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Hi 08 Utilities

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    Heat Integration UVa | Synthesis 08. Utilities 1

    HEAT INTEGRATION

    Synthesis

    8. Utilities

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    Heat Integration UVa | Synthesis 08. Utilities 2

    Outline

    Introduction

    Heating and Cooling

    Designing with composite curves

    Grand composite curve

    Common utility design

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    Heat Integration UVa | Synthesis 08. Utilities 3

    Introduction

    Utilities are the responsibility of the technical staff designing/retrofittingthe plant. One must:

    Select the most suitable type for energy utilities

    Select their levels (T, P)

    Dimensioning

    Each utility has its own characteristics:

    Mass, volume and energy flows ability (big turbines or small ORCs)

    Level variation pattern (isothermic, changing T...)

    Capacity to combine with other utilities

    ...that make it more suitable for some processes than for other

    Typical cases:

    Change a spoiled/damaged utility device (steam boiler)

    Plant revamping (modernize) or debottlenecking (enlargement)

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    4/19Heat Integration UVa | Synthesis 08. Utilities 4

    Heating

    Cooling water (with/without cooling tower) (sea water)

    Air Cooled Exchanger / Condenser

    Low-temperature ('sub-ambient') refrigeration

    Vapor-Compression / Vapor-Absorption

    BFW pre-heating / Combustion air pre-heating

    Steam generation (heat from process)

    Bottoming ORC (organic Rankine cycles) co-generation

    Steam (LP, MP, HP, VHP...)

    From a steam generator (boiler)

    From a heat recovery steam generator (engine/turbine)

    Steam generation through co-generation (turbine)

    Flue gases form a gas engine/turbine (topping)

    Thermal Fluid ('Oil') systems

    FurnacesHeat pumps

    and Cooling

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    5/19Heat Integration UVa | Synthesis 08. Utilities 5

    Heating and Cooling

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    6/19Heat Integration UVa | Synthesis 08. Utilities 6

    Objective: To select the utility or combination of utilities optimized for theproblem and fix their most suitable operating parameters and quantities

    Pinch analysis and H vs. T composite curves can be used:Example: introducing an intermediate level of steam:

    How much use from the new level? How do they affect original steam?

    Utility is an energy stream like the other (level, thermal inertia, duty)

    Increase until the appearance of a utility pinch

    Designing with composite curves

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    7/19Heat Integration UVa | Synthesis 08. Utilities 7

    Example: steam generation from BFW using process heat

    How much steam at given T can be generated from BFW at ambient T?

    This is a complex refrigeration utility:

    Until the appearance of a utility pinch (may appear in the preheating)

    Designing with composite curves

    q = m Cp TVTBFWHVAP

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    8/19Heat Integration UVa | Synthesis 08. Utilities 8

    Example: dimensioning a gas turbine co-generation

    What is the minimum mass flow of flue gases/fuel required for a process

    Until the appearance of a utility pinch

    Summary: the calculation of utilities is possible but not easy

    Designing with composite curves

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    9/19Heat Integration UVa | Synthesis 08. Utilities 9

    Grand composite curve

    Can be calculated by theproblem table algorithm

    Shows the energy profile of theproblem: where heat arises ordies away

    Incoming intervals:

    Heat flow decreases with T

    Enthalpy consumption regions

    Outgoing intervals:

    Heat flow increases with T

    Enthalpy consumption regions

    Utilities are well understoodwhen plotted on this diagram

    T* vs H diagram of heat cascade -heat flows across boundaries-

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    10/19Heat Integration UVa | Synthesis 08. Utilities 10

    Grand composite curve

    Represents the T vs. H characteristics of a problem, enthalpy flows orheat in excess for each temperature level

    Lets you easily visualize the pinch/es and quasi-pinch/es, and theheating and cooling requirements

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    11/19Heat Integration UVa | Synthesis 08. Utilities 11

    Grand composite curve

    The process heat exchanging with the surroundings utilities takesplace only at hot and cold ends (highest and lowest points H coord.)

    In re-entrant areas ('pockets')internal transfer can occursbetween heat-surplus andheat-deficit regions of theprocess (Tmin at least)

    If heat is taken from a pocketmust be restored later (colder)

    Also 'pseudo-utility' design

    Reactors

    Separation systems

    Turbines/engines

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    Heat Integration UVa | Synthesis 08. Utilities 12

    Grand composite curve

    Solving previous examples:

    Intermediate steam level

    Steam generation from BFW

    Co-generation minimumfuel mass flow

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    Heat Integration UVa | Synthesis 08. Utilities 13

    Common utility design Steam systems

    High temperatures, but critical point: Less carrying capacity / Too high P

    Usually several levels (LP, MP, HP, VHP...) for efficiency and cost

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    Heat Integration UVa | Synthesis 08. Utilities 14

    Common utility design Steam systems

    Minimize level temperature

    Maximize flows at lowlevels (normally)

    Complexity increases withthe number of levels

    Different alternatives /setscan be easily explored

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    Heat Integration UVa | Synthesis 08. Utilities 15

    Common utility design Furnaces (simple)

    Used in cases of very high temperature or large duties

    Very complex utility; here a simplified model

    Flue gases loosingheat linearly (mCp)from adiabatic flameT to stack T

    Real T < Flame T(radical formation,excess air)

    Stack T limited by:

    Acid condensationUtility pinch

    GCC informs onwaste heat

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    Heat Integration UVa | Synthesis 08. Utilities 16

    Common utility design Thermal oil

    Heat transfer from liquids at high temperature (not constant)

    Seeks to reduce the flow by reducing the final T

    Initial T fixed by oil

    or process stabilityfinal T limited by:

    Process pinch

    Utility pinch

    C ili d i S b bi C li

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    Heat Integration UVa | Synthesis 08. Utilities 17

    Common utility design Sub-ambient Cooling

    Vapor-Compression / Absorption generation of a liquid refrigerant

    (Constant T boiling) or (mixed refrigerant) heat removal

    Several P/T levels tomaximize efficiency

    Very complex

    designs

    Heat leaks fromoutside to inside

    High cost (shaft

    work, mechanical orelectrical):minimizing shaft

    work, no heat flow

    C tilit d i C li t

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    Heat Integration UVa | Synthesis 08. Utilities 18

    Common utility design Cooling water

    Air-cooled exchangers and combustion air pre-heating are similar

    Mass flow andtemperatures

    Cooling towerdimensioning

    Sea water:pumping rates

    H t d Th l E i

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    Heat Integration UVa | Synthesis 08. Utilities 19

    Heat pumps and Thermal Engines

    Heat pumps:

    The smaller the differencein temperature, the better

    'Big nose' processHeat output = heat input +shaft work (1st principle)

    Difficulty in placing:

    Topping cycle (gas turbine): rendering heat output above the pinch

    Bottoming cycle (ORC): taking heat input from bellow the pinch

    Heat pump:

    Taking heat from bellow the pinch

    Rendering heat above the pinch


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