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    CONSTRUCTORA HOSTOTIPAQUILLO

    CARRETERA TULA - BOJAY, S/N, KM.0+300PARQUE INDUSTRIAL ATITALAQUIA.

    ATITALAQUIA, HGO . MXICO

    COMPRESS Pressure Vessel Design Calculations

    EQUIPO: SEGUNDO ENFRIADOR DE FONDOS DEL AGOTADORTAG: MT-1-EA-3005-A

    CLIENTE : PEMEXZ REFINACIN, AGUAS AMARGAS CD. MADERO

    CONTRATO:

    DISEADOR : RICARDO BARCENAS

    FECHA: 29 OCT. 2013

    You can edit this page by selecting Cover Page settings...in the reportmenu.

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    Table of ContentsGeneral Arrangement Drawing..............................................................................................................................1/229

    Deficiencies Summary............................................................................................................................................2/229

    Nozzle Schedule......................................................................................................................................................3/229

    Nozzle Summary.....................................................................................................................................................4/229

    Pressure Summary.................................................................................................................................................5/229

    Revision History......................................................................................................................................................9/229

    Settings Summary.................................................................................................................................................10/229

    Radiography Summary.........................................................................................................................................12/229

    Thickness Summary.............................................................................................................................................14/229

    Weight Summary...................................................................................................................................................15/229

    Long Seam Summary...........................................................................................................................................17/229

    Test Report............................................................................................................................................................19/229

    Vacuum Summary.................................................................................................................................................21/229

    ENVOLVENTE CANAL..........................................................................................................................................22/229

    ENVOLVENTE 1.....................................................................................................................................................24/229

    ENVOLVENTE 2.....................................................................................................................................................27/229

    Rear Shell Cylinder...............................................................................................................................................30/229

    TAPA BRIDADA CANAL.......................................................................................................................................33/229

    Straight Flange on Rear Shell Head....................................................................................................................34/229

    Rear Shell Head.....................................................................................................................................................37/229

    BRIDA BIPARTIDA................................................................................................................................................39/229

    BRIDA BONET -- CUERPO....................................................................................................................................44/229

    BRIDA CANAL --ESPEJO......................................................................................................................................51/229

    BRIDA CUERPO -- BONETE.................................................................................................................................58/229

    BRIDA CUERPO ESPEJO FIJO............................................................................................................................65/229

    BRIDA TAPA DEL CANAL....................................................................................................................................72/229

    IP1 INSTRUMENTO DE PRESION (IP1)................................................................................................................79/229

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    Tableof ContentsIP2 INSTRUMENTO DE PRESION (IP2)................................................................................................................84/229

    IP3 INSTRUMENTO DE PRESION (IP3)................................................................................................................89/229

    IP4 INSTRUMENTO DE PRESION (IP4)................................................................................................................94/229

    IT1 INDICADOR DE TEMPERATURA (IT1)...........................................................................................................99/229

    IT2 INSTRUMENTO DE TEMPERATUIRA (IT2)..................................................................................................104/229

    IT3 INSTRUMENTO DE TEMPERATUIRA (IT3)..................................................................................................109/229

    IT4 INSTRUMENTO DE TEMPERATURA (IT4)...................................................................................................114/229

    N1 ENTRADA DEL FONDO DEL AGOTADOR (N1)...........................................................................................119/229

    N2 INTERCONEXION DE ENVOLVENTE (N2)...................................................................................................127/229

    N5 INTERCONEXION DE CANALES (N5)..........................................................................................................135/229

    N6 SALIDA DE AGUA DE ENFRIAMIENTO (N6)...............................................................................................143/229

    N7A CONEXION PARA LIMPIEZA QUIMICA (N7A)...........................................................................................151/229

    N7B CONEXION PARA LIMPIEZA QUIMICA (N7B)...........................................................................................157/229

    SILLETA...............................................................................................................................................................163/229

    Baffle Summary Report......................................................................................................................................169/229

    Data Inputs Summary.........................................................................................................................................170/229

    Design Conditions Summary.............................................................................................................................171/229

    Front Stationary Tubesheet -- ASME.................................................................................................................172/229

    Materials and Gaskets Summary.......................................................................................................................196/229

    TEMA RCB-9.132 Pass Partition Plate Calculations........................................................................................198/229

    Rear Floating Tubesheet -- ASME......................................................................................................................199/229

    Shell side liquid level..........................................................................................................................................214/229

    TAPA FLOTANTE................................................................................................................................................215/229

    Tube side liquid level..........................................................................................................................................224/229

    Tubes....................................................................................................................................................................225/229

    Tubesheet Maximum Pressure Report..............................................................................................................227/229

    Front Stationary Tubesheet -- TEMA.................................................................................................................228/229

    i

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    General Arrangement Drawing

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    Deficiencies Summary

    No deficiencies found.

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    Nozzle Schedule

    Nozzlemark

    Service Size MaterialsImpactTested

    NormalizedFineGrain

    Flange Blind

    IP1 IP1 INSTRUMENTO DE PRESIONNPS 0.5 Class 6000 DN 15 -threaded

    Nozzle SA-105 No No No N/A No

    IP2 IP2 INSTRUMENTO DE PRESIONNPS 0.5 Class 6000 DN 15 -threaded

    Nozzle SA-105 No No No N/A No

    IP3 IP3 INSTRUMENTO DE PRESIONNPS 0.5 Class 6000 DN 15 -threaded

    Nozzle SA-105 No No No N/A No

    IP4 IP4 INSTRUMENTO DE PRESIONNPS 0.5 Class 6000 DN 15 -threaded

    Nozzle SA-105 No No No N/A No

    IT1IT1 INDICADOR DETEMPERATURA

    NPS 0.5 Class 6000 DN 15 -threaded

    Nozzle SA-105 No No No N/A No

    IT2IT2 INSTRUMENTO DETEMPERATUIRA

    NPS 0.5 Class 6000 DN 15 -threaded

    Nozzle SA-105 No No No N/A No

    IT3IT3 INSTRUMENTO DETEMPERATUIRA

    NPS 0.5 Class 6000 DN 15 -threaded

    Nozzle SA-105 No No No N/A No

    IT4IT4 INSTRUMENTO DETEMPERATURA

    NPS 0.5 Class 6000 DN 15 -threaded

    Nozzle SA-105 No No No N/A No

    N1N1 ENTRADA DEL FONDO DELAGOTADOR

    NPS 6 Sch 80 (XS) DN 150 NozzleSA-106 B Smls.Pipe

    No No NoNPS 6 Class150WN A105

    No

    N2N2 INTERCONEXION DEENVOLVENTE

    NPS 6 Sch 80 (XS) DN 150 NozzleSA-106 B Smls.Pipe

    No No NoNPS 6 Class150WN A105

    No

    N5 N5 INTERCONEXION DE CANALES NPS 6 Sch 80 (XS) DN 150 NozzleSA-106 B Smls.Pipe

    No No NoNPS 6 Class150WN A105

    No

    N6N6 SALIDA DE AGUA DEENFRIAMIENTO

    NPS 6 Sch 80 (XS) DN 150 NozzleSA-106 B Smls.Pipe

    No No NoNPS 6 Class150WN A105

    No

    N7AN7A CONEXION PARA LIMPIEZAQUIMICA

    NPS 2 Sch 160 DN 50 NozzleSA-106 B Smls.Pipe

    No No NoNPS 2 Class150WN A105

    No

    N7BN7B CONEXION PARA LIMPIEZAQUIMICA

    NPS 2 Sch 160 DN 50 NozzleSA-106 B Smls.Pipe

    No No NoNPS 2 Class150WN A105

    No

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    Nozzle Summary

    Nozzlemark

    OD(mm)

    tn

    (mm)Req t

    n(mm)

    A1? A2?

    ShellReinforcement

    Pad Corr(mm)

    Aa/A

    r(%)

    Nom t(mm)

    Design t(mm)

    User t(mm)

    Width(mm)

    tpad

    (mm)

    IP1 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt

    IP2 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt

    IP3 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt

    IP4 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt

    IT1 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt

    IT2 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt

    IT3 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt

    IT4 38.1 8.38 4.7 Yes Yes 10.97 N/A N/A N/A 3.2 Exempt

    N1 168.27 10.97 8.33 Yes Yes 9.5 7.29 N/A N/A 3.2 100.0

    N2 168.27 10.97 8.33 Yes Yes 9.5 7.29 N/A N/A 3.2 100.0

    N5 168.27 10.97 8.32 Yes Yes 9.5 7.28 N/A N/A 3.17 100.0

    N6 168.27 10.97 8.32 Yes Yes 9.5 7.28 N/A N/A 3.17 100.0

    N7A 60.33 8.74 5.34 Yes Yes 10.97 N/A N/A N/A 3.17 Exempt

    N7B 60.33 8.74 5.34 Yes Yes 10.97 N/A N/A N/A 3.17 Exempt

    tn: Nozzle thickness

    Req tn: Nozzle thickness required per UG-45/UG-16Nom t: Vessel wall thickness

    Design t: Required vessel wall thickness due to pressure + corrosion allowance per UG-37

    User t: Local vessel wall thickness (near opening)Aa: Area available per UG-37, governing condition

    Ar: Area required per UG-37, governing condition

    Corr: Corrosion allowance on nozzle wall

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    Pressure Summary

    Pressure Summary for Tube side chamber

    IdentifierP

    Design( kg/cm2)

    T

    Design( C)

    MAWP( kg/cm2)

    MAP( kg/cm2)

    MAEP( kg/cm2)

    Te

    external( C)

    MDMT( C)

    MDMTExemption

    ImpactTested

    TAPA BRIDADA CANAL 7 66 8.3 8.36 N/A 66 -48 Note 1 No

    ENVOLVENTE CANAL 7 66 27.39 41.36 N/A 66 -105 Note 2 No

    Front Stationary Tubesheet(seeMaximum PressureRating note)

    7 90 16.16 17.97 11.51 90 -48 Note 3 No

    Rear Floating Tubesheet(see Maximum PressureRating note)

    7 90 16.16 17.97 11.51 90 -48 Note 3 No

    TAPA FLOTANTE 7 90 15.38 15.66 17 90 -48 Note 4 No

    Tubes 7 90 198.3 198.36 125.47 90 -105 Note 5 No

    BRIDA TAPA DEL CANAL 7 66 16.27 23.86 N/A 66 -48 Note 6 No

    BRIDA TAPA DEL CANAL - Flange Hub 7 66 27.39 41.36 N/A 66 -105 Note 2 No

    BRIDA CANAL --ESPEJO 7 66 16.7 23.86 N/A 66 -48 Note 6 No

    BRIDA CANAL --ESPEJO - Flange Hub 7 66 27.39 41.36 N/A 66 -105 Note 2 No

    BRIDA BIPARTIDA 7 90 14.51 14.51 70.24 90 -44.58 Note 7 No

    IP2 INSTRUMENTO DE PRESION (IP2) 7 66 96.5 146.38 N/A 66 -105 Note 8 No

    IP3 INSTRUMENTO DE PRESION (IP3) 7 66 96.43 146.38 N/A 66 -105 Note 9 No

    IT2 INSTRUMENTO DE TEMPERATUIRA (IT2) 7 66 96.5 146.38 N/A 66 -105 Note 8 No

    IT3 INSTRUMENTO DE TEMPERATUIRA (IT3) 7 66 96.43 146.38 N/A 66 -105 Note 9 No

    N5 INTERCONEXION DE CANALES (N5) 7 66 17.84 19.99 N/A 66 -48 Note 10 No

    N6 SALIDA DE AGUA DE ENFRIAMIENTO (N6) 7 66 17.91 19.99 N/A 66 -48 Note 10 No

    N7A CONEXION PARA LIMPIEZA QUIMICA (N7A) 7 66 19.09 19.99 N/A 66 -48 Note 10 No

    N7B CONEXION PARA LIMPIEZA QUIMICA (N7B) 7 66 19.02 19.99 N/A 66 -48 Note 10 No

    Chamber design MDMT is -17.78 C

    Chamber rated MDMT is -44.58 C @ 8.3 kg/cm2

    Chamber MAWP hot & corroded is 8.3 kg/cm2@ 66 C

    Chamber MAP cold & new is 8.36 kg/cm2@ 21.11 C

    This pressure chamber is not designed for external pressure.

