Design of Reactor With Agitator Shaft 1

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    CademPVD by CADEM Softwares

    Most value for money software for the mechanical design of process equipment

    Trial version available on our website www.cadem.in

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    all undefined parameters: Flange OD, Flange ID, PCD, Number and Size of bolts, Gasket OD & ID, etc.

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    Pressure Vessels

    Reaction VesselsAgitator ShaftsHeat ExchangersProcess ColumnsStorage TankFloating RoofChimney

    ASME Sec. VIII Div. 1

    TEMAEEUAIS 2825EN 13445

    API 650API 620IS 6533

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    EXAMPLE NO. PC-01

    DESIGN OFREACTION VESSEL WITH AGITATOR SHAFT

    NOTE:

    1) Link to youtube video of this design:https://www.youtube.com/watch?v=Szl9AE_d4pQ&list=PLPL8SPZUxm-mFqQZceyhr13QYDEruelJx&index=6

    2) As you can see in the video, the inbuilt intelligence in the software generates maximum information byitself.

    Eg: For a body flange, the software evaluates all the undefined parameters Flange OD, Flange ID, PCD,Number and Size of bolts, Gasket OD & ID, etc. meeting the requirements of specified equipment designcode.

    3) In case of any changes to the interconnected shell geometry and / or design conditions (pressure /temperature) including material of constructions, these dimensions are automatically regenerated by the

    software to meet the new requirements.

    4) The software can generate cost estimation and BOM in Excel.

    This example covers design of a Reaction Vessel with Agitator Shaft.

    This reaction vessel has dishes at the top and bottom ends. The jacketing is of plain

    shell type, partially covering the main shell and extending on to the bottom dished end.It has an agitator, with say 20 HP power and the agitator shaft RPM is 100. All thecomponents in contact with the internal process liquid are of SS 316 and the jacketing isof SS 304.

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    Index

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    Sr. No. Description Page No

    1 Title page & equipment info

    2 Design data

    3 Material of constructions

    4 Effective Pressures

    5 Weight summary report

    6 Wind load calculations

    7 Seismic load calculations

    8 Design of Dished End (Front)

    9 Design of Closure Flng (Front)

    10 Design of Closure Flng (Front)

    11 Design of Shel l Flng (Front)

    12 Design of Shel l Flng (Front)

    13 Design of Main Shell

    14 Design of Dished End (Rear)

    15 Design of Jacket Closure (Top)

    16 Design of Jacket Shell

    17 Design of Jacket Dish (Bottom)

    18 Design of Lug Support

    19 Design of Lug Support

    20 Design of Shaft

    21 Design of Impeller (1)

    22 Design of Lifting Lugs

    23 Foundation load data

    24 C.G. Data

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    EQUIPMENT INFORMATION :

    DESIGN & REVIEWAL :

    INSPECTION & APPROVAL :

    EQUIPMENT DATA :

    JACKETING DATA :

    AGITATOR DATA :

    OTHER DATA :

    Customer ABC Company Ltd.

    Project Soap Plant

    Location Vapi Site

    Plant Refrigeration Plant

    Design Code ASME VIII Div.1, 10 A11

    Equipment Name Reactor R101

    Equipment Type Reaction Vessel

    Equipment Class N.A.

    Equipment Category N.A.

    Reference Drawing No ---

    Service Chemical Services

    Support Type Lug Supports

    Designed By

    Design Date 06-04-2015 19:23:54

    Checked By

    Approved By

    Revision R00

    Inspection Agency ---

    Reviewed By ---

    Front end Dished End

    Front end flanged True

    Rear end Dished End

    Rear end flanged False

    Shell ID 1600 mm

    Shell OD 1628 mm

    Length, Shell (W.L. to W.L) / Overall 2400 / 3338.3 mm

    Jacketing system Shell & Bottom End

    Jacket type Plain Jacket

    Power 20 hp (MKS)

    RPM 100

    Duty Factor 2

    Diameter of shaft 101 mm

    Free Length of shaft 3738.3 mm

    No of impellers 1

    Propped True

    Fabricated weight 5065.2 kgf Empty weight + external weights 5065.2 kgf

    Estimated operating weight 11231.4 kgf

    Estimated hydrotest weight 10964.4 kgf

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    (1) PROCESS DETAILS :

    (4) TEMPERATURE : C

    (5) ALLOWANCES : mm

    (6) RADIOGRAPHY & JOINT EFFICIENCY :

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    REACTION VESSEL DESIGN DATA

    SHELL SIDE JACKET SIDE

    MEDIA DENSITY MEDIA DENSITY

    kg/m kg/m

    Operating Process 980 Steam 1.5

    Design1 1000 1000

    Design2

    Startup

    Shutdown

    Upset

    Hydrotest Water 1000 Water 1000

    Pneumatic Process 1.2 Steam 1.2

    (2) PR. : kgf/mm g INT. EXT. INT. EXT.

    Input Pr MAWP Input Pr Input Pr MAWP Input Pr

    Operating 0.06 0.06 0.01055 0.04 0.04 0.01055

    Design1 0.08 0.08 0.01055 0.05 0.05 0.01055

    Design2

    Startup

    Shutdown

    Upset

    (3) TEST PR. : kgf/mm g Based on Based on

    Input Pr MAWP MAP Input Pr MAWP MAP

    Hydrotest 0.106 0.106 0.106 0.07085 0.07085 0.07085

    Pneumatic 0.08976 0.08976 0.08976 0.05995 0.05995 0.05995

    MIN. MDMT. MAX. MIN. MDMT. MAX

    Operating 20 120 20 150

    Design1 10 180 10 200

    Design2

    Startup

    Shutdown

    Upset

    Hydrotest 21.67 50 21.67 50

    Pneumatic 21.67 50 21.67

    INT. EXT. INT. EXT.

    Corrosion 0 0 0 0

    Polishing 0 0 0

    RADIOGRAPHY JOINTEFFICIENCY

    RADIOGRAPHY JOINTEFFICIENCY

    Shell Spot + T Joints 0.85 Spot + T Joints 0.85

    Head Full 1.00 Full 1.00

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    REACTION VESSEL DESIGN DATA

    1. MATERIAL OF CONSTRUCTION :

    2. NOZZLE CONNECTIONS :

    3. AGITATOR:

    4. INSULATION & CLADDING:

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    Shell side Jacket side

    Shell / Channel SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Head SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Body flange SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Body flange cover SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Liner

    Shell side Jacket side

    Nozzle neck 40 & < 200SA-312 GR. TP316 Smls. Pipe[UNS:S31600]

    SA-312 GR. TP304 Smls. Pipe[UNS:S30400]

    Flange SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Cover flange SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Nozzle neck >= NPS 200 SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Flange SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Cover flange SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Pad flange SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Pad flange cover SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Manhole flange SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Manhole cover SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]Reinforcement pad SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    External bolt SA-193 GR. B7 Bolt [UNS:G41400] SA-193 GR. B7 Bolt [UNS:G41400]

    External gasket Spiral metal wound CAF filled (S.S.) CAF with suitable binder (3 mm.)

    Stiffener SA-240 GR. 316 Plt. [UNS:S31600] SA-240 GR. 304 Plt. [UNS:S30400]

    Lifting lug IS-2062 GR. A Plt. IS-2062 GR. A Plt.

    Support IS-2062 GR. A Plt. IS-2062 GR. A Plt.

    Anchor bolt SA-36 / IS-1363,67 Bolt [UNS:K02600] SA-36 / IS-1363,67 Bolt [UNS:K02600]

    Shaft SA-479 GR. 316 Bar [UNS:S31600]

    Impeller SA-240 GR. 316 Plt. [UNS:S31600]

    Internal coupling SA-479 GR. 316 Bar [UNS:S31600]

    Housing SA-479 GR. 316 Bar [UNS:S31600]

    Housing cover SA-240 GR. 316 Plt. [UNS:S31600]

    Mat. / Density / Thk. Rockwool (Mineral Fibre) / 136.2 kg/m / 60 mm

    Mat. / Thk. Al. sheet / 1.191 mm

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    SUMMARY OF EFFECTIVE DESIGN PRESSURES IN kgf/mm g VS TEMPERATURE IN C

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    Sr. Item name Temp. Inside pr. Liquid pr. Effective pr.

    No. +ve -ve +ve -ve

    1 Dished End (Front) 180 0.08 0.01055 0 0.08 0.010552 Closure Flng (Front) 180 0.08 0.01055 0 0.08 0.01055

    3 Shell Flng (Front) 180 0.08 0.01055 0 0.08 0.01055

    4 Main Shell 180 0.08 0.01055 0 0.09055 0.06055

    5 Dished End (Rear) 180 0.08 0.01055 0 0.08 0.01055

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    ITEM WISE WEIGHT SUMMARY

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    Sr.No. Item name Item sizeEmptywt

    Volume Filled wt

    kgf m kgf

    1 Dished End (Front)Torispherical End CR = 1440,KR = 272, 8 Nom / 7.2 MinThk, SF = 50

    216.5 0.607 823.5

    2 Closure Flng (Front)Plate Ring - 1786 OD x 1619ID x 1729 PCD, RF, 154.681Thk, Trgv = 1.588

    546.9 0 546.9

    3 Shell Flng (Front)Plate Ring - 1786 OD x 1631ID x 1729 PCD, RF, 158.474Thk, Trgv = 1.588

    522.1 0 522.1

    4 Gasket Flng (Front)1695.2 OD x 1631 ID, 4.763Thk

    0.1 0 0.1

    5 Bolt Flng (Front)

    Hex Head Bolt M24 x 354.18

    Lg, 68 Nos. 86.25 0 86.25

    6 Main Shell 1628 OD x 14 Thk, 2400 Lg 1362.9 4.825 6188.4

    7 Dished End (Rear)Torispherical End CR = 1440,KR = 272, 8 Nom / 7.2 MinThk, SF = 50

    216.5 0.607 823.5

    8 Jacket Closure (Top)5296 Long x 111 Wide x 18Thk

    84.65 0 84.65

    9 Jacket Shell 1744 OD x 8 Thk, 1850 Lg 645.7 0.122 767.6

    10 Jacket Dish (Bottom)Torispherical End CR = 1728,KR = 175, 8 Nom / 7.2 MinThk, SF = 50

    222.2 0 222.2

    11 Gusset Plate

    220 Long x 240 Wide x 16

    Thk, 4 Nos. 26.75 0 26.75

    12 Anchor Bolt Anchor M20 x 200 Lg, 8 Nos. 3.979 0 3.979

    13 Support Pad330 Long x 300 Wide x 14Thk, 4 Nos.

    44.35 0 44.35

    14 Motor 20 HP x 1450 RPM 200 0 200

    15 Gear Box 20 HP x 14.5 Red. Ratio 200 0 200

    16 Coupling Flexible Coupled B5 28.38 0 28.38

    17 Bearing Housing 222 OD x 43 Thk, 325 Lg 62.87 0.00472 67.59

    18 Top Bearing SKF Taper Roller 30216 0.163 0 0.163

    19 Bottom Bearing SKF Taper Roller 30217 0.209 0 0.209

    20 Shaft Seal Gland Packing 10 0 10

    21 Shaft 101 OD x 4438.311 Lg 284.5 0 284.5

    22 Impeller (1)Propeller, Sweep Dia Propellerx 4 Blades

    27 0 27

    23 Lifting Lugs135 Long x 77 Wide x 28 Thk,2 Nos.

    4.608 0 4.608

    24 Pad (Lifting Lugs)70 Long x 180 Wide x 8 Thk, 2Nos.

    1.613 0 1.613

    25 Insulation5805.663 W x 5411.911 L, 60Thk

    256.7 0 256.7

    26 Cladding 5809.404 W x 5411.911 L,1.191 Thk

    10.36 0 10.36

    27

    28

    29

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    30

    5065.2 10964.4

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS ( Design Mode 1 , Uncorroded Condition ) :

