The below figure shows a pump that transfers a steady stream of 35 API crude oil from an oil tanker to a refinery storage tank, both free surfaces being open to the atmosphere. The effective length-including fittings-of the commercial steel pipe is 6,000 ft. The discharge at point 4 is 200 ft above the pump exit, which is level with the free surface of oil in the tanker. However, because of an intervening hill, point 3 is at a higher altitude than point 4. Losses between points 1 and 2 may be ignored. The crude oil has the following properties: Density p = 53 lbm/f³; Viscosity u = 13.2 cP; Vapour Pressure Pv = 4.0 psia 1,000 ft 5,000 ft Storage tank 200 ft Oil tanker
The below figure shows a pump that transfers a steady stream of 35 API crude oil from an oil tanker to a refinery storage tank, both free surfaces being open to the atmosphere. The effective length-including fittings-of the commercial steel pipe is 6,000 ft. The discharge at point 4 is 200 ft above the pump exit, which is level with the free surface of oil in the tanker. However, because of an intervening hill, point 3 is at a higher altitude than point 4. Losses between points 1 and 2 may be ignored. The crude oil has the following properties: Density p = 53 lbm/f³; Viscosity u = 13.2 cP; Vapour Pressure Pv = 4.0 psia 1,000 ft 5,000 ft Storage tank 200 ft Oil tanker
Elements Of Electromagnetics
7th Edition
ISBN:9780190698614
Author:Sadiku, Matthew N. O.
Publisher:Sadiku, Matthew N. O.
ChapterMA: Math Assessment
Section: Chapter Questions
Problem 1.1MA
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![The below figure shows a pump that transfers a steady stream of 35 API crude oil from an oil
tanker to a refinery storage tank, both free surfaces being open to the atmosphere. The
effective length-including fittings-of the commercial steel pipe is 6,000 ft. The discharge
at point 4 is 200 ft above the pump exit, which is level with the free surface of oil in the
tanker. However, because of an intervening hill, point 3 is at a higher altitude than point 4.
Losses between points 1 and 2 may be ignored.
The crude oil has the following properties:
Density p = 53 lbm/ft3; Viscosity u = 13.2 cP;
Vapour Pressure Pv = 4.0 psia
1,000 ft
5,000 ft
Storage
tank
200 ft
Oil tanker](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F1656195c-8a73-4dff-aa4f-3883644d125e%2F2eb61c67-e24e-4635-8403-c2155bd3abbe%2F9dbs11b_processed.jpeg&w=3840&q=75)
Transcribed Image Text:The below figure shows a pump that transfers a steady stream of 35 API crude oil from an oil
tanker to a refinery storage tank, both free surfaces being open to the atmosphere. The
effective length-including fittings-of the commercial steel pipe is 6,000 ft. The discharge
at point 4 is 200 ft above the pump exit, which is level with the free surface of oil in the
tanker. However, because of an intervening hill, point 3 is at a higher altitude than point 4.
Losses between points 1 and 2 may be ignored.
The crude oil has the following properties:
Density p = 53 lbm/ft3; Viscosity u = 13.2 cP;
Vapour Pressure Pv = 4.0 psia
1,000 ft
5,000 ft
Storage
tank
200 ft
Oil tanker
![CASE 1- Type Problem
If the pipeline is Schedule 40 with a nominal diameter of 6 in., and the required flow rate is
506 gpm, what pressure P2 is needed at the pump exit? Solve the problem first by manual
calculations.](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F1656195c-8a73-4dff-aa4f-3883644d125e%2F2eb61c67-e24e-4635-8403-c2155bd3abbe%2Fkhnfv06_processed.jpeg&w=3840&q=75)
Transcribed Image Text:CASE 1- Type Problem
If the pipeline is Schedule 40 with a nominal diameter of 6 in., and the required flow rate is
506 gpm, what pressure P2 is needed at the pump exit? Solve the problem first by manual
calculations.
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