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Problem 1: Continuity and Energy Balance Below is a schematic of a Venturi device. It is esstentially a pipe with a narrowed section called the Throat, which downstream returns to the orginal pipe diameter. Venturi devices are used to measure flow rates in pipes from the pressure difference between the Main Flow (A) and the Throat (B). For the given Venturi the Main Flow region has a diameter of 5.5 cm and Thorat diameter of 3.3 cm. The the pressure difference between the Main Flow (A) and the Throat (B) has been determined to be 950 Pa. The density of the process fluid is 980 kg/m3. Neglect friction over this small region of the device. Main Flow (A) Throat (B) V1 D1 V2 D2 A. What is the velocity in the Throat (B)? B. What is the velocity of the Main Flow (A)?

Problem 1: Continuity and Energy Balance Below is a schematic of a Venturi device. It is esstentially a pipe with a narrowed section called the Throat, which downstream returns to the orginal pipe diameter. Venturi devices are used to measure flow rates in pipes from the pressure difference between the Main Flow (A) and the Throat (B). For the given Venturi the Main Flow region has a diameter of 5.5 cm and Thorat diameter of 3.3 cm. The the pressure difference between the Main Flow (A) and the Throat (B) has been determined to be 950 Pa. The density of the process fluid is 980 kg/m3. Neglect friction over this small region of the device. Main Flow (A) Throat (B) V1 D1 V2 D2 A. What is the velocity in the Throat (B)? B. What is the velocity of the Main Flow (A)?

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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Homework: Below is a schematic of a Venturi Problem 1: Continuity and Energy Balance device. It is esstentially a pipe with a narrowed section called the Throat, which downstream returns to the orginal pipe diameter. Venturi devices are used to measure flow rates in pipes from the pressure difference between the Main Flow (A) and the Throat (B). For the given Venturi the Main Flow region has a diameter of 5.5 cm and Thorat diameter of 3.3 cm. The the pressure difference between the Main Flow (A) and the Throat (B) has been determined to be 950 Pa. The density of the process fluid is 980 kg/m³. Neglect friction over this small region of the device. Main Flow (A) Throat (B) V1 D1 V2 D2 A. What is the velocity in the Throat (B)? B. What is the velocity of the Main Flow (A)?
Transcribed Image Text:Homework: Below is a schematic of a Venturi Problem 1: Continuity and Energy Balance device. It is esstentially a pipe with a narrowed section called the Throat, which downstream returns to the orginal pipe diameter. Venturi devices are used to measure flow rates in pipes from the pressure difference between the Main Flow (A) and the Throat (B). For the given Venturi the Main Flow region has a diameter of 5.5 cm and Thorat diameter of 3.3 cm. The the pressure difference between the Main Flow (A) and the Throat (B) has been determined to be 950 Pa. The density of the process fluid is 980 kg/m³. Neglect friction over this small region of the device. Main Flow (A) Throat (B) V1 D1 V2 D2 A. What is the velocity in the Throat (B)? B. What is the velocity of the Main Flow (A)?
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