBN:9781305635203

Author:Worrell, William A.

Publisher:Worrell, William A.

Chapter5: Separation Processes

Section: Chapter Questions

Problem 5.6P

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Concept explainers

Asphalt Binders and Mixtures

Asphalt binders are subsidiary products procured during the refining process of petroleum while manufacturing gasoline, diesel, and similar petroleum products. Asphalt binders are obtained from the residue that remains after the distillation of petroleum, this residue is further subjected to steam distillation and oxidation to remove the traces of gas oil present in the residue. Certain additives or modifiers are also added to asphalt binders to alter them to suit different applications.

Question

I need the answer as soon as possible

Q2: 1- A centrifugal pump is to be operated with discharge 2.5 m3/min. If the power needed for the motor
is 15 KW, compute the total head of the pump if the efficiency of the motor is 70% and the pump efficiency
is 80%.
Pali
2- For the above question, if you know the atmospheric pressure is 96 kpa, vapor pressure is 15.3 kpa and
the required NPSH is 48 kpa, what will be position of the pump such to avoid cavitation. Neglect losses.

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