Tri_P10

DUTY / CASE

Duty 1: Transfer of Trichloride from storage to Head H ead TankDrumming!/T ankDrumming!/Tanker anker "oading "oadi ng

C#$D%T%#$S (aterial )um*ed )hos*horus Trichloride )T0)um*ing Tem*erature C! 2 304lo5rate m6/h! Design 112 $ormal 7 Density kg/m6! 1898 u0+iscosity u0+iscosity c)! 2; ).*<0+a*our )ressure m=ar! +essel )ress =arA! Suction 1 Discharge Ctrl +l. "oss =ar! 222 E'ui*"oss =ar! #ri>ce mm! )i*e (aterial! CS Schedule $ominal Si?e ins! Suction  Discharge d@Actual %D mm! Suction 88 Discharge < At )um*ing )um*i ng Tem*erature Tem*erature

FRICTION HEAD LOSS ON SUCTION 4luid +elocity m/s! 0 1;16 -eynolds $o 0 196E28 4riction 4actor 0 221 )ressure Dro*  m Guid / 122m e' length 0





11 161 1 2 1222 ;2 18 ;29

See notes tes for for Calcu alcula lati tio on (eth ethod ;28

Total Total 4riction 4riction Head loss including including 18 safety factor! 0

FRICTION HEAD LOSS ON DISCHARGE 4luid +elocity m/s! 0 6 -eynolds $o 0 689E28 4riction 4actor 0 22 )ressure Dro*  m Guid / 122m e' length 0

%nformation highlighted in &"UE are re'uired entries +alues Highlighted in ,-EE$ are calculated .alues

26

m!

See notes for Calculation (ethod 1;968

Total Total 4riction 4riction Head loss including including 18 safety factor! 0

19962

m!

See notes for Actual *i*e diameters

SUCTION FITTINGS & VALVES TY)E 4ACT#$& B $o < )lug +al.e 2;  6 < 2 deg El=o5 2  ; < Std T Side 18  1 <  <  Total tal Suct ct +alF alF4it E' E' "engt ength hs m!

HEADm!  29 62; 2 2 1199

< "ength of Suct straight straight *i*e m! Total E'ui.alent Suct length m!

< < < < <

DISCHARGE FITTINGS & VALVES TY)E 4ACT#$& B $o )lug +al.e 2; 18 ; 2 deg El=o5 2 18 2 Std T SThru 28 18 ; 4lo5meter 2; 18 1 18 Total Disch +alF4it E' "engths m!

9 199

HEADm!  9 61 2 2 6

< "ength of Disch straight straight *i*e m! m! Total Total E'ui.alent Disch Disch length m! SUCTION & DISCHARGE HEADS +essel )ressure m "i' "e.el a=o.e *um* I =elo5 ! m Stat Head a=o.e *um* I=elo5 ! m Total Total 4ric 4ric Head "oss*lus "oss*lus +el +el Head!m Control +al.e see notes 1 and ! m #ri>ce see note  and 6! m E'ui*ment see note ! m Suc Head Sum@metres of 4luid@a=s Dis Head Sum@metres of 4luid@a=s DYNAMIC HEAD Discharge Head Sum Suction Head Sum TDH0Total Dynamic Head

SUCTION ;68 222

DISCHARGE ;68

1269 2222 2222 2222 6

98;1

98; m ;2 m 21.14 m

SYSTEM POWER < EJciencyn EJciencynote; ote;!0 !0 2 K1! Estimated )o5er0 777 LM! NOTES 1Assume control .al.e loss to =e 2 to 122 of *i*ing *lus e'ui*ment friction loss for initial calculation Consult instrument engineer for >nal selection All suction side .alues to =e in*ut negati.ely@ and discharge side .alues to =e in*ut *ositi.ely 6Control .al.es and ori>ces not normally used in *um* suction

NPSH Suction Head Sum ).* $)SH A.aila=le

6222 112 2222 2222 2222

91 1126

;2 m 29; m 6.55 m

;Use com=ined eJciency of *um* and dri.e

DUTY / CASE

Duty : Transfer of Trichloride from storage to -ecycle

C#$D%T%#$S (aterial )um*ed )hos*horus Trichloride )T0)um*ing Tem*erature C! 188 304lo5rate m6/h! Design 182 $ormal 7 Density kg/m6! 1898 u0+iscosity c)! 8 ).*<0+a*our )ressure m=ar! +essel )ress =arA! Suction 1 Discharge Ctrl +l. "oss =ar! 222 E'ui*"oss =ar! #ri>ce mm! )i*e (aterial! CS Schedule $ominal Si?e ins! Suction  Discharge d@Actual %D mm! Suction 88 Discharge < At )um*ing Tem*erature

FRICTION HEAD LOSS ON SUCTION 4luid +elocity m/s! 0 1 -eynolds $o 0 62E2; 4riction 4actor 0 22 )ressure Dro*  m Guid / 122m e' length 0





11 162 1 2 8 ;2 18 ;29

See notes for Calculation (ethod 1

Total 4riction Head loss including 18 safety factor! 0

FRICTION HEAD LOSS ON DISCHARGE 4luid +elocity m/s! 0 61 -eynolds $o 0 ;11E2; 4riction 4actor 0 228 )ressure Dro*  m Guid / 122m e' length 0


12

m!

