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10. your final an A hydrocarbon mixture is being pumped from a tank at atmospheric pressure (101.3 x 103 Pa) to a distillation tower. The density of the feed is 750 kg/m³, and its vapor pressure is 58.3 x 103 Pa. The velocity in the inlet line to the pump is 1 m/s and the friction loss between the tank and pump is 1 m of fluid. The net positive suction head required is 2 m. How far below the liquid level in the tank must the pump be to obtain this required (NPSH)R?

10. your final an A hydrocarbon mixture is being pumped from a tank at atmospheric pressure (101.3 x 103 Pa) to a distillation tower. The density of the feed is 750 kg/m³, and its vapor pressure is 58.3 x 103 Pa. The velocity in the inlet line to the pump is 1 m/s and the friction loss between the tank and pump is 1 m of fluid. The net positive suction head required is 2 m. How far below the liquid level in the tank must the pump be to obtain this required (NPSH)R?

Introduction to Chemical Engineering Thermodynamics
Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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10. your final an A hydrocarbon mixture is being pumped from a tank at atmospheric pressure (101.3 x 103 Pa) to a distillation tower. The density of the feed is 750 kg/m³, and its vapor pressure is 58.3 x 103 Pa. The velocity in the inlet line to the pump is 1 m/s and the friction loss between the tank and pump is 1 m of fluid. The net positive suction head required is 2 m. How far below the liquid level in the tank must the pump be to obtain this required (NPSH)R?
Transcribed Image Text:10. your final an A hydrocarbon mixture is being pumped from a tank at atmospheric pressure (101.3 x 103 Pa) to a distillation tower. The density of the feed is 750 kg/m³, and its vapor pressure is 58.3 x 103 Pa. The velocity in the inlet line to the pump is 1 m/s and the friction loss between the tank and pump is 1 m of fluid. The net positive suction head required is 2 m. How far below the liquid level in the tank must the pump be to obtain this required (NPSH)R?
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