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    Pressure Summary for Shell side chamber

    IdentifierP

    Design( kg/cm2)

    T

    Design( C)

    MAWP( kg/cm2)

    MAP( kg/cm2)

    MAEP( kg/cm2)

    Te

    external( C)

    MDMT( C)

    MDMTExemption

    ImpactTested

    Front Stationary Tubesheet(seeMaximum PressureRating note)

    11.5 90 11.51 13.32 16.16 90 -48 Note 3 No

    ENVOLVENTE 1 11.5 90 27.26 41.36 N/A 90 -48 Note 11 No

    ENVOLVENTE 2 11.5 90 27.26 41.36 N/A 90 -48 Note 11 NoRear Shell Cylinder 11.5 90 24.39 37.01 N/A 90 -48 Note 12 No

    Straight Flange on Rear Shell Head 11.5 90 24.39 37.01 N/A 90 -48 Note 12 No

    Rear Shell Head 11.5 90 24.9 37.5 N/A 90 -48 Note 13 No

    Rear Floating Tubesheet(see Maximum PressureRating note)

    11.5 90 11.51 13.32 16.16 90 -48 Note 3 No

    TAPA FLOTANTE 11.5 90 17 31.36 15.38 90 N/A Note 14 No

    BRIDA BIPARTIDA 11.5 90 70.24 70.24 14.51 90 -44.58 Note 7 No

    Tubes 11.5 90 125.47 125.47 198.3 90 N/A N/A No

    BRIDA CUERPO ESPEJO FIJO 11.5 90 16.84 24.06 N/A 90 -48 Note 15 No

    BRIDA CUERPO ESPEJO FIJO - Flange Hub 11.5 90 27.39 41.36 N/A 90 -48 Note 16 No

    BRIDA CUERPO -- BONETE 11.5 90 11.67 14.77 N/A 90 -48 Note 17 No

    BRIDA CUERPO -- BONETE - Flange Hub 11.5 90 27.39 41.36 N/A 90 -48 Note 16 No

    SILLETA 11.5 90 11.51 N/A N/A N/A N/A N/A N/A

    BRIDA BONET -- CUERPO 11.5 90 11.66 14.77 N/A 90 -48 Note 17 No

    BRIDA BONET -- CUERPO - Flange Hub 11.5 90 24.51 37.01 N/A 90 -48 Note 18 No

    IP1 INSTRUMENTO DE PRESION (IP1) 11.5 90 96.03 146.38 N/A 90 -105 Note 19 No

    IP4 INSTRUMENTO DE PRESION (IP4) 11.5 90 95.96 146.38 N/A 90 -105 Note 20 No

    IT1 INDICADOR DE TEMPERATURA (IT1) 11.5 90 96.03 146.38 N/A 90 -105 Note 19 No

    IT4 INSTRUMENTO DE TEMPERATURA (IT4) 11.5 90 95.96 146.38 N/A 90 -105 Note 20 No

    N1 ENTRADA DEL FONDO DEL AGOTADOR (N1) 11.5 90 17.82 19.99 N/A 90 -48 Note 21 No

    N2 INTERCONEXION DE ENVOLVENTE (N2) 11.5 90 17.75 19.99 N/A 90 -48 Note 22 No

    Chamber design MDMT is -17.78 CChamber rated MDMT is -44.58 C @ 11.51 kg/cm2

    Chamber MAWP hot & corroded is 11.51 kg/cm2@ 90 CMAWPis the maximum allowable shell side pressure for the component.

    Chamber MAP cold & new is 13.32 kg/cm2@ 21.11 C

    This pressure chamber is not designed for external pressure.

    Notes for Maximum Pressure Rating:

    Note # Details

    1.The largest tubesheet MAWP/MAP values have been selected from the multiple design conditions to maximize the hydrotest pressure and to complywith UG-20(b). The MAWP/MAP selected for the shell side may not be coincident with the MAWP/MAP selected for the tube side (and vice versa).

    2.The chamber MAWP listed above is based on the largest tubesheet MAWP values from the multiple design conditions. The lowest tubesheet MAWPvalues should be considered when determining the final chamber MAWP. Refer to the Tubesheet Maximum Pressure Reportfor the lowest tubesheetmaximum pressure ratings.

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    Notes for MDMT Rating:

    Note # Exemption Details

    1.Bolted cover impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.Rated MDMT of -65C is limited to -48C by UCS-66(b)(2)

    UCS-66 governing thickness = 8 mm

    2. Material is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.302)

    3.Tubesheet impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.Rated MDMT of -65C is limited to -48C by UCS-66(b)(2)

    UCS-66 governing thickness = 9.23 mm

    4.

    impact test exemption temperature from Fig UCS-66M Curve B = -15.04 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 17.5 C, (coincident ratio = 0.6874)Rated MDMT of -49.54C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 15.88 mm

    Flange limits MDMT rating.

    5. Material is impact test exempt per UCS-66(d) (NPS 4 or smaller pipe)

    6.UCS-66(b)(1)(b) has been applied.Flange is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.3477)

    Bolts rated MDMT per Fig UCS-66 note (c) = -48 C

    7.

    UCS-66(b)(1)(b) has been applied.Flange impact test exemption temperature from Fig UCS-66M Curve B = -19.38 CFig UCS-66.1M MDMT reduction = 25.2 C, (coincident ratio = 0.5716)UCS-66 governing thickness = 13.75 mm

    Bolts rated MDMT per Fig UCS-66 note (c) = -48 C

    8. Nozzle is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.0158).

    9. Nozzle is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.016).

    10.Flange rating governs:Flange rated MDMT = -65 C (UCS-68(c) applies.)Bolts rated MDMT per Fig UCS-66 note (c) = -48 C

    UCS-66(b)(1)(b)

    11.

    Material impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.3 C, (coincident ratio = 0.4207)Rated MDMT of -110.3C is limited to -48C by UCS-66(b)(2)

    UCS-66 governing thickness = 9.5 mm

    12.

    Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 35.3 C, (coincident ratio = 0.4707)Rated MDMT of -81.3C is limited to -48C by UCS-66(b)(2)

    UCS-66 governing thickness = 9.5 mm

    13. Straight Flangegoverns MDMT

    14. UCS-66 does not apply. Reference Fig. UCS-66.2 General Note (2)

    15.

    UCS-66(b)(1)(b) has been applied.Flange impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 34.3 C, (coincident ratio = 0.4782)Rated MDMT of -80.3C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm

    Bolts rated MDMT per Fig UCS-66 note (c) = -48 C

    16.

    Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.9 C, (coincident ratio = 0.4186)Rated MDMT of -91.9C is limited to -48C by UCS-66(b)(2)

    UCS-66 governing thickness = 9.5 mm

    17.

    UCS-66(b)(1)(b) has been applied.Flange impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 12.4 C, (coincident ratio = 0.779)Rated MDMT of -58.4C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm

    Bolts rated MDMT per Fig UCS-66 note (c) = -48 C

    18.Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 35.7 C, (coincident ratio = 0.4684)Rated MDMT of -81.7C is limited to -48C by UCS-66(b)(2)

    UCS-66 governing thickness = 9.5 mm

    19. Nozzle is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.022).

    20. Nozzle is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.0221).

    21.

    Nozzle impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 46 C, (coincident ratio = 0.4183)Rated MDMT of -92C is limited to -48C by UCS-66(b)(2)

    UCS-66 governing thickness = 9.5 mm.

    22. UCS-66 governing thickness = 9.5 mm.

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    Nozzle impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.3 C, (coincident ratio = 0.4207)Rated MDMT of -91.3C is limited to -48C by UCS-66(b)(2)

    Design notes are available on the Settings Summarypage.

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    Revision History

    No. Date Operator Notes

    0 10/28/2013 rbarcenas New vessel created Heat Exchanger. [COMPRESS 2013 Build 7330]

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    Settings Summary

    COMPRESS 2013 Build 7330

    Units: MKS

    Datum Line Location: -34.00 mm from left seam

    Design

    ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric

    Design or Rating: Get Thickness from Pressure

    Minimum thickness: 1.5 mm per UG-16(b)Design for cold shut down only: No

    Design for lethal service (full radiography required): No

    Design nozzles for: Design P, find nozzle MAWP and MAPCorrosion weight loss: 100% of theoretical loss

    UG-23 Stress Increase: 1.20

    Skirt/legs stress increase: 1.0

    Minimum nozzle projection: 152.4 mmJuncture calculations for > 30 only: Yes

    Preheat P-No 1 Materials > 1.25" and

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    UG-22 Loadings

    UG-22(a) Internal or External Design Pressure : YesUG-22(b) Weight of the vessel and normal contents under operating or test conditions: Yes

    UG-22(c) Superimposed static reactions from weight of attached equipment (external loads): No

    UG-22(d)(2) Vessel supports such as lugs, rings, skirts, saddles and legs: YesUG-22(f) Wind reactions: No

    UG-22(f) Seismic reactions: No

    UG-22(j) Test pressure and coincident static head acting during the test: NoNote: UG-22(b),(c) and (f) loads only considered when supports are present.

