..s) A mixer with a flat blade turbine impeller with six blade-disk is used in a mixing process. The mixing tank has a 2.46 ft impeller diameter, 0.15 m turbine blade width, 2.4 m tank diameter, 0.2 m baffle width, and a liquid depth of 7.874 ft. The mixing fluid has a viscosity of 30 cP and a density of 78 lb/ft. The turbine speed is 120 rpm. Calculate the power in W that is needed to operate this mixer. 100 60 40 2,3 20 10 1 2 3 4 0.6 0.4F 5 0.2 ui 0.1 2 4 102 2 4 103 2 4 109 4 2 10 4 2 4 105 DNp N'Re %3D P Np 642 4-

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
icon
Related questions
Question
100%

Heat Transfer Question 

### Text Transcription

**Problem Statement:**
A mixer with a flat blade turbine impeller with six blade-disk is used in a mixing process. The mixing tank has a 2.46 ft impeller diameter, 0.15 m turbine blade width, 2.4 m tank diameter, 0.2 m baffle width, and a liquid depth of 7.874 ft. The mixing fluid has a viscosity of 30 cP and a density of 78 lb/ft³. The turbine speed is 120 rpm. Calculate the power in W that is needed to operate this mixer.

### Graph Explanation

**Description:**
The graph provided is a logarithmic plot, where the x-axis and y-axis are both on logarithmic scales. The graph is used to find the Power Number (NP) based on the Reynolds number (N'Re). 

- **X-Axis:** The scale is logarithmic, ranging from 1 to \(10^5\). This axis represents the Reynolds number, \(N'Re = \frac{D_a^2N\rho}{\mu}\).

- **Y-Axis:** The scale is logarithmic and displays values from 0.1 to 100. This axis represents the Power Number, \(N_P = \frac{P}{\rho N^3 D_a^5}\).

- **Curves:** Five distinct curves are labeled 1 through 5. These curves correspond to different configurations or conditions of the mixer system.

### Formula Explanation

1. **Power Number (NP):**
   \[
   N_P = \frac{P}{\rho N^3 D_a^5}
   \]
   - \( P \) is the power (W)
   - \( \rho \) is the fluid density
   - \( N \) is the rotational speed
   - \( D_a \) is the impeller diameter

2. **Reynolds Number (N'Re):**
   \[
   N'Re = \frac{D_a^2 N \rho}{\mu}
   \]
   - \( \mu \) is the fluid viscosity

This graph is used in the context of mixing processes to determine the relationship between the mixing dynamics and the required power, given specific fluid and impeller properties.
Transcribed Image Text:### Text Transcription **Problem Statement:** A mixer with a flat blade turbine impeller with six blade-disk is used in a mixing process. The mixing tank has a 2.46 ft impeller diameter, 0.15 m turbine blade width, 2.4 m tank diameter, 0.2 m baffle width, and a liquid depth of 7.874 ft. The mixing fluid has a viscosity of 30 cP and a density of 78 lb/ft³. The turbine speed is 120 rpm. Calculate the power in W that is needed to operate this mixer. ### Graph Explanation **Description:** The graph provided is a logarithmic plot, where the x-axis and y-axis are both on logarithmic scales. The graph is used to find the Power Number (NP) based on the Reynolds number (N'Re). - **X-Axis:** The scale is logarithmic, ranging from 1 to \(10^5\). This axis represents the Reynolds number, \(N'Re = \frac{D_a^2N\rho}{\mu}\). - **Y-Axis:** The scale is logarithmic and displays values from 0.1 to 100. This axis represents the Power Number, \(N_P = \frac{P}{\rho N^3 D_a^5}\). - **Curves:** Five distinct curves are labeled 1 through 5. These curves correspond to different configurations or conditions of the mixer system. ### Formula Explanation 1. **Power Number (NP):** \[ N_P = \frac{P}{\rho N^3 D_a^5} \] - \( P \) is the power (W) - \( \rho \) is the fluid density - \( N \) is the rotational speed - \( D_a \) is the impeller diameter 2. **Reynolds Number (N'Re):** \[ N'Re = \frac{D_a^2 N \rho}{\mu} \] - \( \mu \) is the fluid viscosity This graph is used in the context of mixing processes to determine the relationship between the mixing dynamics and the required power, given specific fluid and impeller properties.
Expert Solution
trending now

Trending now

This is a popular solution!

steps

Step by step

Solved in 2 steps with 3 images

Blurred answer
Knowledge Booster
Convective mass transfer between phases
Learn more about
Need a deep-dive on the concept behind this application? Look no further. Learn more about this topic, chemical-engineering and related others by exploring similar questions and additional content below.
Similar questions
  • SEE MORE QUESTIONS
Recommended textbooks for you
Introduction to Chemical Engineering Thermodynami…
Introduction to Chemical Engineering Thermodynami…
Chemical Engineering
ISBN:
9781259696527
Author:
J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:
McGraw-Hill Education
Elementary Principles of Chemical Processes, Bind…
Elementary Principles of Chemical Processes, Bind…
Chemical Engineering
ISBN:
9781118431221
Author:
Richard M. Felder, Ronald W. Rousseau, Lisa G. Bullard
Publisher:
WILEY
Elements of Chemical Reaction Engineering (5th Ed…
Elements of Chemical Reaction Engineering (5th Ed…
Chemical Engineering
ISBN:
9780133887518
Author:
H. Scott Fogler
Publisher:
Prentice Hall
Process Dynamics and Control, 4e
Process Dynamics and Control, 4e
Chemical Engineering
ISBN:
9781119285915
Author:
Seborg
Publisher:
WILEY
Industrial Plastics: Theory and Applications
Industrial Plastics: Theory and Applications
Chemical Engineering
ISBN:
9781285061238
Author:
Lokensgard, Erik
Publisher:
Delmar Cengage Learning
Unit Operations of Chemical Engineering
Unit Operations of Chemical Engineering
Chemical Engineering
ISBN:
9780072848236
Author:
Warren McCabe, Julian C. Smith, Peter Harriott
Publisher:
McGraw-Hill Companies, The