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主题标题: Heat Exchanger Calc.: Typical U value; TYPICAL FOULING FACTORS [简洁模式]
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    帖子一览:Heat Exchanger Calc.: Typical U value; TYPICAL FOULING FACTORS (新回复在最前,最多列出 6 个)  [列出所有回复]
    Shaw 发表于: 2005/02/07 02:10am
    有用,但很难记住。文字文字
     
    max123 发表于: 2005/02/07 01:32am
    http://www.engineeringpage.com/info/he/HEside.html

    FLUID ALLOCATION: CHOICE BETWEEN SHELL OR TUBE SIDE

    Introduction
    The choice of the allocation of the fluid to the shell side or tube side can have a significant impact on the performance, economics and maintainability of a heat exchanger. For most design work a balanced decision is required as the considerations can lead to opposite preferences. Some general guidelines are provided underneath:

    Fouling
    There are many mechanisms of fouling. Allocating the most fouling fluid to the tube side will be more favourable as mechanical cleaning of the inside of the tubes wil be much easier. As the allowable velocity in the tubes is usually higher than at the shell side and a high fluid velocity causes attrition of the deposits, it is possible to reduce fouling by design.

    Mechanical Design Pressure
    It will be more econamical to put the medium with the highest maximum allowable working pressure at the tube side. If the shell side needs to be designed for a high pressure the wall thickness will increase making the heat exchanger more expensive.

    Corrosion
    If you need an expensive corrosion resistant material it will be more economical to place the corrosive fluid in the tubes as this will reduce the costs of the shell material or cladding.

    High Viscosity or Low Flowrates
    To obtain an economic design high heat transfer coefficients are required. As heat transfer coefficients are much higher for turbulent flow this is the most important aspect to look into. For a highly viscous medium or a low flowrate turbulent flow can be obtained easier at the shell side. If the Reynolds number at the shell side is below 200, however, it will probably be cheaper to allocate this fluid to the tube side and use a high number of tube passes.
    Use the thermal rating calculation routine to do trial and error runs and get an economical design.

     
    max123 发表于: 2005/02/07 01:29am
    TYPICAL FOULING FACTORS:

    COOLING WATER - Fouling Factors in [m2K/W]
    Conditions cooling water < 50 ° C
    cooled fluid < 120 ° C cooling water > 50 ° C
    cooled fluid > 120 ° C
    Water velocity v < 1 m/s          v > 1 m/s          v < 1 m/s          v > 1 m/s          
     
    Type of Water
    Sea 0.00009 0.00009 0.00018 0.00018
    Brackish 0.00035 0.00018 0.00053 0.00035
    Cooling tower with inhibitor 0.00018 0.00018 0.00035 0.00035
    Cooling tower without inhibitor    0.00053 0.00053 0.00088 0.00070
    City grid 0.00018 0.00018 0.00035 0.00035
    River mimimum 0.00018 0.00018 0.00035 0.00035
    River average 0.00053 0.00035 0.00070 0.00035
    Engine jacket 0.00018 0.00018 0.00018 0.00018
    Demineralized or distilled 0.00009 0.00009 0.00009 0.00009
    Treated Boiler Feedwater 0.00018 0.00009 0.00018 0.00018
    Boiler blowdown 0.00035 0.00035 0.00035 0.00035

    --------------------------------------------------------------------------------

    SEVERAL FLUIDS - Fouling Factors in [m2K/W]
    Group       Fluid       Fouling Factor
    Oil Gasoil 0.00009
    Transformer 0.00018
    Lubrication 0.00018
    Heat Transfer oil 0.00018
    Hydraulic 0.00018
     
    Gas and Vapour      Hydrogen 0.00176
    Engine exhaust 0.00176
    Steam 0.00009
    Steam with oiltraces 0.00018
    Cooling fluid vapours with oil traces       0.00035
    Organic solvent vapours 0.00018
    Compressed air 0.00035
    Natural gas 0.00018
    Stable top products 0.00018
     
    Liquid      Cooling Fluid 0.00018
    Organic heat transfer fluids 0.00018
    Salts 0.00009
    LPG, LNG 0.00018
    MEA and DEA (Amines) solutions 0.00035
    DEG and TEG (Glycols) solutions 0.00035
    Stable side products 0.00018
    Stable bottom products 0.00018
    Caustics 0.00035
    Vegetable Oils 0.00053

    --------------------------------------------------------------------------------

    REFINERY FLUIDS - Fouling Factors in [m2K/W]
    Crude - wet,
    (bearing salty water)  
    Temperature 0 to 95 ° C 95 to 160 ° C 160 to 260 ° C > 95 ° C
    Velocity
    < 0.6 m/s       0.00053     0.00088      0.00105     0.00123    
    0.6 m/s to 1.2 m/s       0.00035 0.00070 0.00088 0.00106
    > 1.2 m/s       0.00035 0.00070 0.00070 0.00088
     
    Crude - dry  
    Temperature 0 to 95 ° C 95 to 160 ° C 160 to 260 ° C > 95 ° C
    Velocity
    < 0.6 m/s       0.00053     0.00053      0.00070     0.00088    
    0.6 m/s to 1.2 m/s       0.00035 0.00035 0.00053 0.00070
    > 1.2 m/s       0.00035 0.00035 0.00035 0.00053
     