    3. CALCULATION OF FORCES AND MOMENTS:

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    WIND LOAD CALCULATION

    CODE Wind [IS:875, 87]

    Basic wind speed ( Section 5.2 ) Vb 50 m/s

    Expected life of equipment ( Section 5.3.1 ) 25 Years

    Probability factor (Risk coeff) ( Section 5.3.1 ) K1 0.902

    Terrain category ( Section 5.3.2 ) Category 2

    Structure class ( Section 5.3.2.2 ) Class B

    Topography factor ( Section 5.3.3 ) K3 1.3

    Force coefficient (Shape factor) Cf 0.8

    Equivalent diameter De 2408 mm

    Overall length of equipment L 3338.3 mm

    Height of C.G. of equipment Hcg 1804.4 mm

    Size and height factor ( Section 5.3.2 ) K2 0.98Effective transverse cross sectional area

    = De x L A 8038652.8 mm

    Effective wind speed

    = K1 x K2 x K3 x Vb Vz 57.44 m/s

    Wind pressure

    = 6E-08 x Vz 2 Pz 0.0002 kgf/mm

    Longitudinal force

    = Cf x A x Pz F 1273.2 kgf

    Support elevation H 456.2 mm

    Turning moment

    = F x ( Hcg - H ) M 1716622.5 kgf-mm

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS ( Design Mode 1 , Uncorroded Condition ) :

    2. CALCULATION OF FORCES AND MOMENTS:

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    SEISMIC LOAD CALCULATION

    CODE Seismic [IS:1893, 02]

    Weight of equipment Wo 11231.4 kgf

    Importance factor ( Table-6 , 2002 ) I 1.5

    Soil profile type Stiff Soil Profile (SD)

    Foundation type RCC footings + Tie Beams

    Damping factor 5

    Seismic zone Zone III

    Seismic zone factor ( Table-2 , 2002 ) Z 0.16

    Response reduction factor ( Table-7 , 2002 ) R 2.9

    Spectral accelerations coeff. ( Fig. 2 , 2002 ) Sa / g 2.5, Use max value

    Damping correction factor ( Table-3 , 2002 ) Cf 1

    Seismic coefficient ( Clause-6.4.2 , 2002 )

    = 0.5 x Z x I x Cf x ( Sa / g ) x ( 1 / R )= 0.5 x 0.16 x 1.5 x 1 x

    2.5 x ( 1 / 2.9 ) Ah 0.103

    Elevation of support H 456.2 mm

    Height of C.G. of equipment Hcg 1804.4 mm

    Seismic base shear force

    = Ah x Wo

    = 0.103 x 11231.4 Vb 1161.9 kgf

    Seismic moment of support

    = Vb x ( Hcg - H )

    = 1161.9 x ( 1804.4 - 456.2 ) M 1566464.3 kgf-mm

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS ( Design Mode 1 , Uncorroded Condition ) :

    2. DESIGN CALCULATION AS PER UG 32 e / APPENDIX 1-4 ( d ) :

    Factor [M]

    = ( 1 / 4 ) x [ 3 + SQRT [ CR / KR ] ]

    = ( 1 / 4 ) x [ 3 + SQRT [ 1440 / 272 ] ]

    = 1.325

    Thickness for internal pressure [t]

    = M x Pi x CR / ( 2 x S x E - 0.2 x Pi )

    = 1.325 x 0.08 x 1440 / ( 2 x 13.79 x 1 - 0.2 x 0.08 )= 5.54 mm

    3. DESIGN CALCULATION AS PER UG 33 e :

    Thickness for equivalent external pressure [t]

    = M x 1.67 x Pe x CR / ( 2 x S x 1.0 - 0.2 x 1.67 x Pe )

    = 1.325 x 1.67 x 0.01055 x 1440 / ( 2 x 13.79 x 1.0 - 0.2 x 1.67 x 0.01055 )

    = 1.219 mm

    Assumed head thickness, [te]

    = 4.454 mm

    Assumed outside crown radius, [CRo]

    = 1448 mm

    Factor [A]

    = 0.125 x te / CRo

    = 0.125 x 4.454 / 1448

    = 0.00038

    Factor with reference to chart (HA-2) [B]

    = 3.455 kgf/mm

    Allowable external pressure [Pa]

    = B x te / CRo

    = 3.455 x 4.454 / 1448

    = 0.01063 kgf/mm

    Since Pa > Pe, design is safe

    Since available thickness is more than design thickness, design is safe.

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    DESIGN OF TORISPHERICAL HEAD ( INT. & EXT. PRESSURE ) Dished End (Front)

    CODE ASME VIII Div.1, 10 A11

    Design pressure ( internal ) Pi 0.08 kgf/mm g

    Design pressure ( external ) Pe 0.01055 kgf/mm g

    Design temperature T 180 C

    Material of construction SA-240 GR. 316 Plt. [UNS:S31600]

    Max. allowable stress @ design temp. S 13.79 kgf/mm

    Radiography Full

    Joint efficiency E 1

    Outside diameter of head OD 1616 mm

    Crown radius CR 1440 mm

    Knuckle radius KR 272 mm

    Nominal thickness 8 mm

    Nominal thickness required as per TEMA N.A mmInternal allowance, corrosion + polishing 0 mm

    External allowance, corrosion + polishing 0 mm

    Thinning allowance / Under tolerance 0.8 mm

    Available thickness 7.2 mm

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS ( Design Mode 1 , Uncorroded Condition ) :

    2. FLANGE DATA :

    3. BOLTING DATA :

    4. LINER DATA :

    5. GASKET DATA :

    5a. Flange gasket data :

    5b. Partition groove gasket data (For H.E. body flange) :

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    FLANGE DESIGN ( INTERNAL ) Closure Flng (Front)

    CODE ASME VIII Div.1, 10 A11

    Design pressure P 0.08 kgf/mm g

    Design temperature T 180 C

    Allowance CA 0 mm

    Groove allowance Tg 1.588 mm

    M.O.C. SA-240 GR. 316 Plt. [UNS:S31600]

    Code allw. stress @ design temp. Sfo 10.46 kgf/mm

    Code allw. stress @ atm. temp. Sfa 14.06 kgf/mm

    Inside diameter B 1619 mm

    Outside diameter A 1786 mm

    Hub length h 0 mm

    Thickness ( hub end ) g1 0 mmThickness ( pipe end ) g0 0 mm

    Thickness provided 154.7 mm

    Thickness available 153.1 mm

    M.O.C. SA-193 GR. B7 Bolt [UNS:G41400]

    Code allw. stress @ design temp. Sb 17.58 kgf/mm

    Code allw. stress @ atm. temp. Sa 17.58 kgf/mm

    Bolt PCD C 1729 mm

    Bolt dia. db 24 mm

    No. of bolts nb 68

    M.O.C.

    Liner ID mm

    Liner OD mm

    Liner thk. mm

    M.O.C. Spiral metal wound CAF filled (S.S.)

    Gasket type Ring Gasket

    Gasket confinement type Unconfined

    Flange face type Raised Face

    Flange gakset surface finish Serrated (Normal)

    Counter flange face type Raised FaceCounter gakset surface finish Serrated (Normal)

    Applicalbe gasket sketch in Table 2-5.2 Type 1B

    Applicable gasket column in Table 2-5.2 1

    Gasket seating stress ( refer to Note 1, Table 2-5.1 ) y 7.031 kgf/mm

    Gasket factor ( from Table 2-5.1 ) m 3

    Inside diameter Gi 1631 mm

    Outside diameter Go 1695.2 mm

    Width of gasket ( as per Table 2-5.2 ) N 32.1 mm

    Width of gasket ( as per Table 2-5.2 ) w 32.1 mm

    Width of raised face or gasket contact width 38.1 mm

    ( as per Table 2-5.2 )

    Basic gasket seating width ( as per Table 2-5.2 ) b0 16.05 mm

    Effective gasket width ( as per Table 2-5.2 ) b 10.1 mm

    Dia. at load reaction ( see Table 2-5.2 ) G 1675 mm

    M.O.C. --

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    6. BOLT LOAD CALCULATIONS AS PER APPENDIX 2-5 (b1)

    Total joint - contact surface compression load [Hp]

    = 2 x ( x b x G x m + b' x Lp x m' ) x P

    = 2 x ( x 10.1 x 1675 x 3 + 0 x 0 x 0 ) x 0.08

    = 25499.6 kgfTotal hydrostatic end force [H]

    = 0.25 x x G x P

    = 0.25 x x 1675 x 0.08

    = 176284.5 kgf

    Minimum required bolt load for operating condition [Wm1a]

    = Hp + H

    = 25499.6 + 176284.5

    = 201784.1 kgf

    Minimum required bolt load for operating condition [Wm1b]

    ( from mating flange )

    = 201784.1 kgf

    Governing bolt load for operating condition [Wm1]

    = MAX [ Wm1a , Wm1b ]

    = MAX [ 201784.1 , 201784.1 ]= 201784.1 kgf

    7. BOLT LOAD CALCULATION AS PER APPENDIX 2-5 (b2)

    Minimum required bolt load for gasket seating [Wm2]

    = ( x b x G x y + b' x Lp x y' )

    = ( x 10.1 x 1675 x 7.031 + 0 x 0 x 0 )

    = 373499.5 kgf

    8. BOLT AREAS AS PER APPENDIX 2-5 (d)

    Total required cross-sectional area of bolts [Am]

    = MAX [ Wm2 / Sa , Wm1 / Sb ] ........ For Internal '+' Pr Design

    = Wm2 / Sa ..................................... For External Pr & Self Sealing Design

    = 21249.6 mm

    Actual bolt area using root diameter [Ab]

    = 21266.9 mm

    Flange design bolt load for the gasket seating [W]= 0.5 x ( Am + Ab ) x Sa x 1 .................... average bolt area

    = Ab x Sa x 1 ..........................................full bolt area

    = 373650.9 kgf ( Avg. bolt area and margin factor of 1 )

