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Group: Facilities Services Department
Team Members: Michael Postler and Craig Guenette
Start Date: September 08, 2009
UNCLASSIFIED
UNCLASSIFIED 1
 The System
 Commencement
 As-Built Updates LPL
 As-Built Updates FAB
 Setup for Calculations
 Existing Calculations
 Existing Suggestions
 Problems to be Solved
UNCLASSIFIED
UNCLASSIFIED
 Solutions
 New Design
 New Pipe Routes
 Proposals
 Proposals (continued)
 New Calculations
 Selection
 Questions?
2
 What is Process Cooling Water?
 What is this system used for?
 How does it differ from Chilled Water?
 Why is it advantageous?
UNCLASSIFIED
UNCLASSIFIED 3
 Initial assignment
 Update As-Built drawings
 Calculate existing head loss
 Make design suggestions
 New condition 250 GPM  330 GPM
UNCLASSIFIED
UNCLASSIFIED 4
 Briefed on the “potential” hazards in ML
 Field surveyed in Lower Process Level
 Updated As-Built drawings
UNCLASSIFIED
UNCLASSIFIED 5
 Coordinated a visit to the clean room
 Field surveyed in upper process level
 Updated As-Built drawings
UNCLASSIFIED
UNCLASSIFIED 6
 Assigned numerical values for equipment
 Verified all pipe dimensions and pipe fittings
 Documented all pressure and flow readings
at equipment
UNCLASSIFIED
UNCLASSIFIED 7
 Identified critical areas (greatest head loss)
 Created spreadsheets for problem areas
 Interpreted results with present system
(Ideal operating pressure: 106 psig)
Pipe Pipe Equiv. Friction Loss Section Accum.
Item Size GPM Length Fitting Length Velocity (per 100 ft.) dP dP
(in.) (ft.) Qty. (ft.) (fps) (ft.) (ft.) (ft.)
PCW Return 4 245 5 1 6.404 4.059 0.2029 208.5385
Ball Valve 4 245 1 2.5 6.404 4.059 0.1015 208.6400
PCW Return 2 245 1 1 25.617 103.003 1.0300 209.6700
Union 2 245 1 0.45 25.617 103.003 0.4635 210.1335
90° Elbow 2 245 1 12 25.617 103.003 12.3603 222.4938
PCW Return 2 245 1 1 25.617 103.003 1.0300 223.5238
Pumps 2 245 1 25.617 103.003 0.0000 223.5238
+10 % SAFETY FACTOR 245.8762
UNCLASSIFIED
UNCLASSIFIED 8
 Evaluated critical friction losses
 Manipulated pipe diameters on spreadsheet
 Suggestions were made to save head loss
 Example: Existing LPL tool #34 has 260.7 ft.
of head loss (112.8 psig). With suggestions the
updated system will have 180.9 ft. of head loss
(78.3 psig). This suggestion will save 79.8 ft. of
head loss (34.5 psig).
UNCLASSIFIED
UNCLASSIFIED 9
 Losing 21 psig (102-81 psig) across filters
 Discrepancy of 16 psig between the pressure
gauges and the controls system
 In bay 11 - equipment would occasionally
shut down during operation
 Cracked 45° elbow on riser 11
UNCLASSIFIED
UNCLASSIFIED 10
 Pressure analysis performed, controls –
calibration issue
 After recalibration pump supply went from
102 psig to 86 psig
 In bay 11 – there was not enough pressure
at the equipment and pump output pressure
was increased
 The cracked 45° elbow on riser 11, will be
replaced during the next shutdown
UNCLASSIFIED
UNCLASSIFIED 11
 250 GPM  330 GPM
 Existing system HL = 302.4 ft. (130.9 psig)
requiring 65 HP
 Existing pumps will not handle flow increase
 Existing heat exchanger must be
modified/replaced
UNCLASSIFIED
UNCLASSIFIED 12
 Four different options for main headers
UNCLASSIFIED
UNCLASSIFIED 13
 Two main 4” headers off 5” SS Main
 Filters to be moved to accommodate new
header design
UNCLASSIFIED
UNCLASSIFIED 14
 28 Plates to be added to the Heat
Exchangers (65-93)
 Pumps and motors on VFD to be replaced
 Automatic air vents to be installed on all
risers
UNCLASSIFIED
UNCLASSIFIED 15
 Incorporated new flows, piping and fittings
 Assigned new critical equipment
 New operating pressure: 95 psig (42 HP)
UNCLASSIFIED
UNCLASSIFIED
Pipe Pipe Equiv. Friction Loss Section Accum.
Item Size GPM Length Fitting Length Velocity (per 100 ft.) dP dP
(in.) (ft.) Qty. (ft.) (fps) (ft.) (ft.) (ft.)
