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

description

Heat exchanger specification

Transcript of TEMA Specification Sheet

  • 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