    9. CHECK FOR GASKET CRUSHING

    Minimum gasket width required [Nmin]

    = Ab x Sb / ( 2 x x y x G )

    = 21266.9 x 17.58 / ( 2 x x 7.031 x 1675 )

    = 5.052 mm

    10. BOLT SPACING CORRECTION FACTOR

    As per Brownell & Young or IS 2825,

    = SQRT [ Bolt spacing / ( 2 x db + t ) ]

    As per TEMA or BS 5500,

    = SQRT [ Bolt spacing / Bmax ] ................... where,

    Bmax = maximum recommended bolt spacing = 2 x db + 6 x t / ( m + 0.5 )Brownell & Young, Cf = 1 ( min. equal to 1 )

    11. LOADS AND FORCES DURING OPERATING CONDITION AS PER APPENDIX 2-3

    Hydrostatic end force on area inside of flange [HD]

    = 0.25 x x B 2x P

    = 0.25 x x 1619 2x 0.08

    = 164692.4 kgf

    Gasket load (difference between flange design bolt load and total hydrostatic end force) [HG]

    = Wm1 - H

    = 201784.1 - 176284.5

    = 25499.6 kgf

    Difference between total hydrostatic end force and hydrostatic end force on area inside of flange [HT]

    = H - HD

    = 176284.5 - 164692.4

    = 11592.1 kgf

    12. MOMENT ARMS FOR FLANGE LOADS AS PER TABLE 2-6

    Radial distance from the bolt circle to intersection of hub and back of flange, as per Appendix 2-3 [R]

    = 0.5 x ( C - B ) - g1

    = 0.5 x ( 1729 - 1619 ) - 0

    Gasket seating stress ( refer to Note 1, Table 2-5.1 ) y' 0 kgf/mm

    Gasket factor ( from Table 2-5.1 ) m' 0

    Pass partition gasket width Wp 0 mm

    Pass partition gasket length Lp 0 mm

    Effective pass partition gasket width b' 0 mm

    RING FLANGE DESIGN Closure Flng (Front)

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    = 55

    Radial distance from the bolt circle to the circle on which HD acts [hD]

    = R + 0.5 x g1

    = 55 + 0.5 x 0

    = 55 mm

    Radial distance from gasket load reaction to the bolt circle [hG]

    = 0.5 x ( C - G )

    = 0.5 x ( 1729 - 1675 )

    = 27 mm

    Radial distance from the bolt circle to the circle on which HT acts [hT]

    = 0.5 x ( R + g1 + hG )

    = 0.5 x ( 55 + 0 + 27 )= 41 mm

    13. FLANGE MOMENTS UNDER OPERATING CONDITION AS PER APPENDIX 2-6

    Component of moment due to HD [MD]

    = HD x hD

    = 164692.4 x 55

    = 9058082.2 kgf-mm

    Component of moment due to HG [MG]

    = HG x hG

    = 25499.6 x 27

    = 688371.3 kgf-mm

    Component of moment due to HT [MT]

    = HT x hT

    = 11592.1 x 41

    = 475251.3 kgf-mmTotal moment acting on the flange for operating condition [MO]

    = MD + MG + MT

    = 9058082.2 + 688371.3 + 475251.3

    = 10221704.8 kgf-mm

    14. LOADS AND FORCES DURING GASKET SEATING AS PER APPENDIX 2-3

    Gasket load for seating condition [HG]

    = W

    = 373650.9 kgf

    15. MOMENT UNDER GASKET SEATING AS PER APPENDIX 2-6

    Total moment acting on the flange for gasket seating [MO']

    = W x hG

    = 373650.9 x 27

    = 10086863.4 kgf-mm

    16. SHAPE CONSTANTSFactor [K]

    = A / B

    = 1786 / 1619

    = 1.103

    Flange factor from Fig. 2-7.1 [Y]

    = 19.74

    17. FLANGE THICKNESS REQUIRED AS PER APPENDIX 2-7

    Equivalent moment [Mmax]

    = MAX [ MO , MO' x Sfo / Sfa ]

    = MAX [ 10221704.8 , 10086863.4 x 10.46 / 14.06 ]

    = 10221704.8 kgf-mm

    Corrected equivalent moment per unit length [M]

    = Mmax x Cf / B

    = 10221704.8 x 1 / 1619= 6313.6 kgf

    Required thickness of flange [t]

    = SQRT [ M x Y / Sfo ]

    = SQRT [ 6313.6 x 19.74 / 10.46 ]

    = 109.2 mm

    18. FLANGE RIGIDITY CHECKING AS PER APPENDIX 2-14

    Rigidity index [J]

    = 109.4 x Mmax / ( Efo x tr 3x KL x ln ( K ) )

    = 109.4 x 10221704.8 / ( 18786 x 144.8 3 x 0.2 x ln ( 1.103 ) )

    = 0.999Since J < 1.0, design is safe

    Assumed flange thickness tr 144.8 mm

    Modulus of elasticity for flange Efo 18786 kgf/mm

    Rigidity factor KL 0.2

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS ( Design Mode 1 , Uncorroded Condition ) :

    2. FLANGE DATA :

    3. BOLTING DATA :

    4. LINER DATA :

    5. GASKET DATA :

    5a. Flange gasket data :

    5b. Partition groove gasket data (For H.E. body flange) :

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    FLANGE DESIGN ( EXTERNAL ) Closure Flng (Front)

    CODE ASME VIII Div.1, 10 A11

    Design pressure P 0.01055 kgf/mm g

    Design temperature T 180 C

    Allowance CA 0 mm

    Groove allowance Tg 1.588 mm

    M.O.C. SA-240 GR. 316 Plt. [UNS:S31600]

    Code allw. stress @ design temp. Sfo 10.46 kgf/mm

    Code allw. stress @ atm. temp. Sfa 14.06 kgf/mm

    Inside diameter B 1619 mm

    Outside diameter A 1786 mm

    Hub length h 0 mm

    Thickness ( hub end ) g1 0 mmThickness ( pipe end ) g0 0 mm

    Thickness provided 154.7 mm

    Thickness available 153.1 mm

    M.O.C. SA-193 GR. B7 Bolt [UNS:G41400]

    Code allw. stress @ design temp. Sb 17.58 kgf/mm

    Code allw. stress @ atm. temp. Sa 17.58 kgf/mm

    Bolt PCD C 1729 mm

    Bolt dia. db 24 mm

    No. of bolts nb 68

    M.O.C.

    Liner ID mm

    Liner OD mm

    Liner thk. mm

    M.O.C. Spiral metal wound CAF filled (S.S.)

    Gasket type Ring Gasket

    Gasket confinement type Unconfined

    Flange face type Raised Face

    Flange gakset surface finish Serrated (Normal)

    Counter flange face type Raised FaceCounter gakset surface finish Serrated (Normal)

    Applicalbe gasket sketch in Table 2-5.2 Type 1B

    Applicable gasket column in Table 2-5.2 1

    Gasket seating stress ( refer to Note 1, Table 2-5.1 ) y 7.031 kgf/mm

    Gasket factor ( from Table 2-5.1 ) m 3

    Inside diameter Gi 1631 mm

    Outside diameter Go 1695.2 mm

    Width of gasket ( as per Table 2-5.2 ) N 32.1 mm

    Width of gasket ( as per Table 2-5.2 ) w 32.1 mm

    Width of raised face or gasket contact width 38.1 mm

    ( as per Table 2-5.2 )

    Basic gasket seating width ( as per Table 2-5.2 ) b0 16.05 mm

    Effective gasket width ( as per Table 2-5.2 ) b 10.1 mm

    Dia. at load reaction ( see Table 2-5.2 ) G 1675 mm

    M.O.C. --

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    6. BOLT LOAD CALCULATIONS AS PER APPENDIX 2-5 (b1)

    Total joint - contact surface compression load [Hp]

    = 2 x ( x b x G x m + b' x Lp x m' ) x P

    = 2 x ( x 10.1 x 1675 x 3 + 0 x 0 x 0 ) x 0.01055

    = 3361.6 kgfTotal hydrostatic end force [H]

    = 0.25 x x G x P

    = 0.25 x x 1675 x 0.01055

    = 23239.4 kgf

    Minimum required bolt load for operating condition [Wm1a]

    = Hp + H

    = 3361.6 + 23239.4

    = 26600.9 kgf

    Minimum required bolt load for operating condition [Wm1b]

    ( from mating flange )

    = 26600.9 kgf

    Governing bolt load for operating condition [Wm1]

    = MAX [ Wm1a , Wm1b ]

    = MAX [ 26600.9 , 26600.9 ]= 26600.9 kgf

    7. BOLT LOAD CALCULATION AS PER APPENDIX 2-5 (b2)

    Minimum required bolt load for gasket seating [Wm2]

    = ( x b x G x y + b' x Lp x y' )

    = ( x 10.1 x 1675 x 7.031 + 0 x 0 x 0 )

    = 373499.5 kgf

    8. BOLT AREAS AS PER APPENDIX 2-5 (d)

    Total required cross-sectional area of bolts [Am]

    = MAX [ Wm2 / Sa , Wm1 / Sb ] ........ For Internal '+' Pr Design

    = Wm2 / Sa ..................................... For External Pr & Self Sealing Design

    = 21249.6 mm

    Actual bolt area using root diameter [Ab]

    = 21266.9 mm

    Flange design bolt load for the gasket seating [W]= 0.5 x ( Am + Ab ) x Sa x 1 .................... average bolt area

    = Ab x Sa x 1 ..........................................full bolt area

    = 373650.9 kgf ( Avg. bolt area and margin factor of 1 )

    9. CHECK FOR GASKET CRUSHING

    Minimum gasket width required [Nmin]

    = Ab x Sb / ( 2 x x y x G )

    = 21266.9 x 17.58 / ( 2 x x 7.031 x 1675 )

    = 5.052 mm

    10. BOLT SPACING CORRECTION FACTOR

    As per Brownell & Young or IS 2825,

    = SQRT [ Bolt spacing / ( 2 x db + t ) ]

    As per TEMA or BS 5500,

    = SQRT [ Bolt spacing / Bmax ] ................... where,

    Bmax = maximum recommended bolt spacing = 2 x db + 6 x t / ( m + 0.5 )Brownell & Young, Cf = 1 ( min. equal to 1 )

    11. LOADS AND FORCES DURING OPERATING CONDITION AS PER APPENDIX 2-3

    Hydrostatic end force on area inside of flange [HD]

    = 0.25 x x B 2x P

    = 0.25 x x 1619 2x 0.01055

    = 21711.2 kgf

    Difference between total hydrostatic end force and hydrostatic end force on area inside of flange [HT]

    = H - HD

    = 23239.4 - 21711.2

    = 1528.2 kgf

    12. MOMENT ARMS FOR FLANGE LOADS AS PER TABLE 2-6

    Radial distance from the bolt circle to intersection of hub and back of flange, as per Appendix 2-3 [R]

