Construction Of Shell And Tube Heat Exchanger

7 Chapters
|
45 Pages
|
5,507 Words

A shell and tube heat exchanger is a fundamental component in various industrial processes, facilitating the efficient transfer of heat between two fluid streams while ensuring separation to prevent contamination. Its design encompasses a cylindrical shell housing multiple tubes, typically made of materials like stainless steel or copper, arranged in a bundle configuration. One fluid, termed the “tube-side” fluid, flows through the interior of the tubes, while the other, known as the “shell-side” fluid, circulates around the tubes within the shell. This arrangement maximizes surface area contact between the fluids, enhancing heat transfer efficiency. The heat exchange process occurs through conduction across the tube walls, with fluid flow rates, temperatures, and thermophysical properties influencing heat transfer performance. Various design parameters such as tube diameter, length, and arrangement, as well as shell diameter, baffle spacing, and tube layout, are optimized to meet specific operational requirements and thermal performance objectives. Additionally, considerations for maintenance, pressure drop, fouling, and corrosion resistance play pivotal roles in the design process, ensuring longevity and reliability in diverse industrial applications such as power generation, chemical processing, and HVAC systems.

ABSTRACT

The aim of this project was to construct shell and tube heat exchanger with fixed boundless. A heat exchanger that would cool 5 x 5 x 10 – 3 kg/s of steam at a calculated heat load of 152 – 395/S was fabricated. The steam is to reach the heat exchanger from a distillation column at a temperature of 300k. The specification of the layout as well as the detailed mechanical design were assumed and also calculated.
It is established that a horizontal heat exchanger with cold water at the shall side and the treated steam at the tube side is adequate for this operation, with the aim of cooling the steam from the distillation column.
The available area obtained from calculation is 1.0m2 and also the overall heat transfer coefficient obtained is 4.10W/M2k. it is also seen that the heat exchanger is satisfactory and consists of five copper tubes of inside diameter 90mm and 5920mm length. The shell inside diameter 810mm and 5.770mm length. The tube and shell heat exchanger has a total length of 5820mm.
The material of construction for the shell side is stainless steel while copper tubes were used for the tubes inside.
The total cost of the heat exchanger was N12,000.

TABLE OF CONTENT

Title Page
Approval page
Letter of transmitted
Dedication
Acknowledgements
Abstract
Table of contents

CHAPTER ONE
1.1 Introduction

CHAPTER TWO
2.0 Literature Review
2.1 General Design of Heat Exchanger
2.2 Tubular Heat Exchanger
2.3 Design Description of the Major Components
2.4 Tubes
2.5 Tube Bundles
2.6 Shells
2.7 Baffle
2.8 Tie Road Spacers
2.9 Pass Partition Plates

CHAPTER THREE
3.0 Fabrication Procedures
3.1 Dimensioning and Marking Out
3.2 Cutting
3.3 Folding or Rolling
3.4 Drilling operation
3.5 Assembling Process
3.6 Welding Operation
3.7 Filling
3.8 Dimensions and Parameters Derived
3.9 From the Fabrication Units

CHAPTER FOUR
4.0 Costing

CHAPTER FIVE
5.0 Discussion

CHAPTER SIX
6.0 Conclusion
6.1 Recommendations

CHAPTER SEVEN
7.0 Notation and Nomenclature
References
Appendix
Physical Properties of Water
Calculation of the Head Load

 

CHAPTER ONE

INTRODUCTION
In large industrial processes, it is necessary to transfer heat between the system and its surrounding and the device whose primary objective to do it efficiently and effectively is the heat exchanger.
Therefore heat transfer is defined as the rate of exchange of heat between one body (hot) and another cold.
The most important aim in the chemical engineering sector of any plant is to control the flow of thermal energy between two terminals. It there existing temperature gradient of change.
In industrial process, the heat exchange is a very important unit in all the processing industries that their design has been highly developed. Designers of heat exchanger must be constantly aware of the difference between the idealized conditions for and under which basic knowledge was obtained and the real conditions of the mechanical expressions of their design and it’s environment.
The design must satisfy process operational requirement such as availability and maintainability.
Heat transfer or thermo-kinetics is another chapter of the theoretical fundamentals of heat engineering dealing with the processes of heat propagation. In nature and engineering, the most diverce process of heat propagation are observed and also heat flow from bodies (or their section) of a lower temperature. During the process of heat transfer, from one body to another heat flow continues till their temperature became equal be come to equilibrium state of temperature.

MODES OF HEAT TRANSFER
Heat is transferred by conduction, convection and thermal radiation. In practice, heat is usually transmitted by two or all the three modes of heat transfer concurrently.

CONDUCTION
Heat conduction of simply conduction is the transfer of heat by a direct contact between the elementary particles of a body, Viz molecules, atoms, free electrons, when the bodies involved are at rest.
Pure conduction takes place in opaque or non transpired solid.
In goses, conduction occurs due to random motion of the molecules (the diffuse from high concentration region to lower region. In this made of heat transfer, it is very common with metals and thus call for high thermal conductivity. Also the heat transfer per unit area is proportional to normal temperature gradient given as:
Q = dt = (1)
A dx
Fourier postulated an expression for heat transferred by conduction called fouriers law gives by:
Q = KA dt = (2)
Dx
Where Q rate of flow of heat J/S or welts
K = Fourier’s constant
A = Area of heat transfer perpendicular to the direction of heat flow (M2).
dt/dx temperature gradient (0C or K ).