    Products Gasoline 0.00018
    Naphtha and Light Distillates 0.00018
    Kerosene 0.00018
    Light gas oil 0.00035
    Heavy gas oil 0.00053
    Heavy fuel oils 0.00088
    Asphalt and residuum 0.00176
     
    Cracking and
    Coking Units streams Overhead vapors 0.00035
    Light cycle oil 0.00035
    Heavy cycle oil 0.00053
    Light coker gas oil 0.00053
    Heavy coker gas oil 0.00070
    Bottom slurry (> 1.5 m/s) 0.00053
    Bottom liquid products 0.00035
     
    Catalytic Reforming,
    Hydrocracking,
    Hydrodesulfurization (HDS) Reformer charge 0.00035
    Reformer effluent 0.00018
    Hydrocracker charge and effluent 0.00035
    Recycle gas 0.00018
    HDS charge and effluent 0.00035
    Overhead vapors 0.00018
    Liquid product > 50 API 0.00018
    Liquid product 30 to 50 API 0.00035
     
    Light Ends
    processing streams Overhead vapors and gases 0.00018
    Liquid products 0.00018
    Absorption oils 0.00035
    Alkylation trace acid streams 0.00053
    Reboiler streams 0.00053
    Lube oil processing streams 0.00053
    Feed stock 0.00035
    Solvent feed mix 0.00035
    Solvent 0.00018
    Extract 0.00035
    Raffinate 0.00018
    Asphalt 0.00088
    Wax slurries 0.00053
    Refined lube oil 0.00018

     
    max123 发表于: 2005/02/07 01:28am
    http://www.engineeringpage.com/info/he/typU.html

    TYPICAL OVERALL HEAT TRANSFER COEFFICIENTS (U - valueS)


    Shell and Tube Heat Exchangers     Hot Fluid Cold Fluid U [W/m2C]

    --------------------------------------------------------------------------------

    Heat Exchangers Water Water 800 - 1500
    Organic solvents    Organic Solvents    100 - 300
    Light oils Light oils 100 - 400
    Heavy oils Heavy oils 50 - 300
    Reduced crude Flashed crude 35 - 150
    Regenerated DEA Foul DEA 450 - 650
    Gases (p = atm) Gases (p = atm) 5 - 35
    Gases (p = 200 bar) Gases (p = 200 bar) 100 - 300
       
    Coolers Organic solvents Water 250 - 750
    Light oils Water 350 - 700
    Heavy oils Water 60 - 300
    Reduced crude Water 75 - 200
    Gases (p = atm) Water 5 - 35
    Gases (p = 200 bar)  Water 150 - 400
    Gases Water 20 - 300
    Organic solvents Brine 150 - 500
    Water Brine 600 - 1200
    Gases Brine 15 - 250
       
    Heaters Steam Water 1500 - 4000
    Steam Organic solvents 500 - 1000
    Steam Light oils 300 - 900
    Steam Heavy oils 60 - 450
    Steam Gases 30 - 300
    Heat Transfer (hot) Oil Heavy oils 50 - 300
    Heat Transfer (hot) Oil Gases 20 - 200
    Flue gases Steam 30 - 100
    Flue gases Hydrocarbon vapours 30 -100
       
    Condensers Aqueouos vapours Water 1000 - 1500
    Organic vapours Water 700 - 1000
    Refinery hydrocarbons Water 400 - 550
    Vapours with some non condensibles Water 500 - 700
    Vacuum condensers Water 200 - 500
       
    Vaporisers  
    Steam Aqueouos solutions 1000 - 1500
    Steam Light organics 900 - 1200
    Steam Heavy organics 600 - 900
    Heat Transfer (hot) oil Refinery hydrocarbons 250 - 550

    --------------------------------------------------------------------------------

     
     
    Air Cooled Exchangers Process Fluid  U [W/m2C]

    --------------------------------------------------------------------------------

    Water  300 - 450
    Light organics  300 - 700
    Heavy organics  50 - 150
    Gases  50 - 300
    Condensing hydrocarbons  300 - 600

    --------------------------------------------------------------------------------

       
       
    Immersed coils Coil Pool U [W/m2C]

    --------------------------------------------------------------------------------

    Natural circulation Steam Dilute aqueouos solutions 500 - 1000
    Steam Light oils 200 - 300
    Steam Heavy oils 70 - 150
    Aqueouos solutions Water 200 - 500
    Light oils Water 100 - 150
       
    Agitated Steam Dilute aqueouos solutions 800 - 1500
    Steam Light oils 300 - 500
    Steam Heavy oils 200 - 400
    Aqueouos solutions Water 400 - 700
    Light oils Water 200 - 300

    --------------------------------------------------------------------------------

       
       
    Jacketed vessels Jacket Vessel U [W/m2C]

    --------------------------------------------------------------------------------

    Steam Dilute aqueouos solutions 500 - 700
    Steam Light organics 250 - 500
    Water Dilute aqueouos solutions 200 - 500
    Water Light organics 200 - 300

     


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