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7. The region between concentric cylinders/pipes is known as the 8. A ratio which allows us to approximate friction losses in non-circular channels is known as the -(2 pts. total) 9. Pump curves are constructed by displaying pressure increase or head versus 10. Answer each of the following with positive displacement (P.D.) or centrifugal. (2 pts. each) A. - Can handle solid particulates without catastrophic failures B. Can work effectively as vacuum pump C. - Constant volumetric flow rate output D. - Downstream stoppages can cause catastrophic failures E. - Increased pressure rise across the pump with decreased volumetric flow rate 11. Failure to reach the net positive suction head (NPSH) in certain pumps can lead to

7. The region between concentric cylinders/pipes is known as the 8. A ratio which allows us to approximate friction losses in non-circular channels is known as the -(2 pts. total) 9. Pump curves are constructed by displaying pressure increase or head versus 10. Answer each of the following with positive displacement (P.D.) or centrifugal. (2 pts. each) A. - Can handle solid particulates without catastrophic failures B. Can work effectively as vacuum pump C. - Constant volumetric flow rate output D. - Downstream stoppages can cause catastrophic failures E. - Increased pressure rise across the pump with decreased volumetric flow rate 11. Failure to reach the net positive suction head (NPSH) in certain pumps can lead to

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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7. The region between concentric cylinders/pipes is known as the 8. A ratio which allows us to approximate friction losses in non-circular channels is known as the (2 pts. total) 9. Pump curves are constructed by displaying pressure increase or head versus 10. Answer each of the following with positive displacement (P.D.) or centrifugal. (2 pts. each) A. - Can handle solid particulates without catastrophic failures B. Can work effectively as vacuum pump C. - Constant volumetric flow rate output D. - Downstream stoppages can cause catastrophic failures E. - Increased pressure rise across the pump with decreased volumetric flow rate 11. Failure to reach the net positive suction head (NPSH) in certain pumps can lead to
Transcribed Image Text:7. The region between concentric cylinders/pipes is known as the 8. A ratio which allows us to approximate friction losses in non-circular channels is known as the (2 pts. total) 9. Pump curves are constructed by displaying pressure increase or head versus 10. Answer each of the following with positive displacement (P.D.) or centrifugal. (2 pts. each) A. - Can handle solid particulates without catastrophic failures B. Can work effectively as vacuum pump C. - Constant volumetric flow rate output D. - Downstream stoppages can cause catastrophic failures E. - Increased pressure rise across the pump with decreased volumetric flow rate 11. Failure to reach the net positive suction head (NPSH) in certain pumps can lead to
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