CONVECTION
This involves the transfer of heat from one body to another by the mobile particles of liquid, gas or coarse solids during their relative motion in space. Convection heat transfer can be illustrated by the transfer of heat by heated air from a stove to the upper layers of the room air. Convection consist of forced and natural convection. Forced convection is widely used in chemical processing industries. The expression below shows heat transfer by convection.
Q = KA (Ti – To) = (3)
= hA (Ti – To) = (4)
where h k/x
Q = heat transfer rate J/S or welts
K = Proportionality constant
X = Distance over which heat is transferred (m)
A = Area (M2)
Ti and To = Temperature at different point (0C or K)
h = Convection heat transfer co-efficient (w/m2k)

RADIATION
This is a process of heat transferred by electromagnetic waves through a machines which is transparent to thermal radiation. During this process, a fraction of the thermal energy of a hot body is converted into radiant energy which, when encountering an opaque body again turns partly into heat.
From the second law of thermodynamics, STEFANBOLTZ MANU prop
Proposed that heat is directly proportional to the fourth power of the temperature and the surface area.
Thus given as:
Q = AT – 4 = (5)
Where  = Stefan – Boltman constant
 = Emissivity surface
T = Absolute temperature (0C or K)
A = Area of heat transfer (M2)
Q = Heat transfer rate J/S or welt
HEAT TRANSFER EQUIPMENT
There are various types of heat exchange equipment generally defined by the function it performs in a chemical industry. Generally, heat exchange is the equipment whose primary objective is to transfer heat energy between two fluids. These equipment are classified into three categories mainly:-
(a) Regenerators
(b) Open type heat exchangers and
(c) Closed type bread exchanger or recuperations

a. REGENERATORS
These are heat exchangers in which the hot and cold fluid flow through the same space alternatively with a little physical mixing as possible occurring between the two streams. The amount of heat transferred depends on the fluid and flow properties of the fluid streams as well as the geometry and thermal properties of the surface.

b. OPEN TYPE HEAT EXCHANGERS
These are devices where by fluid stream flow into an open chamber and there the complete mixing occurs. Hot and cold fluid enter the exchanger separately and will at the other end leaves as single fluid stream.

c. RECUPERATORS OR CLOSED TYPE HEAT EXCHANGERS
They are those in which the heat transfer occurs between the two fluid stream that do not physical contact each other. The fluid streams involved are separated from one another by a tube wall or a pipe. Heat transfer occurs by convection from the hot fluid to the solid surface, by conduction through the solid surface and then by convection through solid surface to the cooler fluid.
Another classification is based on relative flow direction of the two fluid streams. They include:-
i. Parallel Flow: When the fluid stream flow in the same direction.
ii. Counter Current Flow: The fluid streams flow in opposite direction.
iii. Cross Flow: If the fluid stream flow at right angle to one another.
The other classification is based on tube construction:-
i. Double – pipe heat exchanger
ii. Shell and tube heat exchanger
iii. Extended – surface exchangers
iv. Spiral plate exchanger
v. Graphic block heat exchangers
vi. Scrap surface exchanger.

 

 

 

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Construction Of Shell And Tube Heat Exchanger:

A shell and tube heat exchanger is a widely used type of heat exchanger in various industrial applications for transferring heat from one fluid to another. It consists of a shell (outer vessel) and a series of tubes (inner vessels) through which the fluids flow. The basic construction of a shell and tube heat exchanger involves several key components and steps:

Shell: The shell is the outer cylindrical or rectangular vessel that houses the tubes and serves as the primary containment for one of the fluids. The shell is typically made of materials like carbon steel, stainless steel, or other corrosion-resistant alloys to withstand the operating conditions and prevent leakage.

Tubes: Tubes are the inner vessels through which the fluids flow. They are usually arranged in a bundle within the shell. Tubes are made from materials compatible with the fluids being processed, often materials like copper, brass, stainless steel, or other alloys. The number, size, and arrangement of tubes depend on the specific design and requirements of the heat exchanger.

Tube Sheets: At both ends of the shell, tube sheets are installed to support and secure the tubes. Tube sheets are usually thick metal plates with holes drilled or machined to precisely fit the tubes. The tubes are expanded or mechanically attached to the tube sheets to ensure a tight seal and efficient heat transfer.

Baffles: Baffles are placed inside the shell to direct the flow of the fluid and improve heat transfer efficiency. They create a turbulent flow pattern, which enhances heat transfer between the fluids. Baffles can take various forms, such as perforated plates, segmental rings, or spiral strips.

Tube Passes: Shell and tube heat exchangers can have multiple tube passes, which refer to the number of times a fluid flows through the tubes before exiting the heat exchanger. Each pass contributes to increased heat transfer. The arrangement of tube passes can be parallel or in a series, depending on the design.

Inlet and Outlet Connections: The heat exchanger has inlet and outlet connections for both the hot and cold fluids. These connections are typically located on the shell and are used for fluid entry and exit. Flanges, pipes, or other connectors are used to join the heat exchanger to the fluid circulation system.

Supports: Shell and tube heat exchangers are often supported by a structural framework to ensure stability and prevent damage or misalignment during operation. The support structure may include brackets, beams, or legs.

Insulation and Casing: To minimize heat loss and improve safety, the heat exchanger may be insulated. Insulation materials like fiberglass or mineral wool are applied around the shell, and a protective casing may be added to shield the insulation and maintain a clean appearance.

Access Ports and Manholes: Access ports and manholes may be provided for inspection, cleaning, and maintenance purposes. These openings allow technicians to access the interior of the heat exchanger without dismantling it completely.

The construction and design of shell and tube heat exchangers can vary widely based on factors such as the type of fluids being processed, temperature and pressure requirements, and the specific application. Detailed engineering and manufacturing standards must be followed to ensure the heat exchanger’s safety, efficiency, and reliability in its intended operating conditions.