AFCL Store
 
 
Login Form





Lost Password?
No account yet? Register
Resources
Home
Drinking Water
Industrial Water Treatment
Cooling Water Treatment
Boiler Water Treatment
Water Treatment Plants
Know Your Heat exchangers
Boiler
Cooling tower
Industrial Wastewater Treatment
Blog
Search
Sitemap
Products
Water Distribution System Handbook
Water Distribution System Handbook
$125.00
Add to Cart


Water Quality Characteristics
Water Quality Characteristics
$139.00
Add to Cart


Corrosion Inhibitors: Principles and Applications
Corrosion Inhibitors: Principles and Applications
$535.00
Add to Cart


Boiler Water Treatment Hand Book
Boiler   Water Treatment Hand Book
$78.00
Add to Cart


Freshwater Issues
Freshwater Issues
$57.49
Add to Cart


Your Cart
Show Cart
Your Cart is currently empty.
Syndicate
AFCL Store
Books (27) E Books (1)

List All Products


Advanced Search
Download Area
Show Cart
Your Cart is currently empty.
Overall heat transfer coefficient Print E-mail

An important parameter in the design and monitoring of heat exchangers is the overall heat transfer coefficient, U, between the two fluids. A value for U can be easily obtained by knowing the followings:

1.      Mass flow of the fluid,

2.      Specific heat of the fluid,

3.      Difference in temperature of the fluid across the heat exchanger,

4.      Inlet and outlet temperature of both the fluids involved in heat exchanger and

5.      Area of the heat transfer surface.

 

 

From the equation         Q = m.cp. Δt

Calculating Q in watts:

Where m = mass flow in kg/hr of kg/sec

            Cp= specific heat or heat content in KJ/Kg K

            Δt= Temperature difference across the heat exchanger.

 

Calculating LMTD from the following equation with the inlet and outlet temperatures of the hot and cold fluid across the heat exchanger and with the knowledge of type of heat exchanger using:

 

(For multipass heat exchangers)

ΔT m =    (T2-t1) – (T1 – t2)                                                                           

               ln [(T2-t1)/(T1-t2)]

 

Where ΔT m = log mean temperature difference,

            T1  = inlet shell side fluid temperature,

            T2  = outlet shell side fluid temperature,

            t1   = inlet tube side temperature,

            t2   = outlet tube-side temperature,

 

 OR

 

 

(for single pass heat exchanger)

Δtm = (T1-t2) +(T2-t1)                                    

                        2

 

We can calculate U from the equation                Q = UA Δtm

Where Q = heat transferred per unit time (W)

            U = the overall heat transfer coefficient (W/m2  oC)

            A –heat-transfer area, m2,

            Δtm = the mean temperature difference, the temperature driving force, oC.

 

U =      .   Q   .                                                                                                 (eq. 1.14)

            A Δtm

Page: 1 | 2 | 3 | 4 | 5 | 6 | 7 | 8 | 9 | 10 | 11 | 12 | 13 | 14 | 15 | 16 | 17 | 18 | 19 | 20

Introduction | Combined heat transfer process | Heat transfer in cooling tower | Variables affecting performance of CT heat transfer | Heat transfer within cooling system (heat exchanger) | Types of heat exchanger | Basic design procedure and theory | Designing a test heat exchanger | Log Mean Temperature difference | L.M.T.D. Correction factors | Overall heat transfer coefficient | Elaborated method for calculating U values | Effect of scale formation | Condensation of steam | Condenser, where the hot fluid temperature varies | Significance of pressure | Significance of flow rate | Methods of checking steam condenser performance | Common conversion factors
 

 
Editor's choice of books

 

Free Ebooks

Books on Waste Water Treatment

Books on Reverse Osmosis

Books on Cooling Water Treatment

Books on Boiler Water Treatment

 
 
   Copyright © 2006 Albatross Fine Chem Ltd.. All rights reserved.