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Home My WebLink AboutBuilding Permit #808 - 1025 OSGOOD STREET 6/7/2007 %►ORTH BUILDING PERMIT o� a �a TOWN OF NORTH ANDOVER o? I, APPLICATION FOR PLAN EXAMINATION : Permit NO: � Date Received! SSACHUSfc Date Issued: r IMPORTANT: Applicant must complete all items on this page ]LOCATION /0.'122� 'P t PROPERTY OWNERS Ci �f3 _IC Pnnt - MAP NO; PARCEL ZONING DISTRICT:._.: '' HISTORIC DISTRICT yes no TYPE OF IMPROVEMENT PROPOSED USE - Residential ! '` Non-Residential ❑ New Building ❑ One family ❑ Addition ❑ Two or more family ❑ Industrial fj Alteration No. of units: - - ❑ Co mercial ❑ Repair, replacement ❑ Assessory Bldg Others: "O Demolition ❑ Other Cl Septic ❑ 1Nell r: ❑ Floodplain �❑Wetlands ❑ Watershed Distnc` Y' HCl UVate_r/Sewer, DESCRIPTION OF WORK TO BE PREFORMED: - - Identification Please Type_,or Print Clearly) OWNER: Name: - Phone: Address: - - - - - - ;x k CONTRACTOR Name .X1245 S� .GJ UsTi>ev� I�IJ l�//��hore a Address: :' "!cJl�'Iu P1 5 j iJ4, ✓t/DD✓ S Vit%: Supervisor's Construction License C f19 Exp Date: Home lmprouement License / f /" Exp Date-: . s ARCHITECT/ENGINEER ___ __ Phone: 7 25' 5 cfl;1 C Address: Reg.INo. _ FEE SCHEDULE:BULDING PERMIT:$12.00 PER$1000.00 OF THE TOTAL ESTIMATED COST BASED ON$125.00 PER S.F. Total Project Cost: $ 4 (3 C� FEE: Check No.: �' ` d Receipt No.: NOTE: Persons contracting with unregistered contractors do not have access to the guaranty fund T Signature of A ent/Owner Si9 nature of contractors __g _. �_ _ _ __ y__u Plans Submitted ❑ Plans Waived ❑ Certified Plot Plan ❑ Stamped Plans ❑ TYPE OF SEWERAGE DISPOSAL Public Sewer ❑ Tanning/Massage/Body Art ❑ Swimming Pools ❑ Well ❑ Tobacco Sales ❑ Food Packaging/Sales ❑ Private(septic tank,etc. ❑ Permanent Dumpster on Site ❑ THE FOLLOWING SECTIONS FOR OFFICE USE ONLY INTERDEPARTMENTAL SIGN OFF - U FORM DATE REJECTED DATE APPROVED PLANNING & DEVELOPMENT ❑ ❑ COMMENTS DATE REJECTED DATE APPROVED CONSERVATION ❑ ❑ COMMENTS f' DATE REJECTED DATE APPROVED HEALTH ❑ ❑ COMMENTS Zoni�q Board of Appeals: Variance, Petition No: Zoning Decision/receipt submitted yes Planning Board Decision: Comments Conservation Decision: Comments Water & Sewer Connection/Signature & Date Driveway Permit Located at 384 Osgood Street FIRE DEPARTMt'V Terj bel¢ rwsi yes Yv: rt Frxe 15Partlrnern: r�ra77 trr �iate "� `�•-y��ra � .:r` � � �.�,'� �. ��;- F � � *t''rx "&ay�L��,r7 .�. `3 r �COMMENTSf Dimension Number of Stories: Total square feet of floor area, based on Exterior dimensions. Total land area, sq. ft.: ELECTRICAL: Movement of Meter location, mast or service drop requires approval of Electrical Inspector Yes No DANGER ZONE LITERATURE: Yes No MGL Chapter 166 Section 21A—F and G min.$100-$1000 fine NOTES and DATA— For department use I ❑ Notified for pickup - Date Doc.Building Permit Revised 2007 Building Department The following is a list of the required forms to be filled out for the appropriate permit to be obtained Roofing, Siding, Interior Rehabilitation Permits ❑ Building Permit Application ❑ Workers Comp Affidavit ❑ Photo Copy Of H.I.C. And/Or C.S.L. Licenses o Copy of Contract ❑ Floor Plan Or Proposed Interior Work ❑ Engineering Affidavits for Engineered products NOTE: All dumpster permits require sign off from Fire Department prior to issuance of Bldg Permit Addition Or Decks ❑ Building Permit Application ❑ Certified Surveyed Plot Plan ❑ Workers Comp Affidavit ❑ Photo Copy of H.I.C. And C.S.L. Licenses ❑ Copy Of Contract ❑ Floor/Crossection/Elevation Plan Of Proposed Work With Sprinkler Plan And Hydraulic Calculations (If Applicable) ❑ Mass check Energy Compliance Report (If Applicable) ❑ Engineering Affidavits for Engineered products NOTE: All dumpster permits require sign off from Fire Department prior to issuance of Bldg Permit New Construction (Single and Two Family) ❑ Building Permit Application ❑ Certified Proposed Plot Plan ❑ Photo of H.I.C. And C.S.L. Licenses ❑ Workers Comp Affidavit ❑ Two Sets of Building Plans (One To Be Returned) to Include Sprinkler Plan And Hydraulic Calculations (If Applicable) ❑ Copy of Contract ❑ Mass check Energy Compliance Report ❑ Engineering Affidavits for Engineered products NOTE: All dumpster permits require sign off from Fire Department prior to issuance of Bldg Permit In all cases if a variance or special permit was required the Town Clerks office must stamp the decision from the Board of Appeals that the appeal period is over. The applicant must then get this recorded at the Registry of Deeds. One copy and proof of recording must be submitted with the building application Doc:INSPECTIONAL SERVICES DEPARTMENT:BPFORM07 Revised 2.2007 1 Location r , No. Date N�RTh TOWN OF NORTH ANDOVER �. Of� .