Page 1 of 12

European Journal of Business &

Social Sciences

Available at https://ejbss.org/

ISSN: 2235-767X

Volume 07 Issue 04

April 2019

Available online:https://ejbss.org/ P a g e | 1352

ENHANCEMENT OF HEAT TRANSFER COEFFICIENTS

OF HEAT EXCHANGER

PRABAKARAN .S

PG Student,

PRIST Deemed to be University, Thanjavur

Abstract – A shell and tube heat

exchanger are the best common type of

heat exchanger in oil refineries and other

large chemical process industries and is

suited for higher-pressure applications.

The designs of thermal energy systems

have crossed many ways in the past few

decades which lead to some improvements

in performance. Even though various

techniques were applied to enhance heat

transfer, there is still bright scope for the

improvement of the performance. For

many decades, efforts have been done by

many researchers to enhance heat transfer

of heat exchangers and finally reported a

reasonable increase in heat transfer

characteristics of nanofluids when

compared to the respective base fluids.

Most of the research works have been

carried out for different nanofluids like

CuO/Water, Al2O3/water, TiO2/Water,

Graphite/water, Ethylene Glycol/Water,

Silicon Nitride/Water and Carbon

nanotube/Water for the study of heat

transfer enhancement in bare tube, twisted

tape and with coils separately.

An improvement in heat transfer co- efficient studied by using Graphite /water

& Al2O3/water nanofluids in shell and tube

heat exchanger increase at different

volume concentration of the nanoparticles

compared with water. We have taken up

these nanofluids and compared to find out

which fluid is having more heat transfer

enhancement at different concentrations

and flow rates in bare tube, twisted tape

with right and left twist. Hence this work

has been taken up for this work.

Keywords- Heat exchanger, shell and tube,

nano fluids

I.Introduction

The Shell and tube heat exchanger are an

important class of heat exchanger designs. In

oil refineries and other large chemical and

process industries this type of shell and tube

heat exchanger is mostly used and best is

suited for higher-pressure applications. As its

name implies, it consists of a shell (a large

pressure vessel) with number of tube made as

a bundle inside it. One fluid flows inside the

tubes and another fluid runs over the tubes

Page 2 of 12

European Journal of Business &

Social Sciences

Available at https://ejbss.org/

ISSN: 2235-767X

Volume 07 Issue 04

April 2019

Available online:https://ejbss.org/ P a g e | 1353

(through the shell) to transfer heat between

these two fluids. The number of tubes

assembled called a tube bundle and may have

several pairs of tubes namely plain,

longitudinally finned etc.

In this heat exchanger two fluids flow at

different temperatures. One fluid flows into

the tubes and the other fluid flows inside the

shell (the shell side).

Transfer of heat occurs from one fluid to

the other through the walls of the tube, either

from shell side to tube side or vice versa. The

fluids may be either liquids or gases on the

shell side or the tube side. To improve the

transfer heat effectively, a large heat transfer

area should be used, leading to more number

of tubes may be used. In this way, waste heat

can be put to use. This is one of the most

efficient ways to conserve energy. There are

many variations in actual practice on the shell

and tube design. Typically, the ends of each

tube are connected to water chambers

(sometimes called water boxes) through holes

in tube sheets. The tubes may be straight or in

the shape of ‘U’ called U-tubes.

The Pressurized water reactors in nuclear

power plants and steam generators which are

otherwise called as large heat exchangers, are

two pass – shell and tube heat exchangers

which have U tubes. These exchanger are

being utilized to boil water which are recycled

from a surface condenser into steam to drive a

turbine to produce power. Most of the shell

and tube heat exchangers are 1, 2, or 4 pass

designs on the tube side. The important use of

this multi pass is to make the fluid passes

through the tubes and shell into number of

times. In a single pass heat exchanger, the fluid

goes from one end of the tube and comes out

through the other.Surface condensers in power

plants generally have single pass straight-tube

heat exchangers. Two and four pass designs

are common because the fluid enters and exits

on the same side. This makes construction

much simpler.

The objective of the project work is to

investigate the heat transfer characteristics of

water/water, Graphite/water and Al2O3/water

nanofluids in a horizontal 1-2 shell and tube

heat exchanger. The behavior of Nusselt

number, thermal conductivities, viscosities,

specific heat capacities, heat transfer

coefficients of various nano fluids such as

Graphite /water and Al2O3/water are to be

studied.

Using suitable inserts like left twisted

tape, right twisted tape 1-2 Shell and Tube heat

exchanger, suitable nanofluids for heat transfer

applications that have more amount of heat

transfer enhancement need to be identified.

Page 3 of 12

European Journal of Business &

Social Sciences

Available at https://ejbss.org/

ISSN: 2235-767X

Volume 07 Issue 04

April 2019

Available online:https://ejbss.org/ P a g e | 1354

II.Experimental Setup

The experimental setup has pump,

water storage tank of capacity 175 lit,

water heater, shell and tube heat

exchanger and thermocouples at inlet and

outlet to measure the temperature. The

thermocouples were calibrated by PT100

type and the error in them is less than 0.1

LC. The thermocouples 1 and 2 are used

to measure the inlet temperature and the

exit temperature of the nano fluid and on

the contrary the thermocouples 3 and 4

measure the inlet temperature of the base

fluid. In order to get very good

experimental results, first of all equipment

is made stable by passing the water

through the shell as well as the tube side

of the heat exchanger.

The experimental setup consists of a

shell with 51 mm inside diameter and the

tube bundle consisting of 6 tubes with 8

mm outside diameter, 1mm thickness and

518 mm length and the tube pitch is 8

mm. The baffle spacing is 15% and 129.5

mm respectively. The heat exchanger as

well as the pipe is strongly wound by a

thermal insulation tape. Two series of

solution are prepared such as aluminium

oxide-water and graphite-water where

water flows through the shell side in both

the cases. To prepare stable nanofluids,

ultrasonic vibrations were made to pass

through it to prevent the agglomeration of

the nanoparticles.The nanofluids are

prepared with different particle

concentration such as 0.1%, 0.2%, 0.3%

respectively. It is done to investigate the

effect of the nanoparticles concentration

on the heat transfer performance of the

nanofluids.

Fig.1 Schematic diagram of experimental

Setup

Twisted Tapes:

To develop flow hydro-dynamically,

twisted tapes are inserted in the heat transfer

test tube. The twisted tapes were tested in

experiments with twist ratio (y/D = 3.0) and

two different twists (Left twist and right twist)

with a clearance of 0.0357 mm. The schematic

figure of twisted tape insert is given in Fig. 2.

The twisted tapes are manufactured and fixed