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    Radiography Summary

    Radiography for Tube side chamber

    Component

    Longitudinal Seam Left Circumferential Seam Right Circumferential Seam

    MarkCategory(Fig

    UW-3)

    Radiography /Joint Type

    Category(Fig

    UW-3)

    Radiography /Joint Type

    Category(Fig

    UW-3)

    Radiography / JointType

    TAPA BRIDADA CANAL N/A Seamless No RT N/A N/A N/A N/A / Gasketed N/A

    ENVOLVENTE CANAL A Full UW-11(a) /Type 1

    C Full UW-11(a) /Type 1

    C Full UW-11(a) / Type1

    RT1

    BRIDA TAPA DEL CANAL N/A Seamless No RT N/A N/A / Gasketed CFull UW-11(a) / Type1

    RT1

    BRIDA CANAL --ESPEJO N/A Seamless No RT CFull UW-11(a) /Type 1

    N/A N/A / Gasketed RT1

    Front Stationary Tubesheet N/A Seamless No RT N/A N/A / Gasketed N/A N/A / Gasketed N/A

    Rear Floating Tubesheet N/A Seamless No RT C N/A / Gasketed N/A N/A / Gasketed N/A

    BRIDA BIPARTIDA N/A Seamless No RT N/A N/A / Gasketed C N/A N/A

    TAPA FLOTANTE N/A Seamless No RT C N/A / Gasketed N/A N/A N/A

    Tubes N/A Seamless No RT N/A N/A / Type 7 N/A N/A / Type 7 N/A

    Nozzle Longitudinal SeamNozzle to Vessel

    Circumferential Seam

    Nozzle free end Circumferential

    Seam

    N6 SALIDA DE AGUA DE ENFRIAMIENTO (N6) N/A Seamless No RT D N/A / Type 7 CUW-11(a)(4) exempt/ Type 1

    N/A

    N7A CONEXION PARA LIMPIEZA QUIMICA (N7A) N/A Seamless No RT D N/A / Type 7 CUW-11(a)(4) exempt/ Type 1

    N/A

    IT2 INSTRUMENTO DE TEMPERATUIRA (IT2) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A

    IP2 INSTRUMENTO DE PRESION (IP2) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A

    N5 INTERCONEXION DE CANALES (N5) N/A Seamless No RT D N/A / Type 7 CUW-11(a)(4) exempt/ Type 1

    N/A

    N7B CONEXION PARA LIMPIEZA QUIMICA (N7B) N/A Seamless No RT D N/A / Type 7 CUW-11(a)(4) exempt/ Type 1

    N/A

    IP3 INSTRUMENTO DE PRESION (IP3) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A

    IT3 INSTRUMENTO DE TEMPERATUIRA (IT3) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A

    Nozzle Flange Longitudinal Seam Flange FaceNozzle to Flange

    Circumferential Seam

    ASME B16.5/16.47 flange attached to N6 SALIDADE AGUA DE ENFRIAMIENTO (N6)

    N/A Seamless No RT N/A N/A / Gasketed CUW-11(a)(4) exempt/ Type 1

    N/A

    ASME B16.5/16.47 flange attached to N7ACONEXION PARA LIMPIEZA QUIMICA (N7A)

    N/A Seamless No RT N/A N/A / Gasketed CUW-11(a)(4) exempt/ Type 1

    N/A

    ASME B16.5/16.47 flange attached to N5INTERCONEXION DE CANALES (N5)

    N/A Seamless No RT N/A N/A / Gasketed CUW-11(a)(4) exempt/ Type 1

    N/A

    ASME B16.5/16.47 flange attached to N7BCONEXION PARA LIMPIEZA QUIMICA (N7B)

    N/A Seamless No RT N/A N/A / Gasketed CUW-11(a)(4) exempt/ Type 1

    N/A

    Tube side chamber - UG-116(e) Radiography:RT1

    Radiography for Shell side chamber

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    Component

    Longitudinal Seam Left Circumferential Seam Right Circumferential Seam

    MarkCategory(Fig

    UW-3)

    Radiography /Joint Type

    Category(Fig

    UW-3)

    Radiography /Joint Type

    Category(Fig

    UW-3)

    Radiography / JointType

    Front Stationary Tubesheet N/A Seamless No RT N/A N/A / Gasketed N/A N/A / Gasketed N/A

    ENVOLVENTE 1 AFull UW-11(a) /Type 1

    CFull UW-11(a) /Type 1

    BFull UW-11(a) / Type1

    RT1

    BRIDA CUERPO ESPEJO FIJO N/A Seamless No RT N/A N/A / Gasketed CFull UW-11(a) / Type1

    RT1

    ENVOLVENTE 2 A Full UW-11(a) /Type 1 B Full UW-11(a) /Type 1 C Full UW-11(a) / Type1 RT1

    BRIDA CUERPO -- BONETE N/A Seamless No RT CFull UW-11(a) /Type 1

    N/A N/A / Gasketed RT1

    Rear Shell Cylinder AFull UW-11(a) /Type 1

    CFull UW-11(a) /Type 1

    BFull UW-11(a) / Type1

    RT1

    BRIDA BONET --CUERPO N/A Seamless No RT N/A N/A / Gasketed CFull UW-11(a) / Type1

    RT1

    Rear Shell Head N/A Seamless No RT BFull UW-11(a) /Type 1

    N/A N/A RT1

    Rear Floating Tubesheet N/A Seamless No RT C N/A / Gasketed N/A N/A / Gasketed N/A

    Nozzle Longitudinal SeamNozzle to Vessel

    Circumferential SeamNozzle free end Circumferential

    Seam

    N2 INTERCONEXION DE ENVOLVENTE (N2) N/A Seamless No RT D N/A / Type 7 C UW-11(a)(4) exempt/ Type 1

    N/A

    IP4 INSTRUMENTO DE PRESION (IP4) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A

    IT4 INSTRUMENTO DE TEMPERATURA (IT4) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A

    N1 ENTRADA DEL FONDO DEL AGOTADOR (N1) N/A Seamless No RT D N/A / Type 7 CUW-11(a)(4) exempt/ Type 1

    N/A

    IP1 INSTRUMENTO DE PRESION (IP1) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A

    IT1 INDICADOR DE TEMPERATURA (IT1) N/A Seamless No RT D N/A / Type 7 N/A N/A N/A

    Nozzle Flange Longitudinal Seam Flange FaceNozzle to Flange

    Circumferential Seam

    ASME B16.5/16.47 flange attached to N2INTERCONEXION DE ENVOLVENTE (N2)

    N/A Seamless No RT N/A N/A / Gasketed CUW-11(a)(4) exempt/ Type 1

    N/A

    ASME B16.5/16.47 flange attached to N1 ENTRADADEL FONDO DEL AGOTADOR (N1) N/A Seamless No RT N/A N/A / Gasketed C UW-11(a)(4) exempt/ Type 1 N/A

    Shell side chamber - UG-116(e) Radiography:RT1

    Tubesheets are always considered to be seamless.

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    Thickness Summary

    ComponentIdentifier

    Material Diameter(mm)

    Length(mm)

    Nominal t(mm)

    Design t(mm)

    Total Corrosion(mm)

    JointE

    Load

    TAPA BRIDADA CANAL SA-516 70 788 OD 32 32* 29.42 0 1.00 Internal

    ENVOLVENTE CANAL SA-516 70 635 ID 355 9.5 4.79 3.17 1.00 Internal

    Front Stationary Tubesheet SA-516 70 665 OD 36.94 36.94 36.93 6.37 1.00 Unknown

    Rear Floating Tubesheet SA-516 70 630 OD 36.94 36.94 36.93 6.37 1.00 Unknown

    Tubes SA-179 Smls. Tube 19 OD 4,877 2.11 0.37 0 1.00 External

    ENVOLVENTE 1 SA-516 70 635 ID 2,214 9.5 5.85 3.2 1.00 Internal

    ENVOLVENTE 2 SA-516 70 635 ID 2,214 9.5 5.85 3.2 1.00 Internal

    Rear Shell Cylinder SA-516 70 711 ID 243 9.5 6.16 3.2 1.00 Internal

    Straight Flange on Rear Shell Head SA-516 70 711 ID 50.8 9.5 6.16 3.2 1.00 Internal

    Rear Shell Head SA-516 70 711 ID 187.25 9.5* 6.12 3.2 1.00 Internal

    Flange - TAPA FLOTANTE SA-105 609 ID 51.49 51.49 57.73 3.17 1.00 Unknown

    TAPA FLOTANTE SA-516 70 609 ID 120.2 15.88* 13.46 6.37 1.00 External

    Nominal t: Vessel wall nominal thickness

    Design t: Required vessel thickness due to governing loading + corrosionJoint E: Longitudinal seam joint efficiency

    * Head minimum thickness after forming

    Load

    internal: Circumferential stress due to internal pressure governs

    external: External pressure governs

    Wind: Combined longitudinal stress of pressure + weight + wind governs

    Seismic: Combined longitudinal stress of pressure + weight + seismic governs

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    Weight Summary

    Component

    Weight ( kg) Contributed by Vessel Elements SurfaceAream2Metal

    New*

    Metal

    Corroded* InsulationInsulationSupports

    LiningPiping

    + Liquid

    Operating Liquid Test Liquid

    New Corroded New Corroded

    TAPA BRIDADA CANAL 122.2 122.2 0 0 0 0 0 0 0 0 0.57

    ENVOLVENTE CANAL 50.2 33.6 0 0 0 0 176.1 179.8 179.4 183.5 0.68

    Front Stationary Tubesheet 80.6 47.8 0 0 0 0 0 0 0 0 0.08

    Rear Floating Tubesheet 64.3 36.3 0 0 0 0 0 0 0 0 N/A

    TAPA FLOTANTE 76.9 59.3 0 0 0 0 18.4 19.4 18.4 19.5 0

    ENVOLVENTE 1 331.9 221.2 0 0 0 0 491.8 506.6 491.8 506.9 4.53

    ENVOLVENTE 2 331.9 221.2 0 0 0 0 487 501.4 489.9 505 4.53

    Tubes 1,581.3 1,581.3 0 0 0 0 309.5 309.5 309.5 309.5 N/A

    Rear Shell Cylinder 40.9 27.3 0 0 0 0 76 79.1 77.6 80.9 0.56

    Rear Shell Head 53.4 35.7 0 0 0 0 66.4 68.3 63.6 66 0.76

    SILLETA 74.4 74.4 0 0 0 0 0 0 0 0 1.59

    TOTAL: 2,808 2,460.3 0 0 0 0 1,625.1 1,664 1,630.2 1,671.3 13.29

    * Shells with attached nozzles have weight reduced by material cut out for opening.

    Component

    Weight ( kg) Contributed by Attachments

    Surface Aream2Body Flanges Nozzles &Flanges

    PackedBeds

    TraysBaffles

    Pass Partitions

    TraySupports

    Rings &Clips

    VerticalLoads

    New Corroded New Corroded

    TAPA BRIDADA CANAL 0 0 0 0 0 0 0 0 0 0

    ENVOLVENTE CANAL 175.4 166.1 46.4 40.7 0 0 0 0 0 1.02

    Front Stationary Tubesheet 0 0 0 0 0 47.9 0 0 0 0

    Rear Floating Tubesheet 29.8 27.1 0 0 0 0 0 0 0 0

    TAPA FLOTANTE 0 0 0 0 0 0 0 0 0 0

    ENVOLVENTE 1 87.7 83.1 19.6 17 0 49.8 0 0 0 0.45

    ENVOLVENTE 2 113.6 109.4 19.6 17 0 49.8 0 0 0 0.45

    Rear Shell Cylinder 90.8 85.6 0 0 0 0 0 0 0 0.25

    Rear Shell Head 0 0 0 0 0 0 0 0 0 0

    TOTAL: 497.3 471.3 85.5 74.7 0 147.4 0 0 0 2.17

    Vessel operating weight, Corroded: 4,794 kg

    Vessel operating weight, New: 5,163 kgVessel empty weight, Corroded: 3,130 kg

    Vessel empty weight, New: 3,538 kg

    Vessel test weight, New: 5,150 kgVessel test weight, Corroded: 4,782 kg

    Vessel surface area: 15.47 m2

    Vessel center of gravity location - from datum - lift condition

    Vessel Lift Weight, New: 3,538 kg

    Center of Gravity: 2,843.58 mm

    Vessel Capacity

    Shell side Capacity** (New): 1,130 litersShell side Capacity** (Corroded): 1,165 liters

    Tube side Capacity** (New): 502 liters

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    Tube side Capacity** (Corroded): 506 liters**The shell and tube capacity does not include volume of nozzle, piping or other attachments.