•o ,•,'t'O ' Certificate of Occupancy $ CMusEt� Building/Frame Permit Fee $ I Foundation Permit Fee $ Other Permit Fee $ t TOTAL $ F Check # r 4 t r 20277 .-......� Building Inspector Maugel Architects Inc. Construction Control Affidavit April 19, 2007 Project Location: Flourishes Fit-Up 1025 Osgood Street- Retail Building North Andover, MA 01845 In accordance with section 116.0 of the Massachusetts State Building Code, 780 CMR,: I;Brent A. Maugel, Registration No..5554, being a registered professional architect hereby certify that I have directly supervised the preparation of all design plans' and construction documents for the above named project and that, to the. best of my-knowledge, such plans meet the applicable provisions of the Massachusetts State Building Code and the Americans with Disabilities Act. All acceptable engineering practices and all applicable laws and ordinances for the proposed use and occupancy will be adhered to. further certify that Maugel Architects, Inc. will perform the necessary professional services on the construction site to determine that the work will be done in . accordance with the documents appy r building permit. \�,�� \the �v Aril 19 2007. Brent A. May(/el-A. . CD No.55y Date Maugel Arc ects, 200 Ayer Ro a .r ,NM 51 `y1T,; M' Commonwealth of Massachusetts County of Worcest r C On this. ')'� 4_day of,� 200,before me,the undersigned Notary Public,personally appeared Brent A. Mauael A.I.A.,proved to me through satisfactory evidence of identification,which was/Wefe personal kno%,0edne,to be the person(s).r,hose name(e)is=r—e signed on the preceding or attached document in my presence,and who swore or affirmed to me that the contents of the document are truthful andwagryte to the best of his/kief knowledge and belief. Signature Notary s �E�1 My commission expires y• . Z Maugel Architects Inc. 200 Ayc-t Road Harvard,Mei 01451 t:978-456-2800 f:078-466-280,1 www.maugel.com 780 CMR, Section 903 Building Permit Narrative Report Retail Building 1025 Osgood Street Treadwells North Andover, MA April 13,2007 Section 1 —Building Description a) Building Use Group; 1025 Osgood Street is Business and Mercantile& Treadwells is use group A-3 b) Square Footage; 1025 Osgood Street 15,312 sf., Treadwells 1,475 sf c) Building Height; 1025 Osgood Street is less than 40 feet in building height, Treadwells less than 20 feet d) Number of Floors: 1025 Osgood Street 2 stories, Treadwells 1 stories, plus basement e) Number of Floors Below Grade: 1025 Osgood Street 1, Treadwells 1 f) Square Feet per Floor: 1025 Osgood Street 7,656 sf, Treadwells 1,475sf g) Type of Occupancy: 1025 Osgood Street is a retail building, Treadwells is a Resturant h) Type of Construction; Type 5B i) Hazardous Materials: N/A j) Storage over 12 feet: N/A k) Site Access: Fire department vehicle access is provided via site parking lots to the buildings Section 2—Applicable Laws,Regulations and Standards a) 780 CMR, sixth edition,Massachusetts State Building Code b) NFPA 13, 2002 edition. c) MGL, Chapter 148 d) 527 CMR,Fire Prevention Regulations e) Local Laws are N/A f) Specialized codes are N/A g) Federal Laws are N/A Section 3-Design Responsibility for Fire Protection Systems Michael J. Joanis,PE Fire Protection Engineer 12 Settlers Ridge Road Windham,NH 03087 MA registration#39974 Section 4—Fire Protection Systems to be Installed Complete automatic wet pipe sprinkler protection for all heated building areas and complete automatic dry pipe sprinkler protection for all unheated building areas in accordance with 780 CMR, sixth edition, and NFPA 13, 2002 edition. Section 5—Features Used in the Design Methodology N/A Section 6—Special Consideration and Description ti I N/A 903.1.1 Sequence of Operation Wet Pipe Systems • Heat from a fire melts the fusible link on a sprinkler • Sprinkler plug releases and water flows from the open sprinkler(s) • Water flow switch is activated • Water flow switch initiates the fire alarm system to notify building occupants and the North Reading Fire Department • Water continues to flow until manually turned off Dry Pipe Systems • Heat from a fire melts the fusible link on a sprinkler • Sprinkler plug releases and air is released from the piping system. • Reduced air pressure activates a low air supervisory alarm to the building fire alarm system. • Dry alarm valve opens and permits piping to fill with water. • Water flows from the open sprinkler(s) • Pressure switch is activated indicating water flow • Pressure switch initiates the fire alarm system to notify building occupants and the North Andover Fire Department • Water continues to flow until manually