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1 418 Heat Exchangers

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    HEAT EXCHANGERS

    Dr. Ali K. Abdel-RahmanM echani cal Engineer ing Depar tment

    F acul ty of Engineer ing

    Assiut Universi ty

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    OUTLINE

    Definition & classification of heat exchangers

    Heat exchangers according to construction Plate heat exchangers Extended surface heat exchangers Tubular heat exchangers

    Heat exchangers according to phase change Condensers Evaporators

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    WHAT IS A HEAT EXCHANGER?

    They are devices specially designed for the efficienttransfer of heat from one fluid to another fluid over

    a solid surface.

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    WHAT ARE HEAT EXCHANGERSUSED FOR?

    They have the function to transfer heat asefficiently as possible. Heat exchangersare widely used in :

    I. refrigerationII. air conditioning

    III. space heatingIV. electricity generationV. chemical processing

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    CLASSIFICATION OF HEAT

    EXCHANGERS

    Heat exchangers may be classifiedaccording to the following main criteria:

    Recuperators and regenerators Transfer processes: direct contact and indirect

    contact Geometry of constructions: tubes, plates and

    extended surfaces Phase change mechanisms: condensers andevaporators

    Flow arrangements: parallel, counter and cross flow

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    RECUPERATORS

    The conventional heat exchangers with heattransfer between two fluids.

    Hot stream A recovers some of the heat from

    stream B.

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    REGENERATORS

    Storage type heat exchangers.The same flow passage (matrix) is alternatelyoccupied by one of the two fluids.

    Thermal energy is not transfered through the wall.

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    TRANSFER PROCESSES

    Heat transfer between the cold

    and hot fluidsthrough a directcontact betweenthese fluids.

    Examples: Spray andtray condensers,cooling towers.

    1. Direct contact type heat exchangers:

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    2. I ndirect contact type heat exchangers :

    Heat energy isexchanged between

    hot and cold fluidsthrough a heattransfer surface.

    The fluids are notmixed.

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    FLOW ARRANGEMENTS

    1. Paralel F low H eat Exchangers:

    Two fluid streams enter together at one end,flow through in the same direction, and leavethrough at the other end.

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    2. Counter F low H eat Exchangers:

    Two fluid streams flow in opposite directions.

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    3. Cross Flow Heat Exchangers:

    The direction of fluids are perpendicular to eachother.

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    BASIC CRITERIAS FOR THE

    SELECTION OF HEAT EXCHANGERS Process specificationsService conditions of the plant environment,resistance to corrosion by the processMaintenance, permission to cleaning andreplacement of componentsCost- EffectivenessSite requirements, lifting, servicing,capabilities

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    PLATE HEAT

    EXCHANCERS

    GASKETED PLATE SPIRAL PLATE LAMELLA

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    Limited to below 25 bar

    and 250C. Plate heat exchangers

    have three main types :gasketed, spiral heatexchangers and lamella.

    The most common of the plate-type heatexchangers is thegasketed plate heatexchanger.

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    GASKETED PLATE HEAT

    EXCHANGER The most common of

    the plate-type heatexchangers is thegasketed plate heat

    exchanger.

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    SPIRAL PLATE HEAT

    EXCHANGER

    Ideal flow conditions and the smallest possible heating surface.

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    LAMELLA

    Consisting of cylindrical

    shell surrounding a numberof heat transfering lamellas. Similar to tubular heat

    exchanger.

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    ADVANTAGES

    Plate heat exchangers yield heat transfer ratesthree to five times greater than other types of heatexchangers.

    The design of the plate heat exchanger allows toadd or remove plates to optimize performance, orto allow for cleaning, service, or maintenancewith a minimum of downtime.

    Plate exchangers offer the highest efficiencymechanism for heat transfer available in industry.

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    DISADVANTAGES

    Plate exchangers are limited when high pressures, high temperatures, or aggressivefluids are present.

    Because of this problem these type of heatexchangers have only been used in small, low

    pressure applications such as on oil coolers forengines.

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    2. EXTENDED SURFACE

    HEAT EXCHANGERS

    - PLATE FIN HEAT EXCHANGER- TUBE FIN HEAT EXCHANGER

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    PLATE FIN HEAT

    EXCHANGER For gas to gasapplications.

    Widely used incryogenic, energyrecovery, processindustry, refrigerationand air coditioningsystems.

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    TUBE FIN HEATEXCAHNGER

    For gas to liquid heatexchangers.

    Used as condersers inelectric power plant, asoil coolers in propulsive

    power plants, as ircooled exchangers in

    process and powerindustires.