    = 0.5 x ( C - B ) - g1

    = 0.5 x ( 1729 - 1619 ) - 0

    = 55

    Radial distance from the bolt circle to the circle on which HD acts [hD]

    = R + 0.5 x g1

    = 55 + 0.5 x 0

    Gasket seating stress ( refer to Note 1, Table 2-5.1 ) y' 0 kgf/mm

    Gasket factor ( from Table 2-5.1 ) m' 0

    Pass partition gasket width Wp 0 mm

    Pass partition gasket length Lp 0 mm

    Effective pass partition gasket width b' 0 mm

    RING FLANGE DESIGN Closure Flng (Front)

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    = 55 mm

    Radial distance from gasket load reaction to the bolt circle [hG]

    = 0.5 x ( C - G )

    = 0.5 x ( 1729 - 1675 )

    = 27 mm

    Radial distance from the bolt circle to the circle on which HT acts [hT]

    = 0.5 x ( R + g1 + hG )

    = 0.5 x ( 55 + 0 + 27 )

    = 41 mm

    13. FLANGE MOMENTS UNDER OPERATING CONDITION AS PER APPENDIX 2-6

    Component of moment due to HD [MD]

    = HD x ( hD - hG )= 21711.2 x ( 55 - 27 )

    = 608012.7 kgf-mm

    Component of moment due to HT [MT]

    = HT x ( hT - hG )

    = 1528.2 x ( 41 - 27 )

    = 21398 kgf-mm

    Total moment acting on the flange for operating condition [MO]

    = MD + MT

    = 608012.7 + 21398

    = 629410.7 kgf-mm

    14. LOADS AND FORCES DURING GASKET SEATING AS PER APPENDIX 2-3

    Gasket load for seating condition [HG]

    = W

    = 373650.9 kgf15. MOMENT UNDER GASKET SEATING AS PER APPENDIX 2-6

    Total moment acting on the flange for gasket seating [MO']

    = W x hG

    = 373650.9 x 27

    = 10086863.4 kgf-mm

    16. SHAPE CONSTANTS

    Factor [K]

    = A / B

    = 1786 / 1619

    = 1.103

    Flange factor from Fig. 2-7.1 [Y]

    = 19.74

    17. FLANGE THICKNESS REQUIRED AS PER APPENDIX 2-7

    Equivalent moment [Mmax]= MAX [ MO , MO' x Sfo / Sfa ]

    = MAX [ 629410.7 , 10086863.4 x 10.46 / 14.06 ]

    = 7500591.6 kgf-mm

    Corrected equivalent moment per unit length [M]

    = Mmax x Cf / B

    = 7500591.6 x 1 / 1619

    = 4632.9 kgf

    Required thickness of flange [t]

    = SQRT [ M x Y / Sfo ]

    = SQRT [ 4632.9 x 19.74 / 10.46 ]

    = 93.51 mm

    18. FLANGE RIGIDITY CHECKING AS PER APPENDIX 2-14

    Rigidity index [J]

    = 109.4 x Mmax / ( Efo x tr 3x KL x ln ( K ) )

    = 109.4 x 7500591.6 / ( 18786 x 144.3 3 x 0.2 x ln ( 1.103 ) )

    = 0.997

    Since J < 1.0, design is safe

    Assumed flange thickness tr 144.3 mm

    Modulus of elasticity for flange Efo 18786 kgf/mm

    Rigidity factor KL 0.2

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS ( Design Mode 1 , Uncorroded Condition ) :

    2. FLANGE DATA :

    3. BOLTING DATA :

    4. LINER DATA :

    5. GASKET DATA :

    5a. Flange gasket data :

    5b. Partition groove gasket data (For H.E. body flange) :

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    FLANGE DESIGN ( INTERNAL ) Shell Flng (Front)

    CODE ASME VIII Div.1, 10 A11

    Design pressure P 0.08 kgf/mm g

    Design temperature T 180 C

    Allowance CA 0 mm

    Groove allowance Tg 1.588 mm

    M.O.C. SA-240 GR. 316 Plt. [UNS:S31600]

    Code allw. stress @ design temp. Sfo 10.46 kgf/mm

    Code allw. stress @ atm. temp. Sfa 14.06 kgf/mm

    Inside diameter B 1631 mm

    Outside diameter A 1786 mm

    Hub length h 0 mm

    Thickness ( hub end ) g1 0 mmThickness ( pipe end ) g0 0 mm

    Thickness provided 158.5 mm

    Thickness available 156.9 mm

    M.O.C. SA-193 GR. B7 Bolt [UNS:G41400]

    Code allw. stress @ design temp. Sb 17.58 kgf/mm

    Code allw. stress @ atm. temp. Sa 17.58 kgf/mm

    Bolt PCD C 1729 mm

    Bolt dia. db 24 mm

    No. of bolts nb 68

    M.O.C.

    Liner ID mm

    Liner OD mm

    Liner thk. mm

    M.O.C. Spiral metal wound CAF filled (S.S.)

    Gasket type Ring Gasket

    Gasket confinement type Unconfined

    Flange face type Raised Face

    Flange gakset surface finish Serrated (Normal)

    Counter flange face type Raised FaceCounter gakset surface finish Serrated (Normal)

    Applicalbe gasket sketch in Table 2-5.2 Type 1B

    Applicable gasket column in Table 2-5.2 1

    Gasket seating stress ( refer to Note 1, Table 2-5.1 ) y 7.031 kgf/mm

    Gasket factor ( from Table 2-5.1 ) m 3

    Inside diameter Gi 1631 mm

    Outside diameter Go 1695.2 mm

    Width of gasket ( as per Table 2-5.2 ) N 32.1 mm

    Width of gasket ( as per Table 2-5.2 ) w 32.1 mm

    Width of raised face or gasket contact width 38.1 mm

    ( as per Table 2-5.2 )

    Basic gasket seating width ( as per Table 2-5.2 ) b0 16.05 mm

    Effective gasket width ( as per Table 2-5.2 ) b 10.1 mm

    Dia. at load reaction ( see Table 2-5.2 ) G 1675 mm

    M.O.C. --

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    6. BOLT LOAD CALCULATIONS AS PER APPENDIX 2-5 (b1)

    Total joint - contact surface compression load [Hp]

    = 2 x ( x b x G x m + b' x Lp x m' ) x P

    = 2 x ( x 10.1 x 1675 x 3 + 0 x 0 x 0 ) x 0.08

    = 25499.6 kgfTotal hydrostatic end force [H]

    = 0.25 x x G x P

    = 0.25 x x 1675 x 0.08

    = 176284.5 kgf

    Minimum required bolt load for operating condition [Wm1a]

    = Hp + H

    = 25499.6 + 176284.5

    = 201784.1 kgf

    Minimum required bolt load for operating condition [Wm1b]

    ( from mating flange )

    = 201784.1 kgf

    Governing bolt load for operating condition [Wm1]

    = MAX [ Wm1a , Wm1b ]

    = MAX [ 201784.1 , 201784.1 ]= 201784.1 kgf

    7. BOLT LOAD CALCULATION AS PER APPENDIX 2-5 (b2)

    Minimum required bolt load for gasket seating [Wm2]

    = ( x b x G x y + b' x Lp x y' )

    = ( x 10.1 x 1675 x 7.031 + 0 x 0 x 0 )

    = 373499.5 kgf

    8. BOLT AREAS AS PER APPENDIX 2-5 (d)

    Total required cross-sectional area of bolts [Am]

    = MAX [ Wm2 / Sa , Wm1 / Sb ] ........ For Internal '+' Pr Design

    = Wm2 / Sa ..................................... For External Pr & Self Sealing Design

    = 21249.6 mm

    Actual bolt area using root diameter [Ab]

    = 21266.9 mm

    Flange design bolt load for the gasket seating [W]= 0.5 x ( Am + Ab ) x Sa x 1 .................... average bolt area

    = Ab x Sa x 1 ..........................................full bolt area

    = 373650.9 kgf ( Avg. bolt area and margin factor of 1 )

    9. CHECK FOR GASKET CRUSHING

    Minimum gasket width required [Nmin]

    = Ab x Sb / ( 2 x x y x G )

    = 21266.9 x 17.58 / ( 2 x x 7.031 x 1675 )

    = 5.052 mm

    10. BOLT SPACING CORRECTION FACTOR

    As per Brownell & Young or IS 2825,

    = SQRT [ Bolt spacing / ( 2 x db + t ) ]

    As per TEMA or BS 5500,

    = SQRT [ Bolt spacing / Bmax ] ................... where,

    Bmax = maximum recommended bolt spacing = 2 x db + 6 x t / ( m + 0.5 )Brownell & Young, Cf = 1 ( min. equal to 1 )

    11. LOADS AND FORCES DURING OPERATING CONDITION AS PER APPENDIX 2-3

    Hydrostatic end force on area inside of flange [HD]

    = 0.25 x x B 2x P

    = 0.25 x x 1631 2x 0.08

    = 167142.8 kgf

    Gasket load (difference between flange design bolt load and total hydrostatic end force) [HG]

    = Wm1 - H

    = 201784.1 - 176284.5

    = 25499.6 kgf

    Difference between total hydrostatic end force and hydrostatic end force on area inside of flange [HT]

    = H - HD

    = 176284.5 - 167142.8

    = 9141.7 kgf

    12. MOMENT ARMS FOR FLANGE LOADS AS PER TABLE 2-6

    Radial distance from the bolt circle to intersection of hub and back of flange, as per Appendix 2-3 [R]

    = 0.5 x ( C - B ) - g1

    = 0.5 x ( 1729 - 1631 ) - 0

    Gasket seating stress ( refer to Note 1, Table 2-5.1 ) y' 0 kgf/mm

    Gasket factor ( from Table 2-5.1 ) m' 0

    Pass partition gasket width Wp 0 mm

    Pass partition gasket length Lp 0 mm

    Effective pass partition gasket width b' 0 mm

    RING FLANGE DESIGN Shell Flng (Front)

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    = 49

    Radial distance from the bolt circle to the circle on which HD acts [hD]

    = R + 0.5 x g1

    = 49 + 0.5 x 0

    = 49 mm

    Radial distance from gasket load reaction to the bolt circle [hG]

    = 0.5 x ( C - G )

    = 0.5 x ( 1729 - 1675 )

    = 27 mm

    Radial distance from the bolt circle to the circle on which HT acts [hT]

    = 0.5 x ( R + g1 + hG )

    = 0.5 x ( 49 + 0 + 27 )= 38 mm

    13. FLANGE MOMENTS UNDER OPERATING CONDITION AS PER APPENDIX 2-6

    Component of moment due to HD [MD]

    = HD x hD

    = 167142.8 x 49

    = 8189999.4 kgf-mm

    Component of moment due to HG [MG]

    = HG x hG

    = 25499.6 x 27

    = 688371.3 kgf-mm

    Component of moment due to HT [MT]