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    Long Seam Summary

    Shell Long Seam Angles

    Component Seam 1

    ENVOLVENTE CANAL 45

    ENVOLVENTE 1 30

    ENVOLVENTE 2 315

    Rear Shell Cylinder 30

    Shell Plate Lengths

    ComponentStartingAngle

    Plate 1

    ENVOLVENTE CANAL 45 2,024.76 mm

    ENVOLVENTE 1 30 2,024.76 mm

    ENVOLVENTE 2 315 2,024.76 mm

    Rear Shell Cylinder 30 2,263.52 mm

    *Plate Lengths use the circumference of the vessel based on the mid diameter of the components

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    Shell Rollout

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    Test Report

    Shop test pressure determination for Tube side chamber based on user defined pressure

    Shop test gauge pressure is 9.1 kg f/cm2at 21.11 C

    The shop test is performed with the vessel in the horizontal position.

    IdentifierLocal testpressurekgf/cm

    2

    Testliquidstatichead

    kgf/cm2

    ENVOLVENTE CANAL 9.19 0.09

    TAPA FLOTANTE 9.19 0.09

    Tubes 9.19 0.09

    BRIDA TAPA DEL CANAL - Flange Hub 9.19 0.09

    BRIDA CANAL --ESPEJO - Flange Hub 9.19 0.09

    TAPA BRIDADA CANAL 9.19 0.09BRIDA TAPA DEL CANAL 9.19 0.09

    BRIDA CANAL --ESPEJO 9.19 0.09

    Front Stationary Tubesheet 9.19 0.09

    Rear Floating Tubesheet 9.19 0.09

    BRIDA BIPARTIDA 9.19 0.09

    IP2 INSTRUMENTO DE PRESION (IP2) 9.12 0.02

    IP3 INSTRUMENTO DE PRESION (IP3) 9.2 0.1

    IT2 INSTRUMENTO DE TEMPERATUIRA (IT2) 9.12 0.02

    IT3 INSTRUMENTO DE TEMPERATUIRA (IT3) 9.2 0.1

    N5 INTERCONEXION DE CANALES (N5) 9.22 0.12

    N6 SALIDA DE AGUA DE ENFRIAMIENTO (N6) 9.13 0.03

    N7A CONEXION PARA LIMPIEZA QUIMICA (N7A) 9.12 0.02

    N7B CONEXION PARA LIMPIEZA QUIMICA (N7B) 9.2 0.1

    Notes:(1) The zero degree angular position is assumed to be up, and the test liquid height is assumed to the top-mostflange.

    The field test condition has not been investigated for the Tube side chamber.

    The test temperature of 21.11 C is warmer than the minimum recommended temperature of -27.58 C so the brittlefracture provision of UG-99(h) has been met.

    Shop test pressure determination for Shell side chamber based on user defined pressure

    Shop test gauge pressure is 14.95 kg f/cm2at 21.11 C

    The shop test is performed with the vessel in the horizontal position.

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    IdentifierLocal testpressurekgf/cm

    2

    Testliquidstatichead

    kgf/cm2

    ENVOLVENTE 1 15.04 0.09

    ENVOLVENTE 2 15.04 0.09

    Rear Shell Cylinder 15.04 0.09

    TAPA FLOTANTE 15.04 0.09

    Straight Flange on Rear Shell Head 15.04 0.09

    Rear Shell Head 15.04 0.09

    Tubes 15.04 0.09

    BRIDA CUERPO ESPEJO FIJO - Flange Hub 15.04 0.09

    BRIDA CUERPO -- BONETE - Flange Hub 15.04 0.09

    BRIDA BONET -- CUERPO - Flange Hub 15.04 0.09

    Front Stationary Tubesheet 15.04 0.09

    BRIDA CUERPO ESPEJO FIJO 15.04 0.09

    BRIDA CUERPO -- BONETE 15.04 0.09

    BRIDA BONET -- CUERPO 15.04 0.09Rear Floating Tubesheet 15.04 0.09

    BRIDA BIPARTIDA 15.04 0.09

    IP1 INSTRUMENTO DE PRESION (IP1) 14.97 0.02

    IP4 INSTRUMENTO DE PRESION (IP4) 15.05 0.1

    IT1 INDICADOR DE TEMPERATURA (IT1) 14.97 0.02

    IT4 INSTRUMENTO DE TEMPERATURA (IT4) 15.05 0.1

    N1 ENTRADA DEL FONDO DEL AGOTADOR (N1) 14.98 0.03

    N2 INTERCONEXION DE ENVOLVENTE (N2) 15.07 0.12

    Notes:

    (1) The zero degree angular position is assumed to be up, and the test liquid height is assumed to the top-mostflange.

    The field test condition has not been investigated for the Shell side chamber.

    The test temperature of 21.11 C is warmer than the minimum recommended temperature of -27.58 C so the brittlefracture provision of UG-99(h) has been met.

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    Vacuum Summary

    Component Line of Support

    Elevation

    aboveDatum(mm)

    Length Le(mm)

    TAPA BRIDADA CANAL - 2 N/A

    - TAPA BRIDADA CANAL 34 N/A

    ENVOLVENTE CANAL Left - 130.2 545.8

    ENVOLVENTE CANAL Right - 485.2 545.8

    Front Stationary Tubesheet - 575 N/A

    - BRIDA CANAL --ESPEJO 579.8 N/A

    - BRIDA CUERPO ESPEJO FIJO 613.54 N/A

    ENVOLVENTE 1 Left - 708.14 4,607.6

    ENVOLVENTE 1 Right - 2,922.14 4,607.6

    ENVOLVENTE 2 Left - 2,922.14 4,607.6

    ENVOLVENTE 2 Right - 5,136.14 4,607.6

    - BRIDA CUERPO -- BONETE 5,221.14 N/A

    - BRIDA BONET -- CUERPO 5,224.34 N/A

    Rear Shell Cylinder Left - 5,316.34 446.12

    Rear Floating Tubesheet - 5,415.06 N/A

    - Flange - TAPA FLOTANTE 5,479.34 N/A

    - 1/3 depth of TAPA FLOTANTE 5,479.34 N/A

    Rear Shell Cylinder Right - 5,559.34 446.12

    Straight Flange on Rear Shell Head Left - 5,559.34 446.12

    TAPA FLOTANTE - 5,599.55 N/A

    Straight Flange on Rear Shell Head Right - 5,610.14 446.12

    - 1/3 depth of Rear Shell Head 5,670.45 N/A

    Rear Shell Head - 5,797.39 N/A

    NoteFor main components, the listed value of 'Le' is the largest unsupported length for the component.

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    ENVOLVENTE CANAL

    ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric

    Component: CylinderMaterial specification: SA-516 70 (II-D Metric p. 18, ln. 19)Material is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.302)

    Internal design pressure: P = 7 kg/cm2@ 66 C

    Static liquid head:

    Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.17 mm,Operating head)

    Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal test

    head)

    Corrosion allowance Inner C = 3.17 mm Outer C = 0 mm

    Design MDMT = -17.78 C No impact test performedRated MDMT = -105 C Material is not normalized

    Material is not produced to Fine Grain PracticePWHT is performed

    Radiography: Longitudinal joint - Full UW-11(a) Type 1Left circumferential joint - Full UW-11(a) Type 1Right circumferential joint - Full UW-11(a) Type 1

    Estimated weight New = 50.2 kg corr = 33.6 kgCapacity New = 112.43 liters corr = 114.68 liters

    ID = 635 mmLengthLc

    = 355 mm

    t = 9.5 mm

    Design thickness, (at 66 C) UG-27(c)(1)

    t = P*R / (S*E - 0.60*P) + Corrosion= 7.06*320.67 / (1,407.21*1.00 - 0.60*7.06) + 3.17= 4.79 mm

    Maximum allowable working pressure, (at 66 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t) - Ps= 1,407.21*1.00*6.33 / (320.67 + 0.60*6.33) - 0.06= 27.39 kg/cm2

    Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (317.5 + 0.60*9.5)= 41.36 kg/cm2

    % Extreme fiber elongation - UCS-79(d)

    EFE = (50*t / Rf)*(1 - Rf/ Ro)

    = (50*9.5 / 322.25)*(1 - 322.25 / infinity)

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    = 1.474%

    The extreme fiber elongation does not exceed 5%.

    Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.33)

    = 0.002420B = 1,092.5 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHC = min(B, S) = 1,092.5 kg/cm2

    Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 9.5)= 0.003631

    B = 1,169 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHN = min(B, S) = 1,169 kg/cm2

    Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)= 0.125 / (327 / 9.5)

    = 0.003631

    B = 1,169 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCN = min(B, S) = 1,169 kg/cm2

    Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.33)= 0.002420

    B = 1,092.5 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCC = min(B, S) = 1,092.5 kg/cm2

    Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.33)

    = 0.002420B = 1,092.5 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScVC = min(B, S) = 1,092.5 kg/cm2

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    ENVOLVENTE 1

    ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric

    Component: CylinderMaterial specification: SA-516 70 (II-D Metric p. 18, ln. 19)Material impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.3 C, (coincident ratio = 0.4207)

    Rated MDMT of -110.3C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm

    Internal design pressure: P = 11.5 kg/cm2@ 90 C

    Static liquid head:

    Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.2 mm,Operating head)

    Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal test

    head)

    Corrosion allowance Inner C = 3.2 mm Outer C = 0 mm

    Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is normalized

    Material is not produced to Fine Grain PracticePWHT is performed

    Radiography: Longitudinal joint - Full UW-11(a) Type 1Left circumferential joint - Full UW-11(a) Type 1Right circumferential joint - Full UW-11(a) Type 1

    Estimated weight New = 331.9 kg corr = 221.2 kg

    Capacity New = 468.9 liters corr = 483.1 liters

    ID = 635 mmLengthLc

    = 2,214 mm

    t = 9.5 mm

    Design thickness, (at 90 C) UG-27(c)(1)

    t = P*R / (S*E - 0.60*P) + Corrosion= 11.56*320.7 / (1,407.21*1.00 - 0.60*11.56) + 3.2= 5.85 mm

    Maximum allowable working pressure, (at 90 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t) - Ps= 1,407.21*1.00*6.3 / (320.7 + 0.60*6.3) - 0.06= 27.26 kg/cm2

    Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (317.5 + 0.60*9.5)= 41.36 kg/cm2

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    % Extreme fiber elongation - UCS-79(d)

    EFE = (50*t / Rf)*(1 - Rf/ Ro)= (50*9.5 / 322.25)*(1 - 322.25 / infinity)

    = 1.474%

    The extreme fiber elongation does not exceed 5%.

    Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.3)

    = 0.002408B = 1,091.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHC = min(B, S) = 1,091.4 kg/cm2

    Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 9.5)

    = 0.003631B = 1,169 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHN = min(B, S) = 1,169 kg/cm2

    Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 9.5)= 0.003631

    B = 1,169 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCN = min(B, S) = 1,169 kg/cm2

    Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.3)

    = 0.002408B = 1,091.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCC = min(B, S) = 1,091.4 kg/cm2

    Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.3)

    = 0.002408

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    B = 1,091.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScVC = min(B, S) = 1,091.4 kg/cm2

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    ENVOLVENTE 2

    ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric

    Component: CylinderMaterial specification: SA-516 70 (II-D Metric p. 18, ln. 19)Material impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.3 C, (coincident ratio = 0.4207)

    Rated MDMT of -110.3C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm

    Internal design pressure: P = 11.5 kg/cm2@ 90 C

    Static liquid head:

    Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.2 mm,Operating head)

    Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal test

    head)

    Corrosion allowance Inner C = 3.2 mm Outer C = 0 mm

    Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is normalized

    Material is not produced to Fine Grain PracticePWHT is performed

    Radiography: Longitudinal joint - Full UW-11(a) Type 1Left circumferential joint - Full UW-11(a) Type 1Right circumferential joint - Full UW-11(a) Type 1

    Estimated weight New = 331.9 kg corr = 221.2 kg

    Capacity New = 468.9 liters corr = 483.1 liters

    ID = 635 mmLengthLc

    = 2,214 mm

    t = 9.5 mm

    Design thickness, (at 90 C) UG-27(c)(1)

    t = P*R / (S*E - 0.60*P) + Corrosion= 11.56*320.7 / (1,407.21*1.00 - 0.60*11.56) + 3.2= 5.85 mm

    Maximum allowable working pressure, (at 90 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t) - Ps= 1,407.21*1.00*6.3 / (320.7 + 0.60*6.3) - 0.06= 27.26 kg/cm2

    Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (317.5 + 0.60*9.5)= 41.36 kg/cm2

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    % Extreme fiber elongation - UCS-79(d)

    EFE = (50*t / Rf)*(1 - Rf/ Ro)= (50*9.5 / 322.25)*(1 - 322.25 / infinity)

    = 1.474%

    The extreme fiber elongation does not exceed 5%.

    Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.3)

    = 0.002408B = 1,091.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHC = min(B, S) = 1,091.4 kg/cm2

    Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 9.5)

    = 0.003631B = 1,169 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHN = min(B, S) = 1,169 kg/cm2

    Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 9.5)= 0.003631

    B = 1,169 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCN = min(B, S) = 1,169 kg/cm2

    Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.3)

    = 0.002408B = 1,091.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCC = min(B, S) = 1,091.4 kg/cm2

    Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.3)

    = 0.002408

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    B = 1,091.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScVC = min(B, S) = 1,091.4 kg/cm2

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    Rear Shell Cylinder

    ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric

    Component: CylinderMaterial specification: SA-516 70 (II-D Metric p. 18, ln. 19)Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 35.3 C, (coincident ratio = 0.4707)

    Rated MDMT of -81.3C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm

    Internal design pressure: P = 11.5 kg/cm2@ 90 C

    Static liquid head:

    Ps = 0.07 kg/cm2 (SG = 1, Hs= 676.2 mm,Operating head)

    Pth = 0.09 kg/cm2 (SG = 1, Hs= 945.5 mm, Horizontal test

    head)

    Corrosion allowance Inner C = 3.2 mm Outer C = 0 mm

    Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is not normalized

    Material is not produced to Fine Grain PracticePWHT is performed

    Radiography: Longitudinal joint - Full UW-11(a) Type 1Left circumferential joint - Full UW-11(a) Type 1Right circumferential joint - Full UW-11(a) Type 1

    Estimated weight New = 40.9 kg corr = 27.3 kg

    Capacity New = 50.12 liters corr = 52.84 liters

    ID = 711 mmLengthLc

    = 243 mm

    t = 9.5 mm

    Design thickness, (at 90 C) UG-27(c)(1)

    t = P*R / (S*E - 0.60*P) + Corrosion= 11.57*358.7 / (1,407.21*1.00 - 0.60*11.57) + 3.2= 6.16 mm

    Maximum allowable working pressure, (at 90 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t) - Ps= 1,407.21*1.00*6.3 / (358.7 + 0.60*6.3) - 0.07= 24.39 kg/cm2

    Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (355.5 + 0.60*9.5)= 37.01 kg/cm2

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    % Extreme fiber elongation - UCS-79(d)

    EFE = (50*t / Rf)*(1 - Rf/ Ro)= (50*9.5 / 360.25)*(1 - 360.25 / infinity)

    = 1.3185%

    The extreme fiber elongation does not exceed 5%.

    Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 6.3)

    = 0.002157B = 1,066.9 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHC = min(B, S) = 1,066.9 kg/cm2

    Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 9.5)

    = 0.003253B = 1,153.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHN = min(B, S) = 1,153.4 kg/cm2

    Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 9.5)= 0.003253

    B = 1,153.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCN = min(B, S) = 1,153.4 kg/cm2

    Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 6.3)

    = 0.002157B = 1,066.9 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCC = min(B, S) = 1,066.9 kg/cm2

    Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 6.3)

    = 0.002157

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    B = 1,066.9 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScVC = min(B, S) = 1,066.9 kg/cm2

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    TAPA BRIDADA CANAL

    ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric

    Component: Bolted CoverAttached to: BRIDA TAPA DEL CANALMaterial specification: SA-516 70 (II-D Metric p. 18, ln. 19)Bolted cover impact test exemption temperature from Fig UCS-66M Curve D = -48 C17 C MDMT reduction per UCS-68(c) applies.

    Rated MDMT of -65C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 8 mm

    Internal design pressure: P = 7 kg/cm2@ 66 C

    Static liquid head:

    Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.17 mm, Operating head)

    Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal testhead)

    Corrosion allowance: Inner C = 0 mm Outer C = 0 mm

    Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is normalized

    Material is not produced to Fine Grain PracticePWHT is performed

    Radiography: Category A joints - Seamless No RT

    Estimated weight: New = 122.2 kg corr = 122.2 kg

    Head diameter, d = 675 mm

    Cover thickness, t = 32 mmDesign thickness, (at 66 C) UG-34 (c)(2), flange operating

    t = d*Sqr(C*P / (S*E) + 1.9*W*hG/ (S*E*d3)) + Corrosion

    = 675*Sqr(0.3*7.06 / (1,407.207*1) + 100*1.9*30,880.81*29 / (1,407.207*1*6753)) + 0= 29.42 mm

    Design thickness, (at 21.11 C) UG-34 (c)(2), gasket seating

    t = d*Sqr(1.9*W*hG/ (S*E*d3)) + Corrosion

    = 10*675*Sqr(1.9*80,471.86*29 / (1,407.207*1*6753)) + 0= 21.61 mm

    Maximum allowable working pressure, (at 66 C )

    P = (S*E / C)*((t / d)2- (1.9*W*hG/ (S*E*d3))) - Ps= (1,407.207*1 / 0.3)*((32 / 675)2- (1.9*100*36,546.12*29 / (1,407.207*1*6753))) - 0.0638= 8.3 kgf/cm

    2

    Maximum allowable pressure, (At 21.11 C )

    P = (S*E / C)*((t / d)2- (1.9*W*hG/ (S*E*d3)))

    = (1,407.207*1 / 0.3)*((32 / 675)2- (1.9*100*36,546.12*29 / (1,407.207*1*6753)))= 8.36 kgf/cm

    2

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    % Extreme fiber elongation - UCS-79(d)

    EFE = (50*t / Rf)*(1 - Rf/ Ro)= (50*9.5 / 360.25)*(1 - 360.25 / infinity)

    = 1.3185%

    The extreme fiber elongation does not exceed 5%.

    Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 6.3)

    = 0.002157B = 1,066.9 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHC = min(B, S) = 1,066.9 kg/cm2

    Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 9.5)

    = 0.003253B = 1,153.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHN = min(B, S) = 1,153.4 kg/cm2

    Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 9.5)= 0.003253

    B = 1,153.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCN = min(B, S) = 1,153.4 kg/cm2

    Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 6.3)

    = 0.002157B = 1,066.9 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCC = min(B, S) = 1,066.9 kg/cm2

    Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 6.3)

    = 0.002157

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    B = 1,066.9 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScVC = min(B, S) = 1,066.9 kg/cm2

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    Rear Shell Head

    ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric

    Component: Ellipsoidal HeadMaterial Specification: SA-516 70 (II-D Metric p.18, ln. 19)Straight Flangegoverns MDMT

    Internal design pressure: P = 11.5 kg f/cm2

    @ 90 C

    Static liquid head:

    Ps= 0.07 kgf/cm2(SG=1, Hs=676.2 mm Operating head)

    Pth= 0.09 kgf/cm2(SG=1, Hs=945.5 mm Horizontal test head)

    Corrosion allowance: Inner C = 3.2 mm Outer C = 0 mm

    Design MDMT = -17.78C No impact test performedRated MDMT = -48C Material is not normalized

    Material is not produced to fine grain practicePWHT is performed

    Do not Optimize MDMT / Find MAWP

    Radiography: Category A joints - Seamless No RTHead to shell seam - Full UW-11(a) Type 1

    Estimated weight*: new = 53.4 kg corr = 35.7 kgCapacity*: new = 63.7 liters corr = 66 liters* includes straight flange

    Inner diameter = 711 mmMinimum head thickness = 9.5 mmHead ratio D/2h = 2 (new)Head ratio D/2h = 1.9823 (corroded)Straight flange length Lsf = 50.8 mmNominal straight flange thickness tsf = 9.5 mmResults Summary

    The governing condition is internal pressure.Minimum thickness per UG-16 = 1.5 mm + 3.2 mm= 4.7 mmDesign thickness due to internal pressure (t) = 6.12mmMaximum allowable working pressure (MAWP) = 24.9kgf/cm

    2

    Maximum allowable pressure (MAP) = 37.5kgf/cm2

    K (Corroded)K=(1/6)*[2 + (D / (2*h))2]=(1/6)*[2 + (717.4 / (2*180.95))2]=0.988261

    K (New)

    K=(1/6)*[2 + (D / (2*h))2]=(1/6)*[2 + (711 / (2*177.75))2]=1

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    Design thickness for internal pressure, (Corroded at 90 C) Appendix 1-4(c)

    t = P*D*K / (2*S*E - 0.2*P) + Corrosion= 11.57*717.4*0.988261 / (2*1,407.21*1 - 0.2*11.57) + 3.2= 6.12 mm

    The head internal pressure design thickness is 6.12mm.

    Maximum allowable working pressure, (Corroded at 90 C) Appendix 1-4(c)

    P = 2*S*E*t / (K*D + 0.2*t) - Ps= 2*1,407.21*1*6.3 / (0.988261*717.4 +0.2*6.3) - 0.07= 24.9 kgf/cm

    2

    The maximum allowable working pressure (MAWP) is 24.9kgf/cm2.

    Maximum allowable pressure, (New at 21.11 C) Appendix 1-4(c)

    P = 2*S*E*t / (K*D + 0.2*t) - Ps= 2*1,407.21*1*9.5 / (1*711 +0.2*9.5) - 0= 37.5 kgf/cm

    2

    The maximum allowable pressure (MAP) is 37.5kgf/cm2.