turned off Testing Criteria Fire protection systems shall be tested in accordance with NFPA 13, 2002 edition, including hydrostatic testing and functional testing. Testing shall be conducted by the fire protection contractor who shall also provide all required testing equipment and provide NFPA 13 test certificates. Testing shall be witnessed and approved by the engineer of record and the North Andover Fire Department. Sincerely, el J. Joanis, PE Fire Protection Engineer 12 Settlers Ridge Road Windham,NH 03087 Cell: 617 438 2820 michaeljoanisna comcat.net CAM Joanis\Projects\1025 Osgood Street\bldg permit narrative report 4-13-07.doc ISD AF 3 l 1 FIRE PROTECTION DESIGN AFFIDAVIT Permit No. To the Commissioner, Inspectional Services Department. Re: Bella Vita Salon&Day Spa, Treadwells, and Core and Shell Tenant Space 1025 Osgood Street,North Andover, MA I certify that to the best of my knowledge, information and belief,the plans and computations accompanying the attached application concerning the locus at: 1025 Osgood Street,North Andover, MA Ward are in accordance with the requirements of the Massachusetts State Building Code and all other pertinent laws and ordinances. _ "OF gJ . Michael J. Joanis — 39974 �o MICHAEL J. yG ENGINEER—MA. REG. NO. JOANIS rt, FIRE PROTECTION 313 Congress Street, Boston, MA 02210 No.39V4 ADDRESS NAL 617-330-9390 PHONE April 12, 2 07 Then personally appeared the above named Michael J. Joanis, PE and made oath that the above statement by him is true. Before me, My Commission Expires: �i , 20 MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ' 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C' C A L C U L A T I O N S C O V E R S H E E T LIGHT HAZ. , BUSINESS, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER, MA W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 �P�A OF Ss9 B 0 0 S T E R P U M P S �� MICHAEL J. y� NUMBER OF BOOSTER PUMPS 0 O JOANIS a v FIRE PROTECTION y No.39974 S P R I N K L E R S A'p0 9F NA " MAXIMUM SPACING OF SPRINKLERS (ft) 14 MAXIMUM SPACING OF SPRINKLER LINES (ft) 14 SPECIFIED DISCHARGE DENSITY (gpm/sq. ft. ) .1 THIS SPRINKLER SYSTEM WILL DELIVER A DENSITY OF .1 gpm/sq. ft. FOR A DESIGN AREA OF 900 SQ. FT. OF FLOOR AREA THIS SYSTEM OPERATES AT A FLOW OF 257.36 gpm AT A PRESSURE OF 61.84 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 a- MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER LIGHT HAZ. , BUSINESS, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER, MA PAGE--------------------------------------------------------------------------------------------- 1 SPRINKLER SYSTEM ANALYSIS TO SHOW THE MAXIMUM DENSITY AVAILABLE WITH ZERO PRESSURE REMAINING --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ J TEST AREA 1 [ ] TEST AREA 2 [ } TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 208 5.60 13.00 31.77 32.18 209 5. 60 13.00 33.04 34 .80 210 5.60 13.00 31.28 31.22 210 5. 60 13.00 31.29 31.22 213 5. 60 13.00 36.21 41.80 219 5. 60 13.00 25.87 21.35 220 5. 60 13.00 25.95 21. 47 221 5. 60 13.00 25.85 21.31 222 5. 60 13.00 27. 43 23. 99 223 5. 60 13.00 29.55 27.85 225 5. 60 13.00 39. 68 50.21 THE SPRINKLER SYSTEM FLOW IS 337. 93 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.132 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605. 00 gpm TOTAL SYSTEM FLOW 437. 93 gpm AVAILABLE PRESSURE 98.06 psi AT 437. 93 gpm OPERATING PRESSURE 98.06 psi AT 437. 93 gpm PRESSURE REMAINING 0.00 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A BACKFLOW PREVENTER [ ] METER [ J DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER LIGHT HAZ. , BUSINESS, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER, MA PAGE 2 NHH~~~N~~~~~NNNNNNNN ~ ~~~~~~N~N~~~~~N~~N~~NNNN~NN~~N~N~ HYDRAULICCALCULATIONSATSPECIFIEDDENSITY -------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 208 5. 60 13.00 24 .17 18. 63 209 5. 60 13.00 25.18 20.22 210 5.60 13.00 23.84 18.13 210 5. 60 13.00 23.84 18.13 213 5.60 13.00 27. 68 24 .44 219 5. 60 13.00 19.58 12.22 220 5. 60 13.00 19. 62 12.27 221 5. 60 13.00 19. 60 12.25 222 5. 60 13.00 20.89 13. 92 223 5. 60 13.00 22.57 16.24 225 5. 60 13.00 30.38 29.43 THE SPRINKLER SYSTEM FLOW IS 257.36 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.100 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 357.36 gpm AVAILABLE PRESSURE 98.68 psi AT 357.36 gpm OPERATING PRESSURE 61.84 psi AT 357.36 gpm PRESSURE REMAINING 36.84 psi ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [� BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER LIGHT HAZ. , BUSINESS, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER, MA PAGE 3 NNryNNNNryNNN FITTING Equivalent Length per NFPA 13 1994, 6-4 .3 -' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3='T'/Cross, 4=Butterfly Valve, 5=Gate Valve, 6=Swing Check Valve ------------- FROM TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIC. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) --------------------------------------------------------------------------------------------- 1 2 257.36 200.00 3522 88.14 140 111 6. 400 0.002 0.000 61.84 61.36 0.48 2 3 257.36 5.00 22 17. 96 120 2 4.260 0.016 0.000 61.36 61.00 0.37 3 4 257.36 5.00 0.00 120 2 4 .260 0.016 0.000 61.00 57 . 92 3.08 4 5 257.36 1.50 0.00 120 2 4.260 0.016 0.000 57. 92 57 . 89 0.02 5 6 257.36 8.00 2462 62.84 120 2 4 .260 0.016 0.000 57.89 0. 43 57.46 6 200 257.36 36.00 22 11.78 120 2 2. 635 0.166 5. 633 0.43 43. 10 -48.30 200 201 257.36 50.00 22 11.78 120 2 2. 635 0.166 0.000 43.10 32. 85 10.25 201 202 226.98 14 .00 0.00 120 2 2. 635 0.132 0.000 32.85 31. 15 1.70 202 203 124 .72 6.00 22 11.78 120 2 2.635 0.043 0.000 31.15 30.33 0.82 203 204 97.04 5.50 0.00 120 2 2. 635 0.027 0.000 30.33 30. 18 0.15 204 205 97.04 13.00 3 6.40 120 1 1. 610 0.300 0.000 30.18 24 .35 5.83 205 206 49.36 12.00 0.00 120 1 1.380 0.182 0.000 24 .35 22. 13 2.22 206 207 24 .17 12.00 0.00 120 1 1.049 0.184 0.000 22.13 19. 94 2. 19 207 208 24.17 2.00 222 5. 10 120 1 1.049 0.184 0. 000 19.94 18. 63 1.31 206 209 25.18 2.00 322 7. 60 120 1 1.049 0.199 0. 000 22.13 20.22 1. 91 205 210 47. 68 2.00 322 7. 60 120 1 1.049 0. 649 0. 000 24.35 18 . 13 6.23 203 211 27.68 1.00 3 5.30 120 1 1.380 0.062 0. 000 30.33 29. 91 0.42 211 212 27. 68 7.00 0.00 120 1 1.049 0.237 0. 000 29. 91 28 .25 1.66 212 213 27.68 11.00 222 5.10 120 1 1.049 0.237 0.000 28.25 24 .44 3.82 202 214 102.26 12.00 3 6.40 120 1 1. 610 0.331 0.000 31.15 25.06 6.09 214 215 102.26 17.00 22 5.20 120 1 1. 610 0.331 0.000 25.06 17 .72 7.35 215 216 79.69 12.00 0.00 120 1 1. 610 0.208 0. 000 17.72 15.20 2.52 216 217 58.80 9.50 0.00 120 1 1. 610 0.119 0. 000 15.20 14 .04 1.16 217 218 39.20 0.50 0.00 120 1 1.380 0.119 0. 000 14 .04 13. 98 0.05 218 219 19.58 9.00 222 5.10 120 1 1.049 0.125 0. 000 13.98 12.22 1.76 218 220 19. 62 6.00 322 7. 60 120 1 1.049 0.125 0.000 13. 98 12.27 1.71 217 221 19. 60 5.00 3222 9.30 120 1 1.099 0.125 0.000 14.04 12.25 1.79 216 222 20.89 1.50 322 7. 60 120 1 1.049 0.141 0.000 15.20 13. 92 1.28 215 223 22.57 1.50 322 7. 60 120 1 1.049 0.162 0.000 17.72 16.24 1.48 201 224 30.38 15.50 3 6.40 120 1 1. 610 0.035 0.000 32.85 32.08 0.77 224 225 30.38 6.00 22 3.40 120 1 1.049 0.282 0.000 32.08 29.43 2. 65 A MAX. VELOCITY OF 17. 69 ft. /sec. OCCURS BETWEEN REF. PT. 205 AND 210 Sprinkler-CALC Release 7.2 Win By Walsh Engineering Inc. North Kingstown R.I. U.S.A. WATER SUPPLY�DEMAND GRAPH LIGHT HA?.,BUSINESS,WET PIPE, UPPER LEVEL,1025 OSGOOD ST, N. ANDOVER, MA 150.00 140.00 130.00 P 110.00 _ _... _. R R 100.00 F € 3 : E 50.003 S 80.00 70.00 r € U 60.00 , R 50.00 E 40.00 3 , i _ 30.00 20.00 ,M _ 10.00 - _ .. ____ 0.00 1 <v_ _...M ,__ ------- ..___� 0 500 1000 1500 2000 Supply: x'8.00 psi 1605.00 gpm /TN Demand: 61.84 psi �� 357.36 gpm } FLOW a srirllr L' 7Wrti MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C C A L C U L A T I O N S C 0 V E R S H E E T ORD. HAZ. II, FUTURE RETAIL, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 B O O S T E R P U M P S NUMBER OF BOOSTER PUMPS 0 S P R I N K L E R S MAXIMUM SPACING OF SPRINKLERS (ft) 10 MAXIMUM SPACING OF SPRINKLER LINES (ft) 13 SPECIFIED DISCHARGE DENSITY (gpm/sq. ft. ) .2 THIS SPRINKLER SYSTEM WILL DELIVER A DENSITY OF .2 gpm/sq. ft. FOR A DESIGN AREA OF 1000 SQ. FT. OF FLOOR AREA THIS SYSTEM OPERATES AT A FLOW OF 301.05 gpm AT A PRESSURE OF 71.31 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 t MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ORD. HAZ. II, FUTURE RETAIL, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER PAGE--------------------------------------------------------------------------------------------- 1 SPRINKLER SYSTEM ANALYSIS TO SHOW THE MAXIMUM DENSITY AVAILABLE WITH 'ZERO PRESSURE REMAINING --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 103 5. 60 14 .00 38.30 46.77 104 5. 60 14 .00 36.39 42.23 105 5. 60 14 .00 35.09 39.26 106 5. 60 14 .00 33.76 36.34 107 5. 60 14.00 32.41 33.48 108 5. 60 14.00 31.12 30.89 109 5. 60 14.00 37.33 44.44 110 5. 60 14 .00 35. 11 39.30 111 5. 60 14.00 39. 93 50.83 112 5. 60 14 .00 39. 65 50.13 THE SPRINKLER SYSTEM FLOW IS 359.10 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 250.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.239 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605. 00 gpm TOTAL SYSTEM FLOW 609.10 gpm AVAILABLE PRESSURE 96.39 psi AT 609. 