    = HT x hT

    = 9141.7 x 38

    = 347363.7 kgf-mmTotal moment acting on the flange for operating condition [MO]

    = MD + MG + MT

    = 8189999.4 + 688371.3 + 347363.7

    = 9225734.4 kgf-mm

    14. LOADS AND FORCES DURING GASKET SEATING AS PER APPENDIX 2-3

    Gasket load for seating condition [HG]

    = W

    = 373650.9 kgf

    15. MOMENT UNDER GASKET SEATING AS PER APPENDIX 2-6

    Total moment acting on the flange for gasket seating [MO']

    = W x hG

    = 373650.9 x 27

    = 10086863.4 kgf-mm

    16. SHAPE CONSTANTSFactor [K]

    = A / B

    = 1786 / 1631

    = 1.095

    Flange factor from Fig. 2-7.1 [Y]

    = 21.32

    17. FLANGE THICKNESS REQUIRED AS PER APPENDIX 2-7

    Equivalent moment [Mmax]

    = MAX [ MO , MO' x Sfo / Sfa ]

    = MAX [ 9225734.4 , 10086863.4 x 10.46 / 14.06 ]

    = 9225734.4 kgf-mm

    Corrected equivalent moment per unit length [M]

    = Mmax x Cf / B

    = 9225734.4 x 1 / 1631= 5656.5 kgf

    Required thickness of flange [t]

    = SQRT [ M x Y / Sfo ]

    = SQRT [ 5656.5 x 21.32 / 10.46 ]

    = 107.4 mm

    18. FLANGE RIGIDITY CHECKING AS PER APPENDIX 2-14

    Rigidity index [J]

    = 109.4 x Mmax / ( Efo x tr 3x KL x ln ( K ) )

    = 109.4 x 9225734.4 / ( 18786 x 148.1 3 x 0.2 x ln ( 1.095 ) )

    = 0.996Since J < 1.0, design is safe

    Assumed flange thickness tr 148.1 mm

    Modulus of elasticity for flange Efo 18786 kgf/mm

    Rigidity factor KL 0.2

  • 7/24/2019 Design of Reactor With Agitator Shaft 1

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS ( Design Mode 1 , Uncorroded Condition ) :

    2. FLANGE DATA :

    3. BOLTING DATA :

    4. LINER DATA :

    5. GASKET DATA :

    5a. Flange gasket data :

    5b. Partition groove gasket data (For H.E. body flange) :

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    FLANGE DESIGN ( EXTERNAL ) Shell Flng (Front)

    CODE ASME VIII Div.1, 10 A11

    Design pressure P 0.01055 kgf/mm g

    Design temperature T 180 C

    Allowance CA 0 mm

    Groove allowance Tg 1.588 mm

    M.O.C. SA-240 GR. 316 Plt. [UNS:S31600]

    Code allw. stress @ design temp. Sfo 10.46 kgf/mm

    Code allw. stress @ atm. temp. Sfa 14.06 kgf/mm

    Inside diameter B 1631 mm

    Outside diameter A 1786 mm

    Hub length h 0 mm

    Thickness ( hub end ) g1 0 mmThickness ( pipe end ) g0 0 mm

    Thickness provided 158.5 mm

    Thickness available 156.9 mm

    M.O.C. SA-193 GR. B7 Bolt [UNS:G41400]

    Code allw. stress @ design temp. Sb 17.58 kgf/mm

    Code allw. stress @ atm. temp. Sa 17.58 kgf/mm

    Bolt PCD C 1729 mm

    Bolt dia. db 24 mm

    No. of bolts nb 68

    M.O.C.

    Liner ID mm

    Liner OD mm

    Liner thk. mm

    M.O.C. Spiral metal wound CAF filled (S.S.)

    Gasket type Ring Gasket

    Gasket confinement type Unconfined

    Flange face type Raised Face

    Flange gakset surface finish Serrated (Normal)

    Counter flange face type Raised FaceCounter gakset surface finish Serrated (Normal)

    Applicalbe gasket sketch in Table 2-5.2 Type 1B

    Applicable gasket column in Table 2-5.2 1

    Gasket seating stress ( refer to Note 1, Table 2-5.1 ) y 7.031 kgf/mm

    Gasket factor ( from Table 2-5.1 ) m 3

    Inside diameter Gi 1631 mm

    Outside diameter Go 1695.2 mm

    Width of gasket ( as per Table 2-5.2 ) N 32.1 mm

    Width of gasket ( as per Table 2-5.2 ) w 32.1 mm

    Width of raised face or gasket contact width 38.1 mm

    ( as per Table 2-5.2 )

    Basic gasket seating width ( as per Table 2-5.2 ) b0 16.05 mm

    Effective gasket width ( as per Table 2-5.2 ) b 10.1 mm

    Dia. at load reaction ( see Table 2-5.2 ) G 1675 mm

    M.O.C. --

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    6. BOLT LOAD CALCULATIONS AS PER APPENDIX 2-5 (b1)

    Total joint - contact surface compression load [Hp]

    = 2 x ( px b x G x m + b' x Lp x m' ) x P

    = 2 x ( px 10.1 x 1675 x 3 + 0 x 0 x 0 ) x 0.01055

    = 3361.6 kgfTotal hydrostatic end force [H]

    = 0.25 x px G x P

    = 0.25 x px 1675 x 0.01055

    = 23239.4 kgf

    Minimum required bolt load for operating condition [Wm1a]

    = Hp + H

    = 3361.6 + 23239.4

    = 26600.9 kgf

    Minimum required bolt load for operating condition [Wm1b]

    ( from mating flange )

    = 26600.9 kgf

    Governing bolt load for operating condition [Wm1]

    = MAX [ Wm1a , Wm1b ]

    = MAX [ 26600.9 , 26600.9 ]= 26600.9 kgf

    7. BOLT LOAD CALCULATION AS PER APPENDIX 2-5 (b2)

    Minimum required bolt load for gasket seating [Wm2]

    = ( px b x G x y + b' x Lp x y' )

    = ( px 10.1 x 1675 x 7.031 + 0 x 0 x 0 )

    = 373499.5 kgf

    8. BOLT AREAS AS PER APPENDIX 2-5 (d)

    Total required cross-sectional area of bolts [Am]

    = MAX [ Wm2 / Sa , Wm1 / Sb ] ........ For Internal '+' Pr Design

    = Wm2 / Sa ..................................... For External Pr & Self Sealing Design

    = 21249.6 mm

    Actual bolt area using root diameter [Ab]

    = 21266.9 mm

    Flange design bolt load for the gasket seating [W]= 0.5 x ( Am + Ab ) x Sa x 1 .................... average bolt area

    = Ab x Sa x 1 ..........................................full bolt area

    = 373650.9 kgf ( Avg. bolt area and margin factor of 1 )

    9. CHECK FOR GASKET CRUSHING

    Minimum gasket width required [Nmin]

    = Ab x Sb / ( 2 x px y x G )

    = 21266.9 x 17.58 / ( 2 x px 7.031 x 1675 )

    = 5.052 mm

    10. BOLT SPACING CORRECTION FACTOR

    As per Brownell & Young or IS 2825,

    = SQRT [ Bolt spacing / ( 2 x db + t ) ]

    As per TEMA or BS 5500,

    = SQRT [ Bolt spacing / Bmax ] ................... where,

    Bmax = maximum recommended bolt spacing = 2 x db + 6 x t / ( m + 0.5 )Brownell & Young, Cf = 1 ( min. equal to 1 )

    11. LOADS AND FORCES DURING OPERATING CONDITION AS PER APPENDIX 2-3

    Hydrostatic end force on area inside of flange [HD]

    = 0.25 x px B 2x P

    = 0.25 x px 1631 2x 0.01055

    = 22034.2 kgf

    Difference between total hydrostatic end force and hydrostatic end force on area inside of flange [HT]

    = H - HD

    = 23239.4 - 22034.2

    = 1205.1 kgf

    12. MOMENT ARMS FOR FLANGE LOADS AS PER TABLE 2-6

    Radial distance from the bolt circle to intersection of hub and back of flange, as per Appendix 2-3 [R]

    = 0.5 x ( C - B ) - g1

    = 0.5 x ( 1729 - 1631 ) - 0

    = 49

    Radial distance from the bolt circle to the circle on which HD acts [hD]

    = R + 0.5 x g1

    = 49 + 0.5 x 0

    Gasket seating stress ( refer to Note 1, Table 2-5.1 ) y' 0 kgf/mm

    Gasket factor ( from Table 2-5.1 ) m' 0

    Pass partition gasket width Wp 0 mm

    Pass partition gasket length Lp 0 mm

    Effective pass partition gasket width b' 0 mm

    RING FLANGE DESIGN Shell Flng (Front)

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    = 49 mm

    Radial distance from gasket load reaction to the bolt circle [hG]

    = 0.5 x ( C - G )

    = 0.5 x ( 1729 - 1675 )

    = 27 mm

    Radial distance from the bolt circle to the circle on which HT acts [hT]

    = 0.5 x ( R + g1 + hG )

    = 0.5 x ( 49 + 0 + 27 )

    = 38 mm

    13. FLANGE MOMENTS UNDER OPERATING CONDITION AS PER APPENDIX 2-6

    Component of moment due to HD [MD]

    = HD x ( hD - hG )= 22034.2 x ( 49 - 27 )

    = 484853.9 kgf-mm

    Component of moment due to HT [MT]

    = HT x ( hT - hG )

    = 1205.1 x ( 38 - 27 )

    = 13259.3 kgf-mm

    Total moment acting on the flange for operating condition [MO]

    = MD + MT

    = 484853.9 + 13259.3

    = 498113.2 kgf-mm

    14. LOADS AND FORCES DURING GASKET SEATING AS PER APPENDIX 2-3

    Gasket load for seating condition [HG]

    = W

    = 373650.9 kgf15. MOMENT UNDER GASKET SEATING AS PER APPENDIX 2-6

    Total moment acting on the flange for gasket seating [MO']

    = W x hG

    = 373650.9 x 27

    = 10086863.4 kgf-mm

    16. SHAPE CONSTANTS

    Factor [K]

    = A / B

    = 1786 / 1631

    = 1.095

    Flange factor from Fig. 2-7.1 [Y]

    = 21.32

    17. FLANGE THICKNESS REQUIRED AS PER APPENDIX 2-7

    Equivalent moment [Mmax]= MAX [ MO , MO' x Sfo / Sfa ]

    = MAX [ 498113.2 , 10086863.4 x 10.46 / 14.06 ]

    = 7500591.6 kgf-mm

    Corrected equivalent moment per unit length [M]

    = Mmax x Cf / B

    = 7500591.6 x 1 / 1631

    = 4598.8 kgf

    Required thickness of flange [t]

    = SQRT [ M x Y / Sfo ]

    = SQRT [ 4598.8 x 21.32 / 10.46 ]

    = 96.83 mm

    18. FLANGE RIGIDITY CHECKING AS PER APPENDIX 2-14

    Rigidity index [J]

    = 109.4 x Mmax / ( Efo x tr 3x KL x ln ( K ) )

    = 109.4 x 7500591.6 / ( 18786 x 148.4 3 x 0.2 x ln ( 1.095 ) )

    = 0.99

    Since J < 1.0, design is safe

    Assumed flange thickness tr 148.4 mm

    Modulus of elasticity for flange Efo 18786 kgf/mm

    Rigidity factor KL 0.2

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS ( Design Mode 1 , Uncorroded Condition )

    2. DESIGN CALCULATION AS PER UG-27

    Thickness of shell under internal pressure [ti]

    = Pi x R / ( S x E - 0.6 x Pi )

    = 0.09055 x 800 / ( 13.79 x 0.85 - 0.6 x 0.09055 )

    = 6.211 mm

    3. DESIGN CALCULATION OF SHELL THICKNESS UNDER EXTERNAL PRESSURE AS PER UG-28

    Allowable external pressure [Pa]

    = 4 x B / ( 3 x ( OD / te ) )

    = 4 x 5.516 / ( 3 x 120.9 )

    = 0.06086 kgf/mm g

    Since Pa > Pe, design is safe

    Since available thickness is more than design thickness, design is safe.