    % Extreme fiber elongation - UCS-79(d)

    EFE = (75*t / Rf)*(1 - Rf/ Ro)

    = (75*9.5 / 125.62)*(1 - 125.62 / infinity)= 5.6719%

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    BRIDA BIPARTIDA

    ASME VIII-1, 2010 Edition, A11 Addenda Metric, Appendix 2 Flange Calculations

    Flange is attached to: Rear Floating TubesheetFlange type: Lap joint loose

    Flange material specification: SA-105 (II-D Metric p. 18, ln. 5)

    Bolt material specification:SA-193 B7 Bolt

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    UCS-66(b)(1)(b) has been applied.Flange impact test exemption temperature from Fig UCS-66M Curve B = -19.38 C

    Fig UCS-66.1M MDMT reduction = 26 C, (coincident ratio = 0.5614)UCS-66 governing thickness = 13.75 mmBolts rated MDMT per Fig UCS-66 note (c) = -48 C

    The rated flange MDMT is -45.38 C

    Flange calculations for Internal Pressure + Weight Only

    Gasket details from facing sketch 1(a) or (b), Column II

    Gasket width N = 10 mm

    b0= N/2 = 5 mm

    Effective gasket seating width, b = b0= 5 mm

    hG= (C - G)/2 = (660 - 619)/2 = 20.5 mm

    hD= (C - B)/2 = (660 - 608)/2 = 26 mm

    hT= (C - G)/2 = (660 - 619)/2 = 20.5 mm

    Hp= 2*b*3.14*G*m*P= 0.01*2*5*3.14*619*3.75*7

    = 5,102.11 kgf

    H = 0.785*G2*P

    = 0.01*0.785*6192*7= 21,054.7 kgf

    HD= 0.785*B2*P

    = 0.01*0.785*6082*7

    = 20,313.04 kgf

    HT= H - HD= 21,054.7 - 20,313.04

    = 741.66 kgf

    Wm1= H + Hp= 21,054.7 + 5,102.11

    = 26,156.81 kgf

    Wm2= 3.14*b*G*y

    = 0.01*3.14*5*619*534.3324= 51,928.08 kgf

    Required bolt area, Am= greater of Am1, Am2= 29.607 cm2

    Am1= Wm1/Sb= 26,156.81/1,753.911 = 14.9134 cm2

    Am2= Wm2/Sa= 51,928.08/1,753.911 = 29.607 cm2

    Total area for 32- 0.625 in dia bolts, corroded, Ab= 41.7031 cm2

    W = (Am+ Ab)*Sa/2

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    = (29.607 + 41.7031)*1,753.911/2= 62,535.86 kgf

    MD= HD*hD= 20,313.04*0.026 = 528.1 kgf-mMT= HT*hT= 741.66*0.0205 = 15.2 kgf-m

    HG= Wm1- H = 26,156.81 - 21,054.7 = 5,102.11 kgf

    MG= HG*hG= 5,102.11*0.0205 = 104.6 kgf-m

    Mo= MD+ MT+ MG= 528.1 + 15.2 + 104.6 = 647.9 kgf-m

    Mg= W*hG= 62,535.86*0.0205 = 1,282 kgf-m

    From FIG. 2-7.1, where K = A/B = 700/608 = 1.1513, Y = 13.8319

    Stresses at operating conditions - VIII-1 Appendix 2-7

    SR= SH= 0

    ST= Y*Mo/(t2*B)

    = 1e5*13.8319*647.9/(552*608)

    = 487.287 kgf/cm2

    Allowable stress Sfo= 1,407.207 kgf/cm2

    STdoes not exceed Sfo

    Stresses at gasket seating - VIII-1 Appendix 2-7

    ST= Y*Mg/(t2*B)

    = 1e5*13.8319*1,282/(552*608)

    = 964.13 kgf/cm2

    Allowable stress Sfa

    = 1,407.207 kgf

    /cm2

    STdoes not exceed Sfa

    Flange rigidity per VIII-1 Appendix 2-14

    J = 109.4*Mo/(E*t3*KL*ln(K))

    = 109.4*1,282/(20.52E+05*553*0.3*ln(1.1513))

    = 0.9718

    The flange rigidity index J does not exceed 1; satisfactory.

    Flange calculations for External Pressure + Weight Only per VIII-1, Appendix 2-11

    Gasket details from facing sketch 1(a) or (b), Column II

    Gasket width N = 10 mm

    b0= N/2 = 5 mm

    Effective gasket seating width, b = b0= 5 mm

    hG= (C - G)/2 = (660 - 619)/2 = 20.5 mm

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    hD= (C - B)/2 = (660 - 608)/2 = 26 mm

    hT= (C - G)/2 = (660 - 619)/2 = 20.5 mm

    Hp= 2*b*3.14*G*m*P= 0.01*2*5*3.14*619*3.75*11.5

    = 8,382.03 kgf

    H = 0.785*G2

    *P= 0.01*0.785*6192*11.5= 34,589.86 kgf

    HD= 0.785*B2*P

    = 0.01*0.785*6082*11.5= 33,371.42 kgf

    HT= H - HD= 34,589.86 - 33,371.42

    = 1,218.44 kgf

    Wm1= H + Hp

    = 34,589.86 + 8,382.03= 42,971.89 kgf

    Wm2= 3.14*b*G*y= 0.01*3.14*5*619*534.3324= 51,928.08 kgf

    Required bolt area, Am= greater of Am1, Am2= 29.607 cm2

    Am1= 0.785*G2*(Pm- Pr)/Sb= 0/1,753.911 = 0 cm

    2

    Am2= Wm2/Sa= 51,928.08/1,753.911 = 29.607 cm2

    Total area for 32- 0.625 in dia bolts, corroded, Ab= 41.7031 cm2

    W = (Am2+ Ab)*Sa/2= (29.607 + 41.7031)*1,753.911/2

    = 62,535.86 kgf

    Mo= HD*(hD- hG) + HT*(hT- hG)

    = 33,371.42*(0.026 - 0.0205) + 1,218.44*(0.0205 - 0.0205)= 183.5 kgf-m

    Mg= W*hG= 62,535.86*0.0205 = 1,282 kgf-m

    From FIG. 2-7.1, where K = A/B = 700/608 = 1.1513, Y = 13.8319

    Stresses at operating conditions - VIII-1 Appendix 2-7

    SR= SH= 0

    ST= Y*Mo/(t2*B)

    = 1e5*13.8319*183.5/(552*608)= 138.035 kgf/cm

    2

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    Allowable stress Sfo= 1,407.207 kgf/cm2

    STdoes not exceed Sfo

    Stresses at gasket seating - VIII-1 Appendix 2-7

    ST= Y*Mg/(t2*B)

    = 1e5*13.8319*1,282/(552*608)= 964.13 kgf/cm

    2

    Allowable stress Sfa= 1,407.207 kgf/cm2

    STdoes not exceed Sfa

    Flange rigidity per VIII-1 Appendix 2-14

    J = 109.4*Mo/(E*t3*KL*ln(K))

    = 109.4*1,282/(20.52E+05*553*0.3*ln(1.1513))= 0.9718

    The flange rigidity index J does not exceed 1; satisfactory.

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    BRIDA BONET -- CUERPO

    ASME VIII-1, 2010 Edition, A11 Addenda Metric, Appendix 2 Flange Calculations

    Flange is attached to: Rear Shell Cylinder (Left)Flange type: Weld neck integralFlange material specification: SA-105 (II-D Metric p. 18, ln. 5)

    Bolt material specification:SA-193 B7 Bolt

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    17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 12.4 C, (coincident ratio = 0.779)Rated MDMT of -58.4C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mmBolts rated MDMT per Fig UCS-66 note (c) = -48 C

    The rated flange MDMT is -48 C

    Flange calculations for Internal Pressure + Weight Only

    Gasket details from facing sketch 1(a) or (b), Column II

    Gasket width N = 13 mm

    b0= N/2 = 6.5 mm

    Effective gasket seating width, b = 2.5*b01/2= 6.37 mm

    G = gasket OD - 2*b = 743 - 2*6.37 = 730.25 mm

    hG= (C - G)/2 = (799 - 730.25)/2 = 34.37 mm

    hD= R + g1/2 = 25 + 15.83/2 = 32.92 mm

    hT= (R + g1+ hG)/2 = (25 + 15.83 + 34.37)/2 = 37.6 mm

    Hp= 2*b*3.14*G*m*P= 0.01*2*6.37*3.14*730.25*3.75*11.5675= 12,677.72 kgf

    H = 0.785*G2*P= 0.01*0.785*730.252*11.5675= 48,423.88 kgf

    HD= 0.785*B2

    *P= 0.01*0.785*717.342*11.5675= 46,726.29 kgf

    HT= H - HD= 48,423.88 - 46,726.29= 1,697.59 kgf

    Wm1= H + Hp= 48,423.88 + 12,677.72= 61,101.6 kgf

    Wm2= 3.14*b*G*y

    = 0.01*3.14*6.37*730.25*534.3324= 78,081.84 kgf

    Required bolt area, Am= greater of Am1, Am2= 44.5187 cm2

    Am1= Wm1/Sb= 61,101.6/1,753.911 = 34.8373 cm2

    Am2= Wm2/Sa= 78,081.84/1,753.911 = 44.5187 cm2

    Total area for 26- 0.875 in dia bolts, corroded, Ab= 48.1251 cm2

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    W = (Am+ Ab)*Sa/2= (44.5187 + 70.2837)*1,753.911/2= 100,676.66 kgf

    MD= HD*hD= 46,726.29*0.0329 = 1,538 kgf-mMT= HT*hT= 1,697.59*0.0376 = 63.8 kgf-m

    HG= Wm1- H = 61,101.6 - 48,423.88 = 12,677.72 kgf

    MG= HG*hG= 12,677.72*0.0344 = 435.8 kgf-m

    Mo= MD+ MT+ MG= 1,538 + 63.8 + 435.8 = 2,037.6 kgf-m

    Mg= W*hG= 100,676.66*0.0344 = 3,460.5 kgf-m

    The bolts are adequately spaced so the TEMA RCB-11.23 load concentration factor does not apply.