10 gpm OPERATING PRESSURE 96.39 psi AT 609.10 gpm PRESSURE REMAINING 0.00 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [v] BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ORD. HAZ. II, FUTURE RETAIL, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER PAGE 2 --------------------------------------------------------------------------------------------- HYDRAULIC CALCULATIONS AT SPECIFIED DENSITY --------------------------------- ----------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ J TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 103 5.60 14 .00 32.16 32.98 104 5.60 14 .00 30.49 29. 64 105 5.60 14 .00 29.45 27. 65 106 5.60 14 .00 28.28 25.49 107 5.60 14 .00 27.06 23.35 108 5.60 14 .00 26.00 21.55 109 5.60 14 .00 31.34 31.32 110 5.60 14 .00 29.40 27.55 111 5.60 14 .00 33.55 35.88 112 5.60 14 .00 33.32 35.39 THE SPRINKLER SYSTEM FLOW IS 301.05 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 250.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.200 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 551.05 gpm AVAILABLE PRESSURE 97.01 psi AT 551.05 gpm OPERATING PRESSURE 71.31 psi AT 551.05 gpm PRESSURE REMAINING 25.70 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [� BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ORD. HAZ. II, FUTURE RETAIL, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER PAGE 3 ------------------------------------------------------------------------------------------- FITTING Equivalent Length per NFPA 13 1994, 6-4.3 '-' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3='T' /Cross, 4=Butterfly Valve, 5=Gate Valve, 6=Swing Check Valve ------------------------------------- FROM TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIC. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) --------------------------------------------------------------------------------------------- 1 2 301.05 200.00 3522 88.14 140 111 6. 400 0.002 0.000 71.31 70. 67 0. 64 2 3 301.05 5.00 22 17. 96 120 2 4 .260 0.021 0.000 • 70.67 70.18 0.49 3 4 301.05 5.00 0.00 120 2 4 .260 0.021 0.000 70.18 67. 07 3.11 4 5 301.05 1.50 0.00 120 2 4 .260 0.021 0.000 67.07 66. 94 0.13 5 6 301.05 8.00 2462 62.84 120 2 4 .260 0.021 0.000 66.94 65.43 1.52 6 100 301.05 78.00 2222 23.56 120 2 2. 635 0.222 6.067 65.43 36. 82 22.54 100 101 234 .18 12. 10 0.00 120 2 2. 635 0.139 0.000 36.82 35.25 1.57 101 102 62. 65 12. 10 0.00 120 2 2. 635 0.012 0.000 35.25 35. 08 0. 18 102 103 62. 65 3.00 22 4 . 40 120 - 1 1.380 0.283 0.000 35.08 32. 98 2. 09 103 104 30.49 10.00 2 1.70 120 1 1.049 0.283 0.000 32.98 29. 64 3.34 101 105 110.79 7.00 33 12.80 120 1 1. 610 0.384 0.000 35.25 27 . 65 7. 60 105 106 81.34 10.00 0.00 120 1 1. 610 0.217 0. 000 27. 65 25. 49 2. 16 106 107 53.06 10.00 0.00 120 1 1.380 0.208 0. 000 25.49 23.35 2. 14 107 108 26.00 7. 00 2 1.70 120 1 1.049 0.211 0.000 23.35 21. 55 1. 80 101 109 60.74 4 .00 33 10. 60 120 1 1.380 0.267 0.000 35.25 31. 32 3. 93 109 110 29.40 10.00 3 4 .20 120 1 1.049 0.265 0.000 31.32 27. 55 3.77 100 111 33.55 7.00 332 15.40 120 1 1. 610 0.042 0.000 36.82 35.88 0. 94 100 112 33.32 4 .00 332 12.80 120 1 1.380 0.088 0.000 36.82 35.39 1. 44 A MAX. VELOCITY OF 17.71 ft./sec. OCCURS BETWEEN REF. PT. 6 AND 100 Sprinkler-CALC Release 7.2 Win By Walsh Engineering Inc. North Kingstown R.I. U.S.A. l WATER SUPPLY/DEMAND GRAPH I ORD. HA%. II,FUTURE RETAILr't�,IET PIPE, UPPER LEVEL,1025 OSGOOD ST, N. ANDOVER 150.00 140.00 i 130.00 [ • I , E 120.00 rl P 110.00 :71ii - r- t ..._... i ._.# r ... ... .. - - _ .. � .... - 4 ., _.. __s_. p R 100.00 ,' �� E 90.00 .��-_ ._ _. _ E } S 80.00 $ S S 70.00 U 60.00 R 50.00 E 40.00 30.00 20.00 € 4 10.00 � 0.00 Gr 560 1000 1500 2000 Supply 75.00 psi 1605.00 9PM FLOW Demand 71.31 psi 01551.05 gpm ' rih� lr- L ' 1irti R MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C C A L C U L A T I O N S C 0 V E R S H E E T ATTIC SYSTEM, DRY PIPE, 1025 OSGOOD ST, N. ANDOVER, MA W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 B O O S T E R P U M P S NUMBER OF BOOSTER PUMPS 0 S P R I N K L E R S MAXIMUM SPACING OF SPRINKLERS (ft) 20 MAXIMUM SPACING OF SPRINKLER LINES (ft) 19 SPECIFIED DISCHARGE DENSITY (gpm/sq. ft. ) .1 THIS SPRINKLER SYSTEM WILL DELIVER A DENSITY OF .1 gpm/sq. ft. FOR A DESIGN AREA OF 1500 SQ. FT. OF FLOOR AREA THIS SYSTEM OPERATES AT A FLOW OF 283.57 gpm AT A PRESSURE OF 63.55 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ATTIC SYSTEM, DRY PIPE, 1025 OSGOOD ST, N. ANDOVER, MA PAGE--------------------------------------------------------------------------------------------- 1 SPRINKLER SYSTEM ANALYSIS TO SHOW THE MAXIMUM DENSITY AVAILABLE WITH ZERO PRESSURE REMAINING --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 315 8.00 28.00 52.49 43.04 316 8.00 28.00 50.81 40.33 317 8.00 28.00 50.21 39.38 318 8.00 28.00 52.49 43.04 319 8.00 28.00 50.80 40.33 320 8.00 28.00 50.22 39.40 325 8.00 28.00 66. 