tema specification sheet

1
0 423,98 685 C - general service Flat Metal Jacket Fibe ASME Code Sec VIII Div 1 - - Single segmental Carbon Steel Carbon Steel Exp. - mm IZMJENJIVAČ TOPLINE DIMNI PLINOVI IZGARANJA - VODA 488 1650 AFL 1 1 28,6 1 28,6 VODA DIMNI PLINOVI 2,8133 0,8203 kg/s 0 0 kg/s 0,8203 0,8203 2,8133 2,8133 kg/s 0 0 kg/s 0 15 90 °C 950 115,12 °C kg/ml 0,32 0,94 mPa s 32,8 32,8 kJ/(kg K) W/(m K) kJ/kg 2,5 0,993 bar 0,15 92,3 m/s 0,5 0,03325 bar 0,2 0,06839 0,0004 0,0002 m˛ K/W kW 913,6 °C 372,81 85,6 94,2 W/(m˛ K) 100,4 bar 3 125 985 °C 2 2 1,59 1,59 mm 203,1 - 41,1 - 125,5 - - - mm 1230 1598,9 kg 659,2 1717 44 kg/(m s˛) 45 41,55 mm mm 312 23,81 19,05 2 1650 mm mm mm Plain Carbon Steel 30 mm 508 Hastelloy C Hastelloy C - None - Hastelloy C - Carbon Steel Hor V Avg - 488 0 0 2,46675 0,92461 3 999,01 964,93 0,0458 0,0154 1,136 0,3113 1,492 1,132 4,316 4,375 0,0859 0,0257 0,5965 0,6774 T1 T2 S1 S2 0,00025 #/m ID 52,3 - 1 1 1 1 None Size/rating Ao based Vapor/Liquid -- Remarks TEMA class Intermediate Bundle Filled with water Weight/Shell Code requirements Floating head Tube Side Gaskets - Shell side Bundle exit Bundle entrance Type Expansion joint Tube-tubesheet joint Bypass seal Type U-bend Supports-tube Impingement protection Tubesheet-floating Channel cover Floating head cover Tubesheet-stationary Channel or bonnet Out In Surf/shell (eff.) Shells/unit Surf/unit(eff.) series parallel Connected in Type Size OD Sketch 1 2 3 4 5 6 7 PERFORMANCE OF ONE UNIT 8 Fluid allocation 9 Fluid name 10 Fluid quantity, Total 11 Vapor (In/Out) 12 Liquid 13 Noncondensable 14 Temperature (In/Out) 15 Dew / Bubble point 16 17 18 19 20 21 22 23 24 25 26 27 28 Heat exchanged 29 Transfer rate, Service 30 CONSTRUCTION OF ONE SHELL 31 Design/vac/test pressure:g 32 Design temperature 33 Number passes per shell 34 Corrosion allowance 35 Connections 36 37 38 Tube No. 39 Tks- 40 41 Length 42 Pitch 43 Tube type 44 Material 45 Shell 46 ID 47 OD 48 Shell Side 49 Tube Side 50 Shell cover 51 Tube pattern 52 Baffle-crossing 53 Type 54 Cut(%d) 55 Spacing: c/c 56 Baffle-long 57 Seal type 58 Inlet RhoV2-Inlet nozzle Shell Side Tube Side Fouling resist. (min) Pressure drop, allow./calc. Velocity Pressure (abs) Latent heat Thermal conductivity Specific heat Molecular wt, NC Molecular wt, Vap Viscosity Density MTD corrected Dirty Clean Heat Exchanger Specification Sheet

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Heat exchanger specification

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  • 0

    423,98

    685

    C - general service

    Flat Metal Jacket Fibe

    ASME Code Sec VIII Div 1

    -

    -

    Single segmentalCarbon Steel

    Carbon Steel

    Exp.

    -

    mm

    IZMJENJIVA TOPLINE DIMNI PLINOVI IZGARANJA - VODA

    488 1650 AFL 1 1

    28,6 m 1 28,6 m

    VODA DIMNI PLINOVI

    2,8133 0,8203kg/s

    0 0kg/s 0,8203 0,8203

    2,8133 2,8133kg/s 0 0

    kg/s 0

    15 90C 950 115,12

    C

    kg/m 0,32 0,94

    mPa s

    32,8 32,8

    kJ/(kg K)

    W/(m K)

    kJ/kg

    2,5 0,993bar

    0,15 92,3m/s

    0,5 0,03325bar 0,2 0,06839

    0,0004 0,0002m K/W

    kW913,6 C372,81

    85,6 94,2 W/(m K)100,4

    bar 3

    125 985C

    2 2

    1,59 1,59mm

    203,1 -41,1 - 125,5 -

    - -

    mm

    1230 1598,9 kg659,2

    1717 44 kg/(m s)45

    41,55mm

    mm

    312 23,8119,05 2 1650mm mm mm

    Plain Carbon Steel 30

    mm508

    Hastelloy C

    Hastelloy C

    - None

    -

    Hastelloy C

    -

    Carbon Steel

    Hor

    V

    Avg

    -

    488

    0 0

    2,46675 0,92461

    3

    999,01 964,93

    0,0458 0,01541,136 0,3113

    1,492 1,1324,316 4,375

    0,0859 0,02570,5965 0,6774

    T1

    T2 S1

    S2

    0,00025

    #/m

    ID

    52,3 -1

    1

    1

    1

    None

    Size/rating

    Ao based

    Vapor/Liquid

    --

    Remarks

    TEMA class

    Intermediate

    BundleFilled with waterWeight/Shell

    Code requirements

    Floating head

    Tube SideGaskets - Shell side

    Bundle exitBundle entrance

    TypeExpansion joint

    Tube-tubesheet jointBypass seal

    TypeU-bendSupports-tube

    Impingement protection

    Tubesheet-floating

    Channel cover

    Floating head cover

    Tubesheet-stationary

    Channel or bonnet

    Out

    In

    Surf/shell (eff.)Shells/unitSurf/unit(eff.)

    seriesparallelConnected inTypeSize

    OD

    Sketch

    1

    2

    3

    4

    5

    6

    7

    PERFORMANCE OF ONE UNIT8

    Fluid allocation9

    Fluid name10

    Fluid quantity, Total11

    Vapor (In/Out)12

    Liquid13

    Noncondensable14

    Temperature (In/Out)

    15

    Dew / Bubble point

    16

    17

    18

    19

    20

    21

    22

    23

    24

    25

    26

    27

    28

    Heat exchanged29

    Transfer rate, Service30

    CONSTRUCTION OF ONE SHELL31

    Design/vac/test pressure:g

    32

    Design temperature

    33

    Number passes per shell

    34

    Corrosion allowance

    35

    Connections

    36

    37

    38

    Tube No.

    39

    Tks-40

    41

    Length

    42

    Pitch

    43

    Tube type

    44

    Material

    45

    Shell

    46

    ID

    47

    OD

    48

    Shell Side

    49

    Tube Side

    50

    Shell cover

    51

    Tube pattern

    52

    Baffle-crossing

    53

    Type

    54

    Cut(%d)

    55

    Spacing: c/c

    56

    Baffle-long

    57

    Seal type

    58

    Inlet

    RhoV2-Inlet nozzle

    Shell Side Tube Side

    Fouling resist. (min)

    Pressure drop, allow./calc.

    Velocity

    Pressure (abs)

    Latent heat

    Thermal conductivity

    Specific heat

    Molecular wt, NC

    Molecular wt, Vap

    Viscosity

    Density

    MTD corrected

    Dirty Clean

    Heat Exchanger Specification Sheet