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    DESIGN OF SHELL ( INTERNAL AND EXTERNAL PRESSURE ) Main Shell

    CODE ASME VIII Div.1, 10 A11

    Design pressure ( internal ) Pi 0.09055 kgf/mm g

    Design pressure ( external ) Pe 0.06055 kgf/mm g

    Design temperature T 180 C

    Material of construction SA-240 GR. 316 Plt. [UNS:S31600]

    Max. allowable stress at design temp. S 13.79 kgf/mm

    Radiography Spot + T Joints

    Joint efficiency long. seam Ec 0.85

    Outside diameter OD 1628 mm

    Inside radius ( corroded ) R 800 mm

    Shell length L 2400 mm

    Design length L1 2400 mm

    Nominal thickness 14 mmNominal thickness required as per TEMA N.A. mm

    Internal allowance, corrosion + polishing 0 mm

    External allowance, corrosion + polishing 0 mm

    Thickness undertolerance 0 mm

    Available thickness 14 mm

    Assumed te 13.47 mm

    L1 / OD 1.474

    OD / te 120.9

    Factor A ( Refer to Fig. G in Subpart 3 of Sec. II, Part D ) 0.00067

    Factor B ( HA-2 ) 5.516 kgf/mm

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS ( Design Mode 1 , Uncorroded Condition ) :

    2. DESIGN CALCULATION AS PER UG 32 e / APPENDIX 1-4 ( d ) :

    Factor [M]

    = ( 1 / 4 ) x [ 3 + SQRT [ CR / KR ] ]

    = ( 1 / 4 ) x [ 3 + SQRT [ 1440 / 272 ] ]

    = 1.325

    Thickness for internal pressure [t]

    = M x Pi x CR / ( 2 x S x E - 0.2 x Pi )

    = 1.325 x 0.08 x 1440 / ( 2 x 13.79 x 1 - 0.2 x 0.08 )= 5.54 mm

    3. DESIGN CALCULATION AS PER UG 33 e :

    Thickness for equivalent external pressure [t]

    = M x 1.67 x Pe x CR / ( 2 x S x 1.0 - 0.2 x 1.67 x Pe )

    = 1.325 x 1.67 x 0.01055 x 1440 / ( 2 x 13.79 x 1.0 - 0.2 x 1.67 x 0.01055 )

    = 1.219 mm

    Assumed head thickness, [te]

    = 4.454 mm

    Assumed outside crown radius, [CRo]

    = 1448 mm

    Factor [A]

    = 0.125 x te / CRo

    = 0.125 x 4.454 / 1448

    = 0.00038

    Factor with reference to chart (HA-2) [B]

    = 3.455 kgf/mm

    Allowable external pressure [Pa]

    = B x te / CRo

    = 3.455 x 4.454 / 1448

    = 0.01063 kgf/mm

    Since Pa > Pe, design is safe

    Since available thickness is more than design thickness, design is safe.

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    DESIGN OF TORISPHERICAL HEAD ( INT. & EXT. PRESSURE ) Dished End (Rear)

    CODE ASME VIII Div.1, 10 A11

    Design pressure ( internal ) Pi 0.08 kgf/mm g

    Design pressure ( external ) Pe 0.01055 kgf/mm g

    Design temperature T 180 C

    Material of construction SA-240 GR. 316 Plt. [UNS:S31600]

    Max. allowable stress @ design temp. S 13.79 kgf/mm

    Radiography Full

    Joint efficiency E 1

    Outside diameter of head OD 1616 mm

    Crown radius CR 1440 mm

    Knuckle radius KR 272 mm

    Nominal thickness 8 mm

    Nominal thickness required as per TEMA N.A mmInternal allowance, corrosion + polishing 0 mm

    External allowance, corrosion + polishing 0 mm

    Thinning allowance / Under tolerance 0.8 mm

    Available thickness 7.2 mm

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS :

    2. SHELL DATA :

    3. JACKET DATA :

    4. MAX. ALLOWABLE WIDTH OF JACKET SPACE

    Maximum allowed jacket spacing [Jmax]

    = [ 4 x S x ts 2/ ( Pi x ID ) ] - 0.5 x ( ts + tj )

    = [ 4 x 12.9 x 14 2/ ( 0.05 x 1728 ) ] - 0.5 x ( 14 + 8 )

    = 106.1 mm.

    In this case J < Jmax , jacket width is acceptable.

    5. DESIGN CALCULATION AS PER 9.5 (c)(5) :

    Calculated thickness of closure member for pressure [t1]

    = 1.414 x SQRT [ 0.5 x OD1 x Pi x J / S ]

    = 1.414 x SQRT [ 0.5 x 1628 x 0.05 x 50 / 12.9 ]

    = 17.76 mmRequired minimum thickness of closure member [tr]

    = MAX [ t1 , trj ]

    = MAX [ 17.76 , 3.951 ]

    = 17.76 mm

    Since required minimum thickness of closure (tr) < available thickness of jacket closure (tc) , design is safe.

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    DESIGN OF JACKET CLOSURE Jacket Closure (Top)

    Code ASME VIII Div.1, 10 A11

    Design pressure ( INTERNAL ) Pi 0.05 kgf/mm g

    Design temperature T 200 C

    Material of construction SA-240 GR. 304 Plt. [UNS:S30400]

    Max. allowable stress @ design temp. S 12.9 kgf/mm

    Radiography Spot + T Joints

    Joint efficiency E 0.85

    Jacketing type Shell & Bottom End

    Closure type Figure (f2)

    Jacket spacing J 50 mm

    Nominal closure thickness t 18 mm

    Internal allowance, corrosion + polishing 0 mm

    External allowance, corrosion + polishing 0 mmAvailable thickness tc 18 mm

    Material of construction SA-240 GR. 316 Plt. [UNS:S31600]

    Outside diameter OD1 1628 mm

    Inside diameter ID1 1600 mm

    Provided thickness 14 mm

    Nominal thickness ts 14 mm

    Material of construction SA-240 GR. 304 Plt. [UNS:S30400]

    Outside diameter OD 1744 mm

    Inside diameter ID 1728 mm

    Provided thickness 8 mm

    Nominal thickness tj 8 mm

    Required minimum thickness of outer jacket wall trj 3.951 mm

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS ( Design Mode 1 , Uncorroded Condition )

    2. DESIGN CALCULATION AS PER UG-27

    Thickness of shell under internal pressure [ti]

    = Pi x R / ( S x E - 0.6 x Pi )

    = 0.05 x 864 / ( 12.9 x 0.85 - 0.6 x 0.05 )

    = 3.951 mm

    3. DESIGN CALCULATION OF SHELL THICKNESS UNDER EXTERNAL PRESSURE AS PER UG-28

    Allowable external pressure [Pa]

    = 4 x B / ( 3 x ( OD / te ) )

    = 4 x 2.272 / ( 3 x 284.6 )

    = 0.01064 kgf/mm g

    Since Pa > Pe, design is safe

    Since available thickness is more than design thickness, design is safe.

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    DESIGN OF SHELL ( INTERNAL AND EXTERNAL PRESSURE ) Jacket Shell

    CODE ASME VIII Div.1, 10 A11

    Design pressure ( internal ) Pi 0.05 kgf/mm g

    Design pressure ( external ) Pe 0.01055 kgf/mm g

    Design temperature T 200 C

    Material of construction SA-240 GR. 304 Plt. [UNS:S30400]

    Max. allowable stress at design temp. S 12.9 kgf/mm

    Radiography Spot + T Joints

    Joint efficiency long. seam Ec 0.85

    Outside diameter OD 1744 mm

    Inside radius ( corroded ) R 864 mm

    Shell length L 1850 mm

    Design length L1 1850 mm

    Nominal thickness 8 mmNominal thickness required as per TEMA N.A. mm

    Internal allowance, corrosion + polishing 0 mm

    External allowance, corrosion + polishing 0 mm

    Thickness undertolerance 0 mm

    Available thickness 8 mm

    Assumed te 6.128 mm

    L1 / OD 1.061

    OD / te 284.6

    Factor A ( Refer to Fig. G in Subpart 3 of Sec. II, Part D ) 0.00026

    Factor B ( HA-1 ) 2.272 kgf/mm

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN CONDITIONS ( Design Mode 1 , Uncorroded Condition ) :

    2. DESIGN CALCULATION AS PER UG 32 e / APPENDIX 1-4 ( d ) :

    Factor [M]

    = ( 1 / 4 ) x [ 3 + SQRT [ CR / KR ] ]

    = ( 1 / 4 ) x [ 3 + SQRT [ 1728 / 175 ] ]

    = 1.536

    Thickness for internal pressure [t]

    = M x Pi x CR / ( 2 x S x E - 0.2 x Pi )

    = 1.536 x 0.05 x 1728 / ( 2 x 12.9 x 1 - 0.2 x 0.05 )= 5.144 mm

    3. DESIGN CALCULATION AS PER UG 33 e :

    Thickness for equivalent external pressure [t]

    = M x 1.67 x Pe x CR / ( 2 x S x 1.0 - 0.2 x 1.67 x Pe )

    = 1.536 x 1.67 x 0.01055 x 1728 / ( 2 x 12.9 x 1.0 - 0.2 x 1.67 x 0.01055 )

    = 1.812 mm

    Assumed head thickness, [te]

    = 5.337 mm

    Assumed outside crown radius, [CRo]

    = 1736 mm

    Factor [A]

    = 0.125 x te / CRo

    = 0.125 x 5.337 / 1736

    = 0.00038

    Factor with reference to chart (HA-1) [B]

    = 3.456 kgf/mm

    Allowable external pressure [Pa]

    = B x te / CRo

    = 3.456 x 5.337 / 1736

    = 0.01062 kgf/mm

    Since Pa > Pe, design is safe

    Since available thickness is more than design thickness, design is safe.