68 69.47 THE SPRINKLER SYSTEM FLOW IS 373.69 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.132 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 473.69 gpm AVAILABLE PRESSURE 97.75 psi AT 473. 69 gpm OPERATING PRESSURE 97.75 psi AT 473. 69 gpm PRESSURE REMAINING 0.00 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [•� BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE M ! MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ATTIC SYSTEM, DRY PIPE, 1025 OSGOOD ST, N. ANDOVER, MA PAGE 2 --------------------------------------------------------------------------------------------- HYDRAULIC CALCULATIONS AT SPECIFIED DENSITY --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ) TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ) REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 315 8.00 28.00 39. 83 24 .78 316 8.00 28.00 38. 49 23.14 317 8.00 28.00 38. 00 22.56 318 8.00 28.00 39. 82 24 .77 319 8.00 28.00 38.49 23.14 320 8.00 28.00 38.00 22.56 325 8.00 28.00 50. 95 40.56 THE SPRINKLER SYSTEM FLOW IS 283.57 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 -gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.100 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 383.57 gpm AVAILABLE PRESSURE 98.49 psi AT 383.57 gpm OPERATING PRESSURE 63.55 psi AT 383.57 gpm PRESSURE REMAINING 34.94 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [✓] BACKFLOW PREVENTER [ J METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ATTIC SYSTEM, DRY PIPE, 1025 OSGOOD ST, N. ANDOVER, MA PAGE 3 --------------------------------------------------------------------------------------------- FITTING Equivalent Length per NFPA 13 1994, 6-4 .3 '-' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3='T' /Cross, 4=Butterfly Valve, S=Gate Valve, 6=Swing Check Valve -------------------------------- FROM TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIC. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) --------------------------------------------------------------------------------------------- 1 2 283.57 200.00 3522 88. 14 140 111 6.400 0.002 0.000 63.55 62.98 0.57 2 3 283.57 5.00 22 17. 96 120 2 4 .260 0.019 0.000 62. 98 62.54 0.44 3 4 283.57 5.00 0.00 120 2 4 .260 0.019 0.000 62.54 59.44 3. 10 4 5 283.57 1.50 0.00 120 2 4.260 0.019 0.000 59.44 59.42 0.03 5 7 283.57 3.00 0.00 120 2 4 .260 0.019 0.000 59.42 59.36 0.06 7 8 283.57 10.00 2562 35. 42 100 2 4 .260 0.027 0.000 59.36 58.16 1.20 8 300 283.57 41.00 222 19.22 100 2 4 .260 0.027 6.500 58. 16 50.04 1. 62 300 301 283.57 20.00 2 6.41 100 2 4 .260 0.027 0.000 50.04 49.33 0.71 301 302 232. 62 35.00 2 4 .20 100 2 2. 635 0.193 0.000 49.33 41.77 7.56 302 303 0.00 29.00 0.00 100 2 2. 635 0.000 0.000 41.77 41.77 0. 00 303 304 0. 00 20.00 0.00 100 2 2. 635 0.000 0.000 41.77 41.77 0.00 304 305 0.00 8.00 22 8.40 100 2 2. 635 0.000 3.033 41.77 38.73 -0. 00 305 306 0.00 3.00 32 6.42 100 1 1. 610 0.000 0.000 38.73 38.73 0.00 305 307 0.00 3.00 32 6. 42 100 1 1. 610 0.000 0.000 38.73 38.73 0.00 303 308 0.00 15.00 32 14.76 100 2 2. 635 0.000 5. 633 41.77 36.13 -0.00P 308 309 0.00 2.00 3 4.57 100 1 1. 610 0.000 0.000 36. 13 36.13 0.00 309 310 0.00 6.00 0.00 100 1 1. 610 0.000 0.000 36. 13 36.13 0. 00 310 311 0.00 6.00 2 1.85 100 1 1. 610 0.000 0.000 36. 13 36.13 0.00 308 312 0.00 4 .00 3 4 .57 100 1 1. 610 0.000 0.000 36.13 36.13 0.00 312 313 0.00 6.00 2 1.85 100 1 1. 610 0.000 0.000 36. 13 36.13 0.00 302 314 232. 62 21.00 32 14 .76 100 2 2. 635 0.193 5.633 41.77 29.24 6. 90 314 315 116.31 3.00 3 4 .57 100 1 1. 610 0.589 0.000 29.24 24 .78 4. 45 315 316 76. 49 6.00 0.00 100 1 1. 610 0.271 0.000 24 .78 23.14 1. 64 316 317 38.00 6.00 2 1.85 100 1 1. 610 0.074 0.000 23. 14 22.56 0.58 314 318 116.31 3.00 3 4.57 100 1 1. 610 0.589 0.000 29.24 24.77 4.46 318 319 76.49 6.00 0.00 100 1 1. 610 0.271 0.000 24 .77 23.14 1. 63 319 320 38.00 6.00 2 1.85 100 1 1. 610 0.074 0.000 23.14 22.56 0.58 301 321 50. 95 1.10 3 15.07 100 2 4 .260 0.001 0.000 49.33 49.31 0.02 321 322 50. 95 21.00 32 14 .76 100 2 2. 635 0.012 5. 633 49.31 43.30 0.38 322 323 50. 95 3.00 3 4 .57 100 1 1. 610 0.128 0.000 43.30 42.33 0. 97 323 324 50. 95 6.00 0.00 100 1 1. 610 0.128 0.000 42.33 41.56 0.77 324 325 50. 95 6.00 2 1.85 100 1 1. 610 0.128 0.000 41.56 40.56 1.00 322 326 0.00 3.00 3 4.57 100 1 1. 610 0.000 0.000 43.30 43.30 0.00 326 327 0.00 6.00 0.00 100 1 1. 610 0.000 0.000 43.30 43.30 0.00 327 328 0.00 6.00 2 1.85 100 1 1. 