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    Hub and Flange Factors

    g0= min(g0, tn) = min(6.33, 6.3) = 6.3

    h0= (B*g0)1/2= (717.34*6.3)1/2= 67.22 mm

    From FIG. 2-7.1, where K = A/B = 854/717.34 = 1.1905

    T = 1.8428 Z = 5.7926 Y = 11.2272 U = 12.3376

    h/h0= 0.476 g1/g0= 2.5129

    F = 0.8234 V = 0.1921 e = F/h0= 0.1225

    d = (U/V)*h0*g02= (12.3376/0.1921)*6.7223*0.632

    = 171.3114 cm3

    Stresses at operating conditions - VIII-1 Appendix 2-7

    f = 2.1263

    L = (t*e + 1)/T + t3/d

    = (6*0.1225 + 1)/1.8428 + 63

    /171.3114= 2.2023

    SH= f*Mo/(L*g12*B)

    = 1e5*2.1263*2,037.6/(2.2023*15.832*717.34)= 1,094.397 kgf/cm

    2

    SR= (1.33*t*e + 1)*Mo/(L*t2*B)

    = (1.33*60*0.0122 + 1)*1e5*2,037.6/(2.2023*602*717.34)= 70.845 kgf/cm

    2

    ST= Y*Mo/(t2*B) - Z*SR

    = 1e5*11.2272*2,037.6/(602*717.34) - 5.7926*70.845

    = 475.482 kgf/cm2

    Allowable stress Sfo= 1,407.207 kgf/cm2

    Allowable stress Sno= 1,407.207 kgf/cm2

    STdoes not exceed SfoSHdoes not exceed Min[ 1.5*Sfo, 2.5*Sno] = 2,110.811 kgf/cm

    2

    SRdoes not exceed Sfo0.5(SH+ SR) = 582.621 kgf/cm

    2does not exceed Sfo0.5(SH+ ST) = 784.94 kgf/cm

    2does not exceed Sfo

    Stresses at gasket seating - VIII-1 Appendix 2-7

    SH= f*Mg/(L*g12*B)= 1e5*2.1263*3,460.5/(2.2023*15.832*717.34)= 1,858.663 kgf/cm

    2

    SR= (1.33*t*e + 1)*Mg/(L*t2*B)

    = (1.33*60*0.0122 + 1)*1e5*3,460.5/(2.2023*602*717.34)= 120.319 kgf/cm

    2

    ST= Y*Mg/(t2*B) - Z*SR

    = 11.2272*1e5*3,460.5/(602*717.34) - 5.7926*120.319

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    = 807.533 kgf/cm2

    Allowable stress Sfa= 1,407.207 kgf/cm2

    Allowable stress Sna= 1,407.207 kgf/cm2

    STdoes not exceed SfaSHdoes not exceed Min[ 1.5*Sfa, 2.5*Sna] = 2,110.811 kgf/cm

    2

    SRdoes not exceed Sfa0.5(SH+ SR) = 989.491 kgf/cm

    2does not exceed Sfa

    0.5(SH+ ST) = 1,333.098 kgf/cm2

    does not exceed Sfa

    Flange rigidity per VIII-1 Appendix 2-14

    J = 52.14*V*Mo/(L*E*g02*KI*h0)

    = 1e5*52.14*0.1921*3,460.5/(2.2023*20.52E+05*6.32*0.3*67.22)= 0.9585

    The flange rigidity index J does not exceed 1; satisfactory.

    BRIDA BONET -- CUERPO - Flange hub

    ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric

    Component: Flange hubMaterial specification: SA-105 (II-D Metric p. 18, ln. 5)Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 35.7 C, (coincident ratio = 0.4684)Rated MDMT of -81.7C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm

    Internal design pressure: P = 11.5 kg/cm2@ 90 C

    Static liquid head:

    Ps = 0.07 kg/cm2 (SG = 1, Hs= 676.17 mm,Operating head)

    Pth = 0.09 kg/cm2 (SG = 1, Hs= 945.5 mm, Horizontal test

    head)

    Corrosion allowance Inner C = 3.17 mm Outer C = 0 mm

    Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is normalized

    Material is not produced to Fine Grain PracticePWHT is performed

    Radiography: Longitudinal joint - Seamless No RT

    Left circumferential joint - N/ARight circumferential joint - Full UW-11(a) Type 1

    Estimated weight New = 5.3 kg corr = 3.6 kg

    Capacity New = 12.71 liters corr = 12.93 liters

    ID = 711 mmLengthLc

    = 32 mm

    t = 9.5 mm

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    Design thickness, (at 90 C) UG-27(c)(1)

    t = P*R / (S*E - 0.60*P) + Corrosion= 11.57*358.67 / (1,407.21*1.00 - 0.60*11.57) + 3.17= 6.13 mm

    Maximum allowable working pressure, (at 90 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t) - Ps

    = 1,407.21*1.00*6.33 / (358.67 + 0.60*6.33) - 0.07= 24.51 kg/cm2

    Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (355.5 + 0.60*9.5)= 37.01 kg/cm2

    Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)= 0.125 / (365 / 6.33)

    = 0.002168B = 1,067.9 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHC = min(B, S) = 1,067.9 kg/cm2

    Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 9.5)

    = 0.003253B = 1,153.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHN = min(B, S) = 1,153.4 kg/cm2

    Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 9.5)= 0.003253

    B = 1,153.4 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCN = min(B, S) = 1,153.4 kg/cm2

    Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 6.33)

    = 0.002168B = 1,067.9 kg/cm2

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    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCC = min(B, S) = 1,067.9 kg/cm2

    Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (365 / 6.33)

    = 0.002168B = 1,067.9 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScVC = min(B, S) = 1,067.9 kg/cm2

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    BRIDA CANAL --ESPEJO

    ASME VIII-1, 2010 Edition, A11 Addenda Metric, Appendix 2 Flange Calculations

    Flange is attached to: ENVOLVENTE CANAL (Right)Flange type: Weld neck integralFlange material specification: SA-105 (II-D Metric p. 18, ln. 5)

    Bolt material specification:SA-193 B7 Bolt

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    Bolts rated MDMT per Fig UCS-66 note (c) = -48 C

    The rated flange MDMT is -48 C

    Flange calculations for Internal Pressure + Weight Only

    Gasket details from facing sketch 1(a) or (b), Column II

    Gasket width N = 10 mm

    b0= N/2 = 5 mm

    Effective gasket seating width, b = b0= 5 mm

    G = (gasket OD + gasket ID) / 2 = (685 + 665) / 2 = 675 mm

    hG= (C - G)/2 = (733 - 675)/2 = 29 mm

    hD= R + g1/2 = 35 + 10.83/2 = 40.42 mm

    hT= (R + g1+ hG)/2 = (35 + 10.83 + 29)/2 = 37.42 mm

    Hp= 2*P*(b*3.14*G*m + br*rl*m')= 0.01*2*7.0638*(5*3.14*675*3.75 + 3.17*2*2)= 5,616.16 kgf

    H = 0.785*G2*P= 0.01*0.785*6752*7.0638= 25,264.65 kgf

    HD= 0.785*B2*P

    = 0.01*0.785*641.342*7.0638= 22,807.73 kgf

    HT= H - HD= 25,264.65 - 22,807.73= 2,456.91 kgf

    Wm1= H + Hp= 25,264.65 + 5,616.16= 30,880.8 kgf

    Per VIII-1 Appendix 2-5(a)(2): Wm1from the mating flange governs so Wm1= 50,122.39 kgf

    Wm2= 3.14*b*G*y + br*rl*Y'= 0.01*3.14*5*675*534.3324 + 3.17*2*175.767= 56,637.07 kgf

    The pass partition gasket load has been included in the calculation of Wm1and Wm2per TEMA RGP-RCB-11.7.

    Per VIII-1 Appendix 2-5(a)(2): Wm2from the mating flange governs so Wm2= 71,049.43 kgf

    Required bolt area, Am= greater of Am1, Am2= 40.5091 cm2

    Am1= Wm1/Sb= 50,122.39/1,753.911 = 28.5775 cm2

    Am2= Wm2/Sa= 71,049.43/1,753.911 = 40.5091 cm2

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    Total area for 22- 0.875 in dia bolts, corroded, Ab= 41.7857 cm2

    W = (Am+ Ab)*Sa/2= (40.5091 + 59.4708)*1,753.911/2= 87,678.03 kgf

    MD= HD*hD= 22,807.73*0.0404 = 921.8 kgf-mMT= HT*hT= 2,456.91*0.0374 = 91.9 kgf-m

    HG= Wm1- H = 50,122.39 - 25,264.65 = 24,857.75 kgf

    MG= HG*hG= 24,857.75*0.029 = 720.9 kgf-m

    Mo= MD+ MT+ MG= 921.8 + 91.9 + 720.9 = 1,734.6 kgf-m

    Mg= W*hG= 87,678.03*0.029 = 2,542.7 kgf-m

    The bolts are adequately spaced so the TEMA RCB-11.23 load concentration factor does not apply.

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    Hub and Flange Factors

    g0= min(g0, tn) = min(6.33, 6.33) = 6.33

    h0= (B*g0)1/2= (641.34*6.33)1/2= 63.72 mm

    From FIG. 2-7.1, where K = A/B = 788/641.34 = 1.2287

    T = 1.8273 Z = 4.9243 Y = 9.5462 U = 10.4904

    h/h0= 0.5022 g1/g0= 1.7109

    F = 0.8359 V = 0.2675 e = F/h0= 0.1312

    d = (U/V)*h0*g02= (10.4904/0.2675)*6.3716*0.6332

    = 100.1071 cm3

    Stresses at operating conditions - VIII-1 Appendix 2-7

    f = 1

    L = (t*e + 1)/T + t3/d

    = (6.1*0.1312 + 1)/1.8273 + 6.13

    /100.1071= 3.2526

    SH= f*Mo/(L*g12*B)

    = 1e5*1*1,734.6/(3.2526*10.832*641.34)= 708.945 kgf/cm

    2

    SR= (1.33*t*e + 1)*Mo/(L*t2*B)

    = (1.33*61*0.0131 + 1)*1e5*1,734.6/(3.2526*612*641.34)= 46.131 kgf/cm

    2

    ST= Y*Mo/(t2*B) - Z*SR

    = 1e5*9.5462*1,734.6/(612*641.34) - 4.9243*46.131

    = 466.706 kgf/cm2

    Allowable stress Sfo= 1,407.207 kgf/cm2

    Allowable stress Sno= 1,407.207 kgf/cm2

    STdoes not exceed SfoSHdoes not exceed Min[ 1.5*Sfo, 2.5*Sno] = 2,110.811 kgf/cm

    2

    SRdoes not exceed Sfo0.5(SH+ SR) = 377.538 kgf/cm

    2does not exceed Sfo0.5(SH+ ST) = 587.826 kgf/cm

    2does not exceed Sfo

    Stresses at gasket seating - VIII-1 Appendix 2-7

    SH= f*Mg/(L*g12*B)= 1e5*1*2,542.7/(3.2526*10.832*641.34)= 1,039.221 kgf/cm

    2

    SR= (1.33*t*e + 1)*Mg/(L*t2*B)

    = (1.33*61*0.0131 + 1)*1e5*2,542.7/(3.2526*612*641.34)= 67.622 kgf/cm

    2

    ST= Y*Mg/(t2*B) - Z*SR

    = 9.5462*1e5*2,542.7/(612*641.34) - 4.9243*67.622

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    = 684.131 kgf/cm2

    Allowable stress Sfa= 1,407.207 kgf/cm2

    Allowable stress Sna= 1,407.207 kgf/cm2

    STdoes not exceed SfaSHdoes not exceed Min[ 1.5*Sfa, 2.5*Sna] = 2,110.811 kgf/cm

    2

    SRdoes not exceed Sfa0.5(SH+ SR) = 553.422 kgf/cm

    2does not exceed Sfa

    0.5(SH+ ST) = 861.676 kgf/cm2

    does not exceed Sfa

    Flange rigidity per VIII-1 Appendix 2-14

    J = 52.14*V*Mo/(L*E*g02*KI*h0)

    = 1e5*52.14*0.2675*2,542.7/(3.2526*20.52E+05*6.332*0.3*63.72)= 0.6938

    The flange rigidity index J does not exceed 1; satisfactory.