See notes for Calculation (ethod 6191


91

m!


SUCTION FITTINGS & VALVES TY)E 4ACT#$& B $o < )lug +al.e 2;  6 < 2 deg El=o5 2  ; < Std T Side 18  1 <  <  Total Suct +alF4it E' "engths m!

HEADm!  29 62; 2 2 1199

< "ength of Suct straight *i*e m! Total E'ui.alent Suct length m!

< < < < <

DISCHARGE FITTINGS & VALVES TY)E 4ACT#$& B $o )lug +al.e 2; 18 ; 2 deg El=o5 2 18  Std T SThru 28 18 1 4lo5meter 2; 18 2 18 Total Disch +alF4it E' "engths m!

9 199

HEADm!  9; 29 2 2 1269

< "ength of Disch straight *i*e m! Total E'ui.alent Disch length m! SUCTION & DISCHARGE HEADS +essel )ressure m "i' "e.el a=o.e *um* I =elo5 ! m Stat Head a=o.e *um* I=elo5 ! m Total 4ric Head "oss*lus +el Head!m Control +al.e see notes 1 and ! m #ri>ce see note  and 6! m E'ui*ment see note ! m Suc Head Sum@metres of 4luid@a=s Dis Head Sum@metres of 4luid@a=s DYNAMIC HEAD Discharge Head Sum Suction Head Sum TDH0Total Dynamic Head

SUCTION ;68 1222

DISCHARGE ;68

 2222 2222 2222 816

616

61; m 81; m 26.60 m

SYSTEM POWER < EJciencynote;!0 2 K1! Estimated )o5er0 777 LM! NOTES 1Assume control .al.e loss to =e 2 to 122 of *i*ing *lus e'ui*ment friction loss for initial calculation Consult instrument engineer for >nal selection All suction side .alues to =e in*ut negati.ely@ and discharge side .alues to =e in*ut *ositi.ely 6Control .al.es and ori>ces not normally used in *um* suction


222 ;68 2222 9 2222

81; m 29; m 4.30 m

1; ;69


DUTY / CASE

Duty 6: Transfer of Trichloride from storage to Drum 4illing

C#$D%T%#$S (aterial )um*ed )hos*horus Trichloride )T0)um*ing Tem*erature C! 188 304lo5rate m6/h! Design 182 $ormal 7 Density kg/m6! 1898 u0+iscosity c)! 8 ).*<0+a*our )ressure m=ar! +essel )ress =arA! Suction 1 Discharge Ctrl +l. "oss =ar! 222 E'ui*"oss =ar! #ri>ce mm! )i*e (aterial! CS Schedule $ominal Si?e ins! Suction  Discharge d@Actual %D mm! Suction 88 Discharge < At )um*ing Tem*erature

FRICTION HEAD LOSS ON SUCTION 4luid +elocity m/s! 0 1 -eynolds $o 0 62E2; 4riction 4actor 0 22 )ressure Dro*  m Guid / 122m e' length 0





11 162 1 2 8 ;2 18 ;29

See notes for Calculation (ethod 1


FRICTION HEAD LOSS ON DISCHARGE 4luid +elocity m/s! 0 61 -eynolds $o 0 ;11E2; 4riction 4actor 0 228 )ressure Dro*  m Guid / 122m e' length 0


12

m!

See notes for Calculation (ethod 6191


6922

m!


SUCTION FITTINGS & VALVES TY)E 4ACT#$& B $o < )lug +al.e 2;  6 < 2 deg El=o5 2  ; < Std T Side 18  1 <  <  Total Suct +alF4it E' "engths m!

HEADm!  29 62; 2 2 1199

< "ength of Suct straight *i*e m! Total E'ui.alent Suct length m!

< < < < <

DISCHARGE FITTINGS & VALVES TY)E 4ACT#$& B $o )lug +al.e 2; 18 9 2 deg El=o5 2 18 2 Std T SThru 28 18  4lo5meter 2; 18 1 18 Total Disch +alF4it E' "engths m!