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    DESIGN OF TORISPHERICAL HEAD ( INT. & EXT. PRESSURE ) Jacket Dish (Bottom)

    CODE ASME VIII Div.1, 10 A11

    Design pressure ( internal ) Pi 0.05 kgf/mm g

    Design pressure ( external ) Pe 0.01055 kgf/mm g

    Design temperature T 200 C

    Material of construction SA-240 GR. 304 Plt. [UNS:S30400]

    Max. allowable stress @ design temp. S 12.9 kgf/mm

    Radiography Full

    Joint efficiency E 1

    Outside diameter of head OD 1744 mm

    Crown radius CR 1728 mm

    Knuckle radius KR 175 mm

    Nominal thickness 8 mm

    Nominal thickness required as per TEMA N.A mmInternal allowance, corrosion + polishing 0 mm

    External allowance, corrosion + polishing 0 mm

    Thinning allowance / Under tolerance 0.8 mm

    Available thickness 7.2 mm

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. LUG DATA :

    2. BOLT DATA :

    3. GUSSET DATA :

    4. SHELL DATA :

    5. PAD DATA :

    6. LOAD AND MOMENT ( Wind ) :

    7. DESIGN OF ANCHOR BOLTS :

    Total uplift force on bolts [T]

    = [ 4 x M / ( D x N ) ] - Wt / N

    = [ 4 x 2107478.2 / ( 1928 x 4 ) ] - 6175 / 4

    = -450.7 kgf

    Required area of bolts [Am]

    = MAX [ ( T / Fs ) , 0 ]

    = MAX [ ( -450.7 / 20.88 ) , 0 ]

    = 0 mm

    Available area of bolts [Ab]

    = Ar x Nb ........................................................................................ where, Ar = 217.1 mm, is root area of bolt= 217.1 x 2

    = 434.1 mm

    Since Ab > Am, bolts provided are sufficient

    8. GUSSET DESIGN :

    Reaction force at each support [Q]

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    LUG SUPPORT DESIGN Lug Support

    CODE P V Design Manual, D.R. Moss

    Design Mode 1 , Uncorroded

    Condition

    M.O.C IS-2062 GR. A Plt.

    No. of support N 4

    Base plate width b1 42 mm

    Base plate depth Lb 220 mm

    Thickness of base plate tb 16 mm

    Allowable bending stress Sb 22.15 kgf/mm

    M.O.C SA-36 / IS-1363,67 Bolt [UNS:K02600]

    No. of bolt / lug Nb 2

    Bolt diameter db 20 mm

    PCD D 1928 mm

    Diameter of bolt hole 24 mm

    Allowable tensile stress Fs 20.88 kgf/mm

    Thickness tg 16 mm

    Height h 240 mm

    Gusset angle ! 54.69

    Gusset depth at top Lc 50 mm

    Number of gussets n 1

    Distance between gussets b 0 mm

    Material SA-240 GR. 316 Plt. [UNS:S31600]

    OD diameter OD 1628 mm

    Inside diameter ID 1600 mm

    Thickness available ts 14 mm

    Material SA-240 GR. 316 Plt. [UNS:S31600]

    Thickness tp 14 mm

    Width W 330 mm

    Length L 300 mm

    Max. overturning moment M 2107478.2 kgf-mm

    Design weight of vessel Wt 6175 kgf

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    = [ 4 x M / ( D x N ) ] + Wt / N

    = [ 4 x 2107478.2 / ( 1928 x 4 ) ] + 6175 / 4

    = 2636.8 kgf

    Maximum axial force in gusset [P1]

    = Q

    = 2636.8

    = 2636.8 kgf

    Allowable compr. stress in gusset [Sg]

    = 1800 / [ ( 1 + 12 / 18000 ) x ( h / tg ) 2] ....................................... where, h = 294.1 mm

    = 1800 / [ ( 1 + 12 / 18000 ) x ( 294.1 / 16 ) 2]

    = 14690.8 psi

    = 10.33 kgf/mm

    Required thickness of gusset [tg]

    = 2 x P1 x ( 3 x a - Lb ) / [ Sg x Lb 2x ( sin !) 2]

    = 2 x 2636.8 x ( 3 x 150 - 220 ) / [ 10.33 x ( 220 ) 2x ( sin 54.69 ) 2]

    = 3.644 mm

    9. BASE PLATE DESIGN :

    Bending moment [Mb]

    = Q x b1 / 4

    = 2636.8 x 42 / 4

    = 27686.9 kgf-mmBearing pressure [bp]

    = Q / ( w x b1 ) ............................................................................... where, w = 132 mm

    = 2636.8 / ( 132 x 42 )

    = 0.476 kgf/mm

    Bending moment due to bearing pressure [Mb]

    = bp x b 2/ 2

    = 0.476 x 0 2/ 2

    = 40.19 kgf-mm

    Required thickness of base plate between chairs [tb]

    = SQRT { 6 x MAX [ Mb , Mb' ] / [ ( Lb - db ) x Sb ] }

    = SQRT { 6 x MAX [ 27686.9 , 40.19 ] / [ ( 220 - 20 ) x 22.15 ] }

    = 6.186 mm

    10. CHECK FOR COMPRESSION PLATE :

    Equivalent radial load [f]

    = Q x a / h

    = 2636.8 x 150 / 240

    = 1648 kgf

    Angle between supports [b]

    = 2 x p/ N

    = 2 x p/ 4

    = 1.571 rad

    Internal bending moment coefficient [Kr]

    = 0.5 x [ 1 / a - cot (a) ]= 0.5 x [ 1 / 1.571 - cot ( 1.571 ) ]

    = 0.318

    Internal bending moment [Mc]

    = 0.5 x Kr x f x OD

    = 0.5 x 0.318 x 1648 x 1628

    = 427011.1 kgf-mm

    Bending stress induced [fb]

    = Mo / Zc

    = 427011.1 / 30687.7

    = 13.91 kgf/mm ......................................................................... < Sb = 22.15 kgf/mm

    Since, induced stress fb < allow. stress Sb in shell material, design is safe.

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. LUG DATA :

    2. BOLT DATA :

    3. GUSSET DATA :

    4. SHELL DATA :

    5. PAD DATA :

    6. LOAD AND MOMENT ( Seismic ) :

    7. DESIGN OF ANCHOR BOLTS :

    Total uplift force on bolts [T]

    = [ 4 x M / ( D x N ) ] - Wt / N

    = [ 4 x 1923130.8 / ( 1928 x 4 ) ] - 4385.1 / 4

    = -98.79 kgf

    Required area of bolts [Am]

    = MAX [ ( T / Fs ) , 0 ]

    = MAX [ ( -98.79 / 20.88 ) , 0 ]

    = 0 mm

    Available area of bolts [Ab]

    = Ar x Nb ........................................................................................ where, Ar = 217.1 mm, is root area of bolt= 217.1 x 2

    = 434.1 mm

    Since Ab > Am, bolts provided are sufficient

    8. GUSSET DESIGN :

    Reaction force at each support [Q]

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    LUG SUPPORT DESIGN Lug Support

    CODE P V Design Manual, D.R. Moss

    Design Mode 1 , Uncorroded

    Condition

    M.O.C IS-2062 GR. A Plt.

    No. of support N 4

    Base plate width b1 42 mm

    Base plate depth Lb 220 mm

    Thickness of base plate tb 16 mm

    Allowable bending stress Sb 22.15 kgf/mm

    M.O.C SA-36 / IS-1363,67 Bolt [UNS:K02600]

    No. of bolt / lug Nb 2

    Bolt diameter db 20 mm

    PCD D 1928 mm

    Diameter of bolt hole 24 mm

    Allowable tensile stress Fs 20.88 kgf/mm

    Thickness tg 16 mm

    Height h 240 mm

    Gusset angle ! 54.69

    Gusset depth at top Lc 50 mm

    Number of gussets n 1

    Distance between gussets b 0 mm

    Material SA-240 GR. 316 Plt. [UNS:S31600]

    OD diameter OD 1628 mm

    Inside diameter ID 1600 mm

    Thickness available ts 14 mm

    Material SA-240 GR. 316 Plt. [UNS:S31600]

    Thickness tp 14 mm

    Width W 330 mm

    Length L 300 mm

    Max. overturning moment M 1923130.8 kgf-mm

    Design weight of vessel Wt 4385.1 kgf

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    = [ 4 x M / ( D x N ) ] + Wt / N

    = [ 4 x 1923130.8 / ( 1928 x 4 ) ] + 4385.1 / 4

    = 2093.7 kgf

    Maximum axial force in gusset [P1]

    = Q

    = 2093.7

    = 2093.7 kgf

    Allowable compr. stress in gusset [Sg]

    = 1800 / [ ( 1 + 12 / 18000 ) x ( h / tg ) 2] ....................................... where, h = 294.1 mm

    = 1800 / [ ( 1 + 12 / 18000 ) x ( 294.1 / 16 ) 2]

    = 14690.8 psi

    = 10.33 kgf/mm

    Required thickness of gusset [tg]

    = 2 x P1 x ( 3 x a - Lb ) / [ Sg x Lb 2x ( sin !) 2]

    = 2 x 2093.7 x ( 3 x 150 - 220 ) / [ 10.33 x ( 220 ) 2x ( sin 54.69 ) 2]

    = 2.893 mm

    9. BASE PLATE DESIGN :

    Bending moment [Mb]

    = Q x b1 / 4

    = 2093.7 x 42 / 4

    = 21984.3 kgf-mmBearing pressure [bp]

    = Q / ( w x b1 ) ............................................................................... where, w = 132 mm

    = 2093.7 / ( 132 x 42 )

    = 0.378 kgf/mm

    Bending moment due to bearing pressure [Mb]

    = bp x b 2/ 2

    = 0.378 x 0 2/ 2

    = 31.91 kgf-mm

    Required thickness of base plate between chairs [tb]

    = SQRT { 6 x MAX [ Mb , Mb' ] / [ ( Lb - db ) x Sb ] }

    = SQRT { 6 x MAX [ 21984.3 , 31.91 ] / [ ( 220 - 20 ) x 22.15 ] }

    = 5.513 mm

    10. CHECK FOR COMPRESSION PLATE :

    Equivalent radial load [f]

    = Q x a / h

    = 2093.7 x 150 / 240

    = 1308.6 kgf

    Angle between supports [b]

    = 2 x p/ N

    = 2 x p/ 4

    = 1.571 rad

    Internal bending moment coefficient [Kr]

    = 0.5 x [ 1 / a - cot (a) ]= 0.5 x [ 1 / 1.571 - cot ( 1.571 ) ]

    = 0.318

    Internal bending moment [Mc]

    = 0.5 x Kr x f x OD

    = 0.5 x 0.318 x 1308.6 x 1628

    = 339060.9 kgf-mm

    Bending stress induced [fb]

    = Mo / Zc

    = 339060.9 / 30687.7

    = 11.05 kgf/mm ......................................................................... < Sb = 22.15 kgf/mm

    Since, induced stress fb < allow. stress Sb in shell material, design is safe.