PCW Return 5 330 5 1 5.521 2.488 0.1244 193.7651
Ball Valve 5 330 1 3.1 5.521 2.488 0.0771 193.8422
PCW Return 5 330 1 1 5.521 2.488 0.0249 193.8671
Union 5 330 1 0.65 5.521 2.488 0.0162 193.8833
90° Elbow 5 330 1 15 5.521 2.488 0.3732
Suction Diffuser 5X4 330 1 1.850 1.8500 195.7333
PCW Return 4 330 1 1 8.626 7.046 0.0705 195.8037
Pumps 4 330 1 8.626 7.046 0.0000 195.8037
+10 % SAFETY FACTOR 215.3841
16
 Close coupled, stainless steel 40 HP pumps
 Heat exchangers to be upgraded to 93
plates and reconditioned
 Stainless steel suction diffuser and triple
duty valves
 Relocation of filter housings with 20 micron
filters to be installed
UNCLASSIFIED
UNCLASSIFIED 17
UNCLASSIFIED
UNCLASSIFIED 18

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Facilities Services Process Cooling Water Upgrade

  • 1. Group: Facilities Services Department Team Members: Michael Postler and Craig Guenette Start Date: September 08, 2009 UNCLASSIFIED UNCLASSIFIED 1
  • 2.  The System  Commencement  As-Built Updates LPL  As-Built Updates FAB  Setup for Calculations  Existing Calculations  Existing Suggestions  Problems to be Solved UNCLASSIFIED UNCLASSIFIED  Solutions  New Design  New Pipe Routes  Proposals  Proposals (continued)  New Calculations  Selection  Questions? 2
  • 3.  What is Process Cooling Water?  What is this system used for?  How does it differ from Chilled Water?  Why is it advantageous? UNCLASSIFIED UNCLASSIFIED 3
  • 4.  Initial assignment  Update As-Built drawings  Calculate existing head loss  Make design suggestions  New condition 250 GPM  330 GPM UNCLASSIFIED UNCLASSIFIED 4
  • 5.  Briefed on the “potential” hazards in ML  Field surveyed in Lower Process Level  Updated As-Built drawings UNCLASSIFIED UNCLASSIFIED 5
  • 6.  Coordinated a visit to the clean room  Field surveyed in upper process level  Updated As-Built drawings UNCLASSIFIED UNCLASSIFIED 6
  • 7.  Assigned numerical values for equipment  Verified all pipe dimensions and pipe fittings  Documented all pressure and flow readings at equipment UNCLASSIFIED UNCLASSIFIED 7
  • 8.  Identified critical areas (greatest head loss)  Created spreadsheets for problem areas  Interpreted results with present system (Ideal operating pressure: 106 psig) Pipe Pipe Equiv. Friction Loss Section Accum. Item Size GPM Length Fitting Length Velocity (per 100 ft.) dP dP (in.) (ft.) Qty. (ft.) (fps) (ft.) (ft.) (ft.) PCW Return 4 245 5 1 6.404 4.059 0.2029 208.5385 Ball Valve 4 245 1 2.5 6.404 4.059 0.1015 208.6400 PCW Return 2 245 1 1 25.617 103.003 1.0300 209.6700 Union 2 245 1 0.45 25.617 103.003 0.4635 210.1335 90° Elbow 2 245 1 12 25.617 103.003 12.3603 222.4938 PCW Return 2 245 1 1 25.617 103.003 1.0300 223.5238 Pumps 2 245 1 25.617 103.003 0.0000 223.5238 +10 % SAFETY FACTOR 245.8762 UNCLASSIFIED UNCLASSIFIED 8
  • 9.  Evaluated critical friction losses  Manipulated pipe diameters on spreadsheet  Suggestions were made to save head loss  Example: Existing LPL tool #34 has 260.7 ft. of head loss (112.8 psig). With suggestions the updated system will have 180.9 ft. of head loss (78.3 psig). This suggestion will save 79.8 ft. of head loss (34.5 psig). UNCLASSIFIED UNCLASSIFIED 9
  • 10.  Losing 21 psig (102-81 psig) across filters  Discrepancy of 16 psig between the pressure gauges and the controls system  In bay 11 - equipment would occasionally shut down during operation  Cracked 45° elbow on riser 11 UNCLASSIFIED UNCLASSIFIED 10
  • 11.  Pressure analysis performed, controls – calibration issue  After recalibration pump supply went from 102 psig to 86 psig  In bay 11 – there was not enough pressure at the equipment and pump output pressure was increased  The cracked 45° elbow on riser 11, will be replaced during the next shutdown UNCLASSIFIED UNCLASSIFIED 11
  • 12.  250 GPM  330 GPM  Existing system HL = 302.4 ft. (130.9 psig) requiring 65 HP  Existing pumps will not handle flow increase  Existing heat exchanger must be modified/replaced UNCLASSIFIED UNCLASSIFIED 12
  • 13.  Four different options for main headers UNCLASSIFIED UNCLASSIFIED 13
  • 14.  Two main 4” headers off 5” SS Main  Filters to be moved to accommodate new header design UNCLASSIFIED UNCLASSIFIED 14
  • 15.  28 Plates to be added to the Heat Exchangers (65-93)  Pumps and motors on VFD to be replaced  Automatic air vents to be installed on all risers UNCLASSIFIED UNCLASSIFIED 15
  • 16.  Incorporated new flows, piping and fittings  Assigned new critical equipment  New operating pressure: 95 psig (42 HP) UNCLASSIFIED UNCLASSIFIED Pipe Pipe Equiv. Friction Loss Section Accum. Item Size GPM Length Fitting Length Velocity (per 100 ft.) dP dP (in.) (ft.) Qty. (ft.) (fps) (ft.) (ft.) (ft.) PCW Return 5 330 5 1 5.521 2.488 0.1244 193.7651 Ball Valve 5 330 1 3.1 5.521 2.488 0.0771 193.8422 PCW Return 5 330 1 1 5.521 2.488 0.0249 193.8671 Union 5 330 1 0.65 5.521 2.488 0.0162 193.8833 90° Elbow 5 330 1 15 5.521 2.488 0.3732 Suction Diffuser 5X4 330 1 1.850 1.8500 195.7333 PCW Return 4 330 1 1 8.626 7.046 0.0705 195.8037 Pumps 4 330 1 8.626 7.046 0.0000 195.8037 +10 % SAFETY FACTOR 215.3841 16
  • 17.  Close coupled, stainless steel 40 HP pumps  Heat exchangers to be upgraded to 93 plates and reconditioned  Stainless steel suction diffuser and triple duty valves  Relocation of filter housings with 20 micron filters to be installed UNCLASSIFIED UNCLASSIFIED 17