    BRIDA CANAL --ESPEJO - Flange hub

    ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric

    Component: Flange hubMaterial specification: SA-105 (II-D Metric p. 18, ln. 5)Material is impact test exempt to -105 C per UCS-66(b)(3) (coincident ratio = 0.302)

    Internal design pressure: P = 7 kg/cm2@ 66 C

    Static liquid head:

    Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.17 mm,Operating head)

    Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal test

    head)

    Corrosion allowance Inner C = 3.17 mm Outer C = 0 mm

    Design MDMT = -17.78 C No impact test performedRated MDMT = -105 C Material is normalized

    Material is not produced to Fine Grain PracticePWHT is performed

    Radiography: Longitudinal joint - Seamless No RTLeft circumferential joint - Full UW-11(a) Type 1Right circumferential joint - N/A

    Estimated weight New = 4.8 kg corr = 3.2 kg

    Capacity New = 10.13 liters corr = 10.34 liters

    ID = 635 mmLengthLc

    = 32 mm

    t = 9.5 mm

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    Design thickness, (at 66 C) UG-27(c)(1)

    t = P*R / (S*E - 0.60*P) + Corrosion= 7.06*320.67 / (1,407.21*1.00 - 0.60*7.06) + 3.17= 4.79 mm

    Maximum allowable working pressure, (at 66 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t) - Ps

    = 1,407.21*1.00*6.33 / (320.67 + 0.60*6.33) - 0.06= 27.39 kg/cm2

    Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (317.5 + 0.60*9.5)= 41.36 kg/cm2

    Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)= 0.125 / (327 / 6.33)

    = 0.002420B = 1,092.5 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHC = min(B, S) = 1,092.5 kg/cm2

    Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 9.5)

    = 0.003631B = 1,169 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHN = min(B, S) = 1,169 kg/cm2

    Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 9.5)= 0.003631

    B = 1,169 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCN = min(B, S) = 1,169 kg/cm2

    Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.33)

    = 0.002420B = 1,092.5 kg/cm2

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    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCC = min(B, S) = 1,092.5 kg/cm2

    Allowable Compressive Stress, Vacuum and Corroded- ScVC, (tableCS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.33)

    = 0.002420B = 1,092.5 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScVC = min(B, S) = 1,092.5 kg/cm2

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    BRIDA CUERPO -- BONETE

    ASME VIII-1, 2010 Edition, A11 Addenda Metric, Appendix 2 Flange Calculations

    Flange is attached to: ENVOLVENTE 2 (Right)Flange type: Weld neck integralFlange material specification: SA-105 (II-D Metric p. 18, ln. 5)

    Bolt material specification:SA-193 B7 Bolt

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    17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 12.4 C, (coincident ratio = 0.779)Rated MDMT of -58.4C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mmBolts rated MDMT per Fig UCS-66 note (c) = -48 C

    The rated flange MDMT is -48 C

    Flange calculations for Internal Pressure + Weight Only

    Gasket details from facing sketch 1(a) or (b), Column II

    Gasket width N = 13 mm

    b0= N/2 = 6.5 mm

    Effective gasket seating width, b = 2.5*b01/2= 6.37 mm

    G = gasket OD - 2*b = 743 - 2*6.37 = 730.25 mm

    hG= (C - G)/2 = (799 - 730.25)/2 = 34.37 mm

    hD= R + g1/2 = 63 + 15.83/2 = 70.92 mm

    hT= (R + g1+ hG)/2 = (63 + 15.83 + 34.37)/2 = 56.6 mm

    Hp= 2*b*3.14*G*m*P= 0.01*2*6.37*3.14*730.25*3.75*11.5638= 12,673.56 kgf

    H = 0.785*G2*P= 0.01*0.785*730.252*11.5638= 48,407.99 kgf

    HD= 0.785*B2

    *P= 0.01*0.785*641.342*11.5638= 37,337.5 kgf

    HT= H - HD= 48,407.99 - 37,337.5= 11,070.49 kgf

    Wm1= H + Hp= 48,407.99 + 12,673.56= 61,081.54 kgf

    Per VIII-1 Appendix 2-5(a)(2): Wm1from the mating flange governs so Wm1= 61,101.6 kgf

    Wm2= 3.14*b*G*y= 0.01*3.14*6.37*730.25*534.3324= 78,081.84 kgf

    Required bolt area, Am= greater of Am1, Am2= 44.5187 cm2

    Am1= Wm1/Sb= 61,101.6/1,753.911 = 34.8373 cm2

    Am2= Wm2/Sa= 78,081.84/1,753.911 = 44.5187 cm2

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    Total area for 26- 0.875 in dia bolts, corroded, Ab= 48.1251 cm2

    W = (Am+ Ab)*Sa/2= (44.5187 + 70.2837)*1,753.911/2= 100,676.66 kgf

    MD= HD*hD= 37,337.5*0.0709 = 2,647.8 kgf-mMT= HT*hT= 11,070.49*0.0566 = 626.6 kgf-m

    HG= Wm1- H = 61,101.6 - 48,407.99 = 12,693.61 kgf

    MG= HG*hG= 12,693.61*0.0344 = 436.3 kgf-m

    Mo= MD+ MT+ MG= 2,647.8 + 626.6 + 436.3 = 3,710.7 kgf-m

    Mg= W*hG= 100,676.66*0.0344 = 3,460.5 kgf-m

    The bolts are adequately spaced so the TEMA RCB-11.23 load concentration factor does not apply.

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    Hub and Flange Factors

    g0= min(g0, tn) = min(6.33, 6.3) = 6.3

    h0= (B*g0)1/2= (641.34*6.3)1/2= 63.56 mm

    From FIG. 2-7.1, where K = A/B = 854/641.34 = 1.3316

    T = 1.7838 Z = 3.5869 Y = 6.9337 U = 7.6194

    h/h0= 0.5034 g1/g0= 2.5129

    F = 0.8161 V = 0.1837 e = F/h0= 0.1284

    d = (U/V)*h0*g02= (7.6194/0.1837)*6.3562*0.632

    = 104.6257 cm3

    Stresses at operating conditions - VIII-1 Appendix 2-7

    f = 1.9795

    L = (t*e + 1)/T + t3/d

    = (5.3*0.1284 + 1)/1.7838 + 5.33

    /104.6257= 2.365

    SH= f*Mo/(L*g12*B)

    = 1e5*1.9795*3,710.7/(2.365*15.832*641.34)= 1,932.593 kgf/cm

    2

    SR= (1.33*t*e + 1)*Mo/(L*t2*B)

    = (1.33*53*0.0128 + 1)*1e5*3,710.7/(2.365*532*641.34)= 165.914 kgf/cm

    2

    ST= Y*Mo/(t2*B) - Z*SR

    = 1e5*6.9337*3,710.7/(532*641.34) - 3.5869*165.914

    = 833.051 kgf/cm2

    Allowable stress Sfo= 1,407.207 kgf/cm2

    Allowable stress Sno= 1,407.207 kgf/cm2

    STdoes not exceed SfoSHdoes not exceed Min[ 1.5*Sfo, 2.5*Sno] = 2,110.811 kgf/cm

    2

    SRdoes not exceed Sfo0.5(SH+ SR) = 1,049.254 kgf/cm

    2does not exceed Sfo0.5(SH+ ST) = 1,382.822 kgf/cm

    2does not exceed Sfo

    Stresses at gasket seating - VIII-1 Appendix 2-7

    SH= f*Mg/(L*g12*B)= 1e5*1.9795*3,460.5/(2.365*15.832*641.34)= 1,802.302 kgf/cm

    2

    SR= (1.33*t*e + 1)*Mg/(L*t2*B)

    = (1.33*53*0.0128 + 1)*1e5*3,460.5/(2.365*532*641.34)= 154.729 kgf/cm

    2

    ST= Y*Mg/(t2*B) - Z*SR

    = 6.9337*1e5*3,460.5/(532*641.34) - 3.5869*154.729

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    = 776.889 kgf/cm2

    Allowable stress Sfa= 1,407.207 kgf/cm2

    Allowable stress Sna= 1,407.207 kgf/cm2

    STdoes not exceed SfaSHdoes not exceed Min[ 1.5*Sfa, 2.5*Sna] = 2,110.811 kgf/cm

    2

    SRdoes not exceed Sfa0.5(SH+ SR) = 978.515 kgf/cm

    2does not exceed Sfa

    0.5(SH+ ST) = 1,289.596 kgf/cm2

    does not exceed Sfa

    Flange rigidity per VIII-1 Appendix 2-14

    J = 52.14*V*Mo/(L*E*g02*KI*h0)

    = 1e5*52.14*0.1837*3,710.7/(2.365*20.14E+05*6.32*0.3*63.56)= 0.9859

    The flange rigidity index J does not exceed 1; satisfactory.

    BRIDA CUERPO -- BONETE - Flange hub

    ASME Section VIII Division 1, 2010 Edition, A11 Addenda Metric

    Component: Flange hubMaterial specification: SA-105 (II-D Metric p. 18, ln. 5)Material impact test exemption temperature from Fig UCS-66M Curve B = -29 C17 C MDMT reduction per UCS-68(c) applies.Fig UCS-66.1M MDMT reduction = 45.9 C, (coincident ratio = 0.4186)Rated MDMT of -91.9C is limited to -48C by UCS-66(b)(2)UCS-66 governing thickness = 9.5 mm

    Internal design pressure: P = 11.5 kg/cm2@ 90 C

    Static liquid head:

    Ps = 0.06 kg/cm2 (SG = 1, Hs= 638.17 mm,Operating head)

    Pth = 0.09 kg/cm2 (SG = 1, Hs= 907.5 mm, Horizontal test

    head)

    Corrosion allowance Inner C = 3.17 mm Outer C = 0 mm

    Design MDMT = -17.78 C No impact test performedRated MDMT = -48 C Material is normalized

    Material is not produced to Fine Grain PracticePWHT is performed

    Radiography: Longitudinal joint - Seamless No RT

    Left circumferential joint - Full UW-11(a) Type 1Right circumferential joint - N/A

    Estimated weight New = 4.8 kg corr = 3.2 kg

    Capacity New = 10.13 liters corr = 10.34 liters

    ID = 635 mmLengthLc

    = 32 mm

    t = 9.5 mm

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    Design thickness, (at 90 C) UG-27(c)(1)

    t = P*R / (S*E - 0.60*P) + Corrosion= 11.56*320.67 / (1,407.21*1.00 - 0.60*11.56) + 3.17= 5.82 mm

    Maximum allowable working pressure, (at 90 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t) - Ps

    = 1,407.21*1.00*6.33 / (320.67 + 0.60*6.33) - 0.06= 27.39 kg/cm2

    Maximum allowable pressure, (at 21.11 C) UG-27(c)(1)

    P = S*E*t / (R + 0.60*t)= 1,407.21*1.00*9.5 / (317.5 + 0.60*9.5)= 41.36 kg/cm2

    Allowable Compressive Stress, Hot and Corroded- ScHC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)= 0.125 / (327 / 6.33)

    = 0.002420B = 1,092.5 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHC = min(B, S) = 1,092.5 kg/cm2

    Allowable Compressive Stress, Hot and New- ScHN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 9.5)

    = 0.003631B = 1,169 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScHN = min(B, S) = 1,169 kg/cm2

    Allowable Compressive Stress, Cold and New- ScCN, (table CS-2 Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 9.5)= 0.003631

    B = 1,169 kg/cm2

    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2

    ScCN = min(B, S) = 1,169 kg/cm2

    Allowable Compressive Stress, Cold and Corroded- ScCC, (table CS-2Metric)

    A = 0.125 / (Ro/ t)

    = 0.125 / (327 / 6.33)

    = 0.002420B = 1,092.5 kg/cm2

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    S = 1,407.2 / 1.00 = 1,407.2 kg/cm2