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. SHAFT DATA :

    2. IMPELLER TORQUE, FORCES AND MOMENTS :

    Formulae used in the above table :

    Tm(i) = [ 736 x 60 x HP(i) / ( 9.81 x 2 x px RPM ) ] kgf-m = [ 716440.6 x P(i) / RPM ] kgf-mm

    F(i) = Tm(i) / ( 0.75 x Rb ) kgf

    M(i) = F(i) x L(i) kgf-mm

    M'(i) = F(i) x ( L - L(i) ) kgf-mm

    M"(i) = F(i) x ( L - L(i) ) 3kgf-mm 3

    3. CHECK FOR EQUIVALENT BENDING MOMENT

    Reaction at top bearing [R1]

    = [ M" - M' x L 2] / [ 2 x A x L x ( A + L ) ]

    = [ 146.8E09 - 424140.7 x 3738.3 2] / [ 2 x 250 x 3738.3 x ( 250 + 3738.3 ) ]

    = -775.4 kgf

    Reaction at bottom bearing [R2]

    = [ - M' - R1 x ( A + L ) ] / L

    = [ - 424140.7 - -775.4 x ( 250 + 3738.3 ) ] / 3738.3

    = 713.8 kgf

    Reaction at bush [R3]

    = - [ R1 + R2 + F ]

    = - [ -775.4 + 713.8 + 720.9 ]

    = -659.3 kgf

    Bending moment at the bottom bearing [Mt]

    = M + R3 x L

    = 2270981.5 + -659.3 x 3738.3

    = -193854.1 kgf-mm

    Induced equivalent moment in shaft [Me]

    = ( Mt 2+ 0.75 x Tm 2) 0.5

    = ( -193854.1 2+ 0.75 x 143288.1 2) 0.5

    = 230169.6 kgf-mm

    Stress induced in shaft [Fy]

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    AGITATOR SHAFT WITH INTERMEDIATE BEARING HOUSING Shaft

    Power P 20 hp (MKS)

    Pumping capacity (RPM) RPM 100

    Service (Duty) factor sf 2

    Material of impeller SA-479 GR. 316 Bar [UNS:S31600]

    0.2% Proof stress Sy 21.09 kgf/mm

    Allowable stress Sa 14.05 kgf/mm

    Youngs modulus Es 18786 kgf/mm

    Weight density rho 7999.5 kg/m

    Shaft OD OD 101 mm

    Shaft ID ID 0 mm

    Total length 4438.3 mm

    Allowance CA 0 mm

    Shaft is propped at bottom TrueDistance between bearings A 250 mm

    Overhanging length L 3738.3 mm

    Type of shaft seal Gland Packing

    Distance of packing /seal Y 300 mm

    Allowable deflection at packing 0.5 mm

    Impeller Length, Power, Radius, Torque, Force, Moment, Moment, Moment,

    HubNo

    L(i) mmP(i) hp(MKS)

    Rb(i) mmTm(i) kgf-mm

    F(i) kgf M(i) kgf-mm M'(i) kgf-mmM''(i) kgf-

    mm3

    1 3150 20 265 143288.1 720.9 2270981.5 424140.7 146.8E09

    2

    3

    4

    5

    P = 20Tm =

    143288.1F = 720.9

    M =

    2270981.5

    M' =

    424140.7

    M" =

    146.8E09

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    = ( 32 x sf x Me x D1 ) / [ px ( D1 4 - ID 4) ] .......................... where, assumed D1 = 60.58 mm

    = ( 32 x 2 x 230169.6 x 60.58 ) / [ px ( 60.58 4 - 0 4) ]

    = 21.09 kgf/mm

    Since induced stress (Fy)

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. DESIGN DATA :

    2. SHAFT DATA :

    3. BLADE DATA :

    4. CALCULATION OF BLADE THICKNESS

    Torsional moment on shaft [Tm]

    = 736 x 60 x H.P. / ( 9.81 x 2 x px RPM ) kg-m

    = 716440.6 x P / RPM kgf-mm

    = 716440.6 x 20 / 100

    = 143288.1 kgf-mm

    Effective force on blade [Fm]= Tm / ( 0.75 x Rb )

    = 143288.1 / ( 0.75 x 265 )

    = 720.9 kgf

    Minimum blade thickness required [tb]

    = SQRT [ 6 x sf x Tm / ( Nb x d x Sa ) ]

    = SQRT [ 6 x 2 x 143288.1 / ( 4 x 125 x 21.09 ) ]

    = 12.77 mm

    Since the calculated thickness 12.77 mm is less that provided thickness 14 mm of blade, blade thickness is adequate.

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    DESIGN OF IMPELLER BLADE WITH STIFFENER : Impeller (1)

    Power P 20 hp (MKS)

    Pumping capacity (RPM) RPM 100

    Service (Duty) factor sf 2

    Material of impeller SA-240 GR. 316 Plt. [UNS:S31600]

    0.2% Proof stress Sy 21.09 kgf/mm

    Youngs modulus Es 18786 kgf/mm

    Weight density r 7999.5 kg/m

    Allowance CA 0 mm

    Shaft OD at Impeller OD 101 mm

    Total length L 3150 mm

    Type of impellerImpellar radius R 265 mm

    Distance of impeller from bottom bearing c 3150 mm

    No of blades Nb 4 mm

    Width of blade w 125 mm

    Blade thickness tb 14 mm

    Blade angle a 0

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    1. LIFTING LUG DATA :

    2. DESIGN LOADS :

    3. CALCULATION OF REFERENCE DIMENSIONS :

    4. DESIGN OF LUG PLATE :

    5. CALCULATION OF STRESSES IN LUG PLATE WELDS :

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    DESIGN OF LIFTING LUG Lifting Lugs

    CODE P V Design Manual, D.R. Moss

    Design Mode 1 , Uncorroded

    Condition

    Material IS-2062 GR. A Plt.

    Length of lug LL 77 mm

    Width of lug A 135 mm

    Thickness of lug plate TL 28 mm

    Straight length B1 10 mm

    Radius at tip R3 40 mm

    Pin Hole diameter D1 50 mm

    Lug to vessel weld size W1 10.22 mm

    Min yield stress Sy 24.61 kgf/mm

    Allowable tensile stress ( 2 / 3 x Sy ) St 16.4 kgf/mm

    Allowable bending stress ( 1.5 x St ) Sb 22.15 kgf/mm

    Allowable shear stress (0.6 x St ) Ss 9.843 kgf/mm

    Empty weight of equipment Wt 5065.2 kgf

    Number of lifting lugs N 2

    Jirk load factor j 1.5

    Dimension [ L1 ]

    = LL - B1 - R3

    = 77 - 10 - 40

    = 27 mm

    Dimension [ L2 ]

    = L1 / SIN ( q1 )

    = 27 / SIN ( 0.381 )

    = 72.7 mm

    Dimension [ LT ]= LL - R3

    = 77 - 40

    = 37 mm

    Angle [ q2 ]= ASIN ( R3 / L2 )

    = ASIN ( 40 / 72.7 )

    = 0.583 radians

    Angle [q1 ]

    = ATAN ( 2 x L1 / A )

    = ATAN ( 2 x 27 / 135 )

    = 0.381 radians

    Angle [ q3 ]

    = q1 + q2

    = 0.381 + 0.583

    = 0.963 radians

    Dimension [ L3 ]

    = R3 / SIN ( q3 )

    = 40 / SIN ( 0.963 )

    = 48.72 mm

    Effective design load on each lug [ P ]

    = j x Wt / N

    = 1.5 x 5065.2 / 2

    = 3798.9 kgf

    Required min. thickness of lug plate for shear [ t2 ]

    = P / [ ( R3 - 0.5 x D1) x ss ]

    = 3798.9 / [ ( 40 - 0.5 x 50 ) x 9.843 ]

    = 25.73 mm

    Required min. thickness of lug plate for bending [ t1 ]

    = 6 x P x LT / ( A 2x Sb )

    = 6 x 3798.9 x 37 / ( 135 2x 22.15 )

    = 2.089 mm

    Required min. thickness of lug plate for shear [ t3 ]

    = P / [ ( 2 x L3 - D1 ) x ss ]

    = 3798.9 / [ ( 2 x 48.72 - 50 ) x 9.843 ]

    = 4.881 mm

    Bending stress in weld [ f1 ]

    = 6 x P x LT / [ 2 x LL2

    ]= 6 x 3798.9 x 37 / ( 2 x 77 2)

    = 71.12 kgf/mm

    Max. shear stress in weld [ f2 ]

    = P / [ 2 x A ]= 3798.9 / ( 2 x 135 )

    = 14.07 kgf/mm

    Min. Size of lug plate weld [ w1 ]

    = MAX ( f1 , 2 x f2 ) / ( 0.707 x Ss )

    = MAX ( 71.12 , 2 x 14.07 ) / ( 0.707 x 9.843 )

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    = 10.22 mm

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    FOUNDATION LOAD DATA

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    Sr.

    No.

    Mode Condition

    Weight ( kgf ) Wind Seismic

    Empty Filled

    Shear ( kgf ) Moment ( kgf-m ) Shear Moment

    Tran. Long. Tran. Long. ( kgf ) ( kgf-m )

    1 Operating Uncorroded 5065.2 10988.8 1273.2 1273.2 2107.5 2107.5 1136.8 1534.9

    2 Design1 Uncorroded 5065.2 11231.4 1273.2 1273.2 2107.5 2107.5 1161.9 1566.5

    3 Hydro Uncorroded 4798.1 10964.4 1273.2 1273.2 2107.5 2107.5 1134.2 1529.2

    4 Pneumatic Uncorroded 4798.1 4805.5 1273.2 1273.2 2107.5 2107.5 497.1 822.3

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    'CademPVD' Version 14.91 by CADEM Softwares , Pune , Website www.cadem.in

    CENTER OF GRAVITY DATA

    Licensee :Sunay Wagle, CADEM Services,

    Pune, India

    Customer ABC Company Ltd.

    Project / Equipment Soap Plant / Reactor R101

    Designed By / Revision and Date / R00 , 06-04-2015 19:23:54

    Sr.

    No.Mode Condition

    Empty Operating / Filled

    Wt ( kgf ) C.G. ( mm ) Wt ( kgf ) C.G. ( mm )

    1 Operating Uncorroded 5065.2 2111.4 10988.8 1806.42 Design1 Uncorroded 5065.2 2111.4 11231.4 1804.4

    3 Hydro Uncorroded 4798.1 2111.4 10964.4 1804.4

    4 Pneumatic Uncorroded 4798.1 2111.4 4805.5 2110.2