610 0.000 0.000 43.30 43.30 0.00 A MAX. VELOCITY OF 18.32 ft./sec. OCCURS BETWEEN REF. PT. 314 AND 315 Sprinkler-CALC Release 7.2 Win By Walsh Engineering Inc. North Kingstown R.I. U.S.A. WATER SUPPLY/DEMAND GRAPH ATTIC SYSTEM,DRY PIPE, 1025 OSGOOD ST,N. ANDOVER, MA 150.00 � F f r _ ryr i 140.00 ; 130.00 120.00 _ P 110.00 E _ __ _ g 100.00 E 90.00 S 80.00 (' S 70.00 j$(('7 � - - - -- - } i' R 50.00 E 40.00 30.00 t , 20.00 10.00 __ , 0.00 4- 0 500 1 000 1500 2000 S upplu: 78.00 psi 1505.00 gpmFLOW tv Demand 53.55 psi Cf,383 57 gpm tthikl r 1 MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C C A L. 0 U. L A T I 0 N S C O V E R S H E E T BASEMENT, WET PIPE, ORD. HAZ. GRP1, TREADWELLS, NORTH ANDOVER, MA W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 B O O S T E R P U M P S NUMBER OF BOOSTER PUMPS 0 S P R I N K L E R S MAXIMUM SPACING OF SPRINKLERS (ft) 14 MAXIMUM SPACING OF SPRINKLER LINES (ft) 9 SPECIFIED DISCHARGE DENSITY (gpm/sq. ft. ) .15 THIS SPRINKLER SYSTEM WILL DELIVER A DENSITY OF .15 gpm/sq. ft. FOR A DESIGN AREA OF 900 SQ. FT. OF FLOOR AREA THIS SYSTEM OPERATES AT A FLOW OF 189.51 gpm AT A PRESSURE OF 31.18 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 • MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER BASEMENT, WET PIPE, ORD. HAZ. GRP1, TREADWELLS, NORTH ANDOVER, MA PAGE--------------------------------------------------------------------------------------------- 1 SPRINKLER SYSTEM ANALYSIS TO SHOW THE MAXIMUM DENSITY AVAILABLE WITH ZERO PRESSURE REMAINING --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 505 5.60 3.00 39.74 50.36 506 5.60 3.00 37.11 43. 90 507 5.60 3.00 38. 61 47.52 508 5. 60 3.00 36.05 41.43 510 5.60 3.00 41.27 54 .30 511 5. 60 3.00 38.55 47.37 512 5. 60 3.00 42.28 56. 99 513 5. 60 3.00 39.53 49.83 514 5.60 3. 00 45.27 65.33 THE SPRINKLER SYSTEM FLOW IS 358.39 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 250.00 gpm ( ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.286 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 608.39 gpm AVAILABLE PRESSURE 96.39 psi AT 608.39 gpm OPERATING PRESSURE 96.39 psi AT 608.39 gpm PRESSURE REMAINING 0.00 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [�] BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER BASEMENT, WET PIPE, ORD. HAZ. GRP1, TREADWELLS, NORTH ANDOVER, MA PAGE 2 NNNNNNNryNNMNrvryNNNNNryNNMNryNryryNNNNNNNNNNNNNryNNNNNNNNNNNN HYDRAULICCALCULATIONSATSPECIFIEDDENSITY -------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm, psi 505 5. 60 3.00 21.01 14 .07 506 5. 60 3.00 19.50 12. 13 507 5. 60 3.00 20.36 13.22 508 5. 60 3.00 18. 90 11.39 510 5.60 3.00 21.88 15.26 511 5.60 3.00 20.32 13.16 512 5. 60 3.00 22.48 16.11 513 5. 60 3.00 20.87 13.88 514 5. 60 3.00 24.20 18.67 THE SPRINKLER SYSTEM FLOW IS 189.51 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 250.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.150 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 439.51 gpm AVAILABLE PRESSURE 98.05 psi AT 439.51 gpm OPERATING PRESSURE 31.18 psi AT 439.51 gpm PRESSURE REMAINING 66.86 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [ � BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER BP4SEMENT, WET PIPE, ORD. HAZ. GRP1, TREADWELLS, NORTH ANDOVER, MA PAGE 3 --------------------------------------------------------------------------------------------- FITTING Equivalent Length per NFPA 13 1994, 6-4 .3 '-' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3='T' /Cross, 4=Butterfly Valve, S=Gate Valve, 6=Swing Check Valve FROM TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIC. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) -------------------------------------------------------------------------------------ti------- 1 2 189.51 200.00 3522 88. 14 140 111 6.400 0.001 0.000 31.18 30. 91 0.27 2 3 189.51 3.00 22 17. 96 120 2 4.260 0.009 0.000 30.91 30.72 0. 19 3 4 189.51 5.00 0.00 120 2 4.260 0.009 0.000 30.72 27. 68 3.05 4 5 189.51 2.00 0.00 120 2 4 .260 0.009 0.000 27. 68 27. 66 0. 02 5 7 189.51 3.00 0.00 120 2 4 .260 0.009 0.000 27.66 27. 67 -0. 02 7 8 189.51 10.00 2562 49. 64 120 2 4 .260 0.009 0.000 27. 67 27.13 0. 54 8 500 189.51 37 .00 2222 23.56 120 2 2. 635 0.094 1.300 27.13 20. 13 5. 70 500 501 165.31 8.50 0.00 120 2 2. 635 0.073 0.000 20.13 19.48 0. 65 501 502 121. 97 12.50 22 11.78 120 2 2. 635 0.042 0.000 19.48 18.45 1. 03 502 503 79.77 8.50 0.00 120 2 2. 635 0.019 0.000 18.45 18.29 0. 16 503 504 40.51 8.50 0.00 120 2 2. 635 0.005 0.000 18.29 18.24 0. 05 504 505 40.51 7.00 2 1.70 120 1 1.049 0.480 0.000 18.24 14 .07 4 . 17 505 506 19.50 14 .00 2 1.70 120 1 1.049 0.124 0.000 14 .07 12.13 1. 94 503 507 39.26 7.00 3 4 .20 120 1 1.049 0.453 0.000 18.29 13.22 5. 07 507 508 18.90 14 .00 2 1.70 120 1 1.049 0.117 0.000 13.22 11.39 1. 83 502 509 42.20 3.00 3 5.30 120 1 1.380 0.136 0.000 18. 