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    TUBULAR HEAT EXCHANGERS

    SHELL AND TUBE

    DOUBLE-PIPE

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    SHELL AND TUBE HEATEXCHANGERS

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    SHELL AND TUBE HEATEXCHANGERS

    Are the most commonlyused heat exchangers in oilrefineries and other largechemical processes.

    Are used when a process

    requires large amounts offluid to be heated orcooled.

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    SHELL AND TUBE HEATEXCHANGERS

    Provide transfer of heatefficiently.

    Use baffles on the shell-side fluid to accomplishedmixing or turbulence.

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    SHELL AND TUBE HEAT EXCHANGERS

    U - TUBE HEAT EXCHANGERS

    FIXED TUBE HEAT EXCHANGERS

    FLOATING HEAD HEAT EXCHANGERS

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    U - TUBE HEAT EXCHANGERS Heat exchanger systems consisting of straight

    length tubes bent into a U-shape surrounded by a shell.

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    U - TUBE HEAT EXCHANGERS

    Both initial and maintenance costs are reduced by reducing the number of joints.

    They have drawbacks like inability to replaceindividual tubes except in the outer row andinability to clean around the bend.

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    U - TUBE HEAT EXCHANGERS

    Examples: reboilers, evaporators and Kettletype.

    They have enlarged shell sections for vapor-liquid separation.

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    FIXED TUBE HEAT EXCHANGERS

    Have straight tubes that are secured at bothends to tube sheets welded to the shell.

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    FIXED TUBE HEAT EXCHANGERS

    They are the most economical type design. They have very popular version as the heads

    can be removed to clean the inside of thetubes.

    Cleaning the outside surface of the tubes is

    impossible as these are inside the fixed part. Chemical cleaning can be used.

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    FLOATING HEAD HEAT EXCHANGERS

    Examples : kettle boilers which have dirtyheating medium.

    They have the most highest construction cost of

    all exchanger types.

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    DOUBLE-PIPE HEAT EXCHANGERS

    Utilize true counter-current flow which

    maximizes the temperature differences

    between the shell side and tube side fluids.

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    When the process callsfor a temperature cross,

    it is the most efficientdesign and will result infewer sections and lesssurface area.

    DOUBLE-PIPE HEAT EXCHANGERS

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    DOUBLE-PIPE HEAT EXCHANGERS

    ADVANTAGES

    Operates in true counter current flow permittingextreme temperature cross.

    Economically adaptable to service differentials. Ideal for wide temperature ranges and

    differentials. Provides shorter deliveries than shell and tube

    due to standardization of design andconstruction.

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    1)REBOILER to generate vapor to drive fractional distillationseparation

    Most Common Reboiler s Types Kettle Reboilers Forced Recirculation ReboilersThermosiphon Reboiler

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    Kettle Reboilers

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    Major factors influence reboiler typeselection:

    Plot space available

    Total duty required

    Fraction of tower liquid traffic vaporized

    Fouling tendency

    Temperature approach available

    Temperature approach required

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    Kettle Reboilers

    AdvantagesInsensitive tohydrodynamicsHigh heat fluxes are

    possibleCan handle highvaporization

    Simple pipingUnlimited area

    DisadvantagesAll the dirt collects andnon volatilesaccumulateShell side is difficult tocleanDifficult to determinethe degree of mixingOversize shell isexpensive

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    Thermosiphon Reboiler

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    Thermosiphon Reboiler

    operate using natural circulation with processflow on the shell side

    process flow on the tube or shell side invertical units.not require a pump for recirculationhave sensible heat transfer followed bynucleate boiling.

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    F orced Recirculation Reboilers

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    F orced Recirculation Reboilers

    These reboiler types have two mechanismsof heat transfer: sensible heat transfer

    followed by nucleate boiling.

    Process flow is typically on the tube side of

    a standard exchanger in the vertical position.

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    2)CONDENSERS

    a) Water-CooledCondensensersHorizontal shell andtubeVertical shell andtubeShell and coilDouble pipe

    b) Air- CooledCondensers

    Phases:1) de-super-heating

    2) Condensing3) Subcooling

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    Single-Pass Condenser

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    SELECT AN WATER-COOLED

    CONDENSER IF:

    1. Adequate water supplies are available from tower, city or well sources.2. Water supply is of good quality.3. Heat recovery is not practical or unimportant.4. Plant ambient temperatures consistently exceed 95F.5. Ambient air is polluted with large dust and dirt particles.

    ADVANTAGE & DISADVANTAGES

    1. Offer lower capital investment.2. Operates more efficiently on hot summer days.3. Easier to operate.4. Does not offer summer ventilation.

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    OUTLINE

    Definition & classification of heat exchangers

    Heat exchangers according to construction Plate heat exchangers Extended surface heat exchangers Tubular heat exchangers

    Heat exchangers according to phase change Condensers Evaporators

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