9 199

HEADm! 88 9 18 2 2 628

< "ength of Disch straight *i*e m! Total E'ui.alent Disch length m! SUCTION & DISCHARGE HEADS +essel )ressure m "i' "e.el a=o.e *um* I =elo5 ! m Stat Head a=o.e *um* I=elo5 ! m Total 4ric Head "oss*lus +el Head!m Control +al.e see notes 1 and ! m #ri>ce see note  and 6! m E'ui*ment see note ! m Suc Head Sum@metres of 4luid@a=s Dis Head Sum@metres of 4luid@a=s DYNAMIC HEAD Discharge Head Sum Suction Head Sum TDH0Total Dynamic Head

SUCTION ;68 1222

DISCHARGE ;68

 2222 2222 2222 816

81

8 m 81; m 54.48 m

SYSTEM POWER < EJciencynote;!0 2 K1! Estimated )o5er0 777 LM! NOTES 1Assume control .al.e loss to =e 2 to 122 of *i*ing *lus e'ui*ment friction loss for initial calculation Consult instrument engineer for >nal selection All suction side .alues to =e in*ut negati.ely@ and discharge side .alues to =e in*ut *ositi.ely 6Control .al.es and ori>ces not normally used in *um* suction


222 6618 2222 9 2222

2 1228

81; m 29; m 4.30 m


F()* !3 22 2 ;2 2 92 122 12

P!" C+, ! 192 192 192 1 1 1 1

S#$%! C'$ M'-.L,( M/.L,( ! ! 22 22 6  ; ; 11; 1;; 191 11   6 6

922 22

1911 18

Design )oint 1 Design )oint 

Pump vs System Head Curves Case:_________________________________ 45.0 40.0 ) m ( d a e H

35.0 30.0 25.0 20.0 15.0 10.0 5.0 0.0 0.0

2.0

4.0

6.0

8.0 Flow (m3/h)

10.0

12.0

Pump vs System Head Curves Case:_________________________________ 45.0 40.0 ) m ( d a e H

35.0 30.0 25.0 20.0 15.0 10.0 5.0 0.0 0.0

2.0

4.0

6.0

8.0

10.0

Flow (m3/h)

Pump Curve

Design Point 1

Design Point 2

Max.Level

Min.Level

12.0

Pump Curve

Design Point 1

Design Point 2

Max.Level

Min.Level

14.0

14.0

CENTRIFUGAL PUMP CALCULATION SHEET N)%$ '/ A$$!"%)/$

DATA ENTRY %nformation highlighted in &"UE are re'uired entries +alues Highlighted in ,-EE$ are calculated .alues

ACTUAL PIPE DIAMETERS N)!/'( P" S I/ 1 18  6 ; 8  9 12

S( 40 I/ !! 12; ; 112 ;29 2 882 629  ;2 12 82; 191 28 18;28 91 2 1222 8;81

EUIVALENT LENGTHS

,ate ,lo=e 5ye Angle

A%'( I/$ D'!%+ S( 80 PTFE L/ I/ !! I/ !! 28 ;61 29 191 1822 6912 161 66 16 ;8 19 ;6 22 6 92 11 69 19 6 882 ;912 11   81 1;66   8 169   8; ;6  

Enter ty*e and factor for each +al.e or 4itting follo5ed =y the $um=er F'%)+$ )+ V'(,$ 7)"/ '/ F%%/9$ 26; Dia*hr ; S5ing Chk 668 98; )lug +al.e 2; lr or MEld 28 ; 2 std El= 2 Teeside o 18 ;  ;8 std El= 2;

CENTRIFUGAL PUMP CALCULATION SHEET N)%$ '/ A$$!"%)/$

DATA ENTRY %nformation highlighted in &"UE are re'uired entries +alues Highlighted in ,-EE$ are calculated .alues

ACTUAL PIPE DIAMETERS N)!/'( P" S I/ 1 18  6 ; 8  9 12

S( 40 I/ !! 12; ; 112 ;29 2 882 629  ;2 12 82; 191 28 18;28 91 2 1222 8;81

A%'( I/$ D'!%+ S( 80 PTFE L/ I/ !! I/ !! 28 ;61 29 191 1822 6912 161 66 16 ;8 19 ;6 22 6 92 11 69 19 6 882 ;912 11   81 1;66   8 169   8; ;6  

EUIVALENT LENGTHS

,ate ,lo=e 5ye Angle

Enter ty*e and factor for each +al.e or 4itting follo5ed =y the $um=er F'%)+$ )+ V'(,$ 7)"/ '/ F%%/9$ 26; Dia*hr ; S5ing Chk 668 98; )lug +al.e 2; lr or MEld 28 ; 2 std El= 2 Teeside o 18 ; ;8 std El= 2;

FRICTION HEAD LOSS CALCULATIONS -eynolds $o

0

4luid +elocity

N

4luid Density N 4luid +iscosity

Actual Diameter

%f -e O 122 4ormula taken from Std T6 Std 8@ A**roNimate (oody 4ormula! 4riction 4actor

0

22288 N

P 1   2@222 N )i*e -oughness  1222222 P )i*e Diameter -eynolds $o !Q

4riction 4actor

0

; -eynolds $o

)ressure Dro*

0

8122 N 4riction 4actor N +elocityR Diameter

or %f -e K 122

Ty*e of )i*e )i*e -oughness mm! Dra5n Tu=ing Co**er@ ,lass@ Stainless Steel 22218 Commercial Steel )i*e 22; As*halt Di**ed Cast %ron )i*e 21 ,al.inised %ron )i*e 218 &are Cast %ron )i*e 2 Concrete )i*e 26  62 -i.eted Steel )i*e 2  2

!QR266

Tri_P10

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