45 17.33 1. 12 509 510 42.20 4 .00 0.00 120 1 1.049 0.517 0.000 17.33 15.26 2. 07 510 511 20.32 14 .00 2 1.70 120 1 1.049 0.134 0.000 15.26 13.16 2. 10 501 512 43.34 2.00 3 4 .20 120 1 1.049 0.544 0.000 19.48 16.11 3.37 512 513 20.87 14 .00 2 1.70 120 1 1.049 0.140 0.000 16.11 13.88 2.22 500 514 24.20 2.00 32 5. 90 120 1 1.049 0.185 0.000 20. 13 18. 67 1.46 A MAX. VELOCITY OF 16.08 ft./sec. OCCURS BETWEEN REF. PT. 501 AND 512 Sprinkler-CALC Release 7.2 Win By Walsh Engineering, Inc. North Kingstown R.I. U.S.A. WATER SUPPLY/DEMAND GRAPH 150.00 L. , BASEMENT,WET PIPE, ORD. HAZ. GRP1, TREADWELLS, NORTH ANDOVER, MA 140.00 130.00 6 f i t 120.00 P 110.00 i 7 ;_.. _ R 100.00 E 90.00 . I S $a.as _Mf 70.00U 60.00 _ t _._...w._Aa.- f a _ _ w•._ 1 R ! 50.00 40.00 s 90.00 20.00 10.00 0.00 a 500 1000 1500 2000 Supply: 7$.00 psi 1605.00 gpm FLa Demand: 1.1$ psi 409.51 gpm r rir~ lr- L �.. " F y F x l �3 MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C C A L C U L A T I O N S C O V E R S H E E T FIRST FLOOR, WET PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 B O O S T E R P U M P S NUMBER OF BOOSTER PUMPS 0 S P R I N K L E R S MAXIMUM SPACING OF SPRINKLERS (ft) 16 MAXIMUM SPACING OF SPRINKLER LINES (ft) 16 SPECIFIED DISCHARGE DENSITY (gpm/sq. ft. ) .1 THIS SPRINKLER SYSTEM WILL DELIVER A DENSITY OF . 1 gpm/sq. ft. FOR A DESIGN AREA OF 1000 SQ. FT. OF FLOOR AREA THIS SYSTEM OPERATES AT A FLOW OF 362.40 gpm AT A PRESSURE OF 85.04 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER FIRST FLOOR, WET PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE 1 ------------------ -------------------------------------------------------------------------- SPRINKLER SYSTEM ANALYSIS TO SHOW THE MAXIMUM DENSITY AVAILABLE WITH ZERO PRESSURE REMAINING --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 407 8.00 14 .00 39. 62 24 . 53 408 5. 60 14 .00 30.06 28. 81 411 5. 60 14 .00 30. 98 30. 60 412 8.00 14 .00 41. 64 27.09 413 5. 60 14 .00 31.91 32. 46 415 5. 60 14 .00 29.93 28.56 l 416 5. 60 14 .00 30.78 30.20 419 5. 60 14.00 27.87 24 .77 420 5. 60 14.00 29.23 27.24 422 8.00 14 . 00 43. 90 30. 12 424 5. 60 14 .00 27.77 24 .59 425 5. 60 14. 00 29.05 26. 92 THE SPRINKLER SYSTEM FLOW IS 392.75 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.108 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605. 00 gpm TOTAL SYSTEM FLOW 492.75 gpm AVAILABLE PRESSURE 97.57 psi AT 492.75 gpm OPERATING PRESSURE 97.57 psi AT 492.75 gpm PRESSURE REMAINING 0.00 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [V] BACKFLOW PREVENTER [ ] METER DETECTOR CHECK VALVE L ] OTHER DEVICE L • MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER FIRST FLOOR, WET PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE 2 --------------------------------------------------------------------------------------------- HYDRAULIC CALCULATIONS AT SPECIFIED DENSITY --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 407 8.00 14 .00 36.52 20.83 408 5. 60 14 .00 27.74 24 .54 411 5. 60 14 .00 28.58 26.04 412 8.00 14 .00 38.39 23.03 413 5. 60 14 .00 29.45 27. 66 415 5. 60 14.00 27.67 24 .41 416 5. 60 14 .00 28 .44 25.78 419 5. 60 14 .00 25. 65 20. 98 420 5. 60 14 .00 26. 99 23.22 422 8.00 14 .00 40.59 25.73 424 5. 60 14 .00 25. 60 20.90 425 5. 60 14.00 26.79 22.88 THE SPRINKLER SYSTEM FLOW IS 362.40 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0. 100 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 462.40 gpm AVAILABLE PRESSURE 97.85 psi AT 462.40 gpm OPERATING PRESSURE 85.04 psi AT 462.40 gpm PRESSURE REMAINING 12.81 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [ � BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE l_ MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER FPRST FLOOR, WET PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE 3 ~~~N~~~~~~NH~H~~ FITTING Equivalent Length per NFPA 13 1994, 6-4.3 '-' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3=1T' /Cross, 4=Butterfly Valve, 5=Gate Valve, 6=Swing Check Valve -------------------- FROM TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIG. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) --------------------------------------------------------------------------------------------- 1 2 362.40 200.00 3522 88. 14 140 111 6.400 0.003 0.000 85.04 84 . 14 0. 90 2 3 362.40 3.00 22 17. 96 120 2 4 .260 0.030 0.000 84 . 14 83.51 0. 63 3 4 362.40 5.00 0.00 120 2 4 .260 0.030 0.000 83.51 80.35 3.15 4 5 362.40 2.00 0.00 120 2 4 .260 0.030 0.000 80. 35 80.29 0.06 5 7 362.40 3.00 0.00 120 2 4 .260 0.030 0.000 80.29 80.20 0.09 7 8 362.40 10.00 2562 49. 64 120 2 4 .260 0.030 0.000 80.20 78.45 1.75 8 400 362.40 50.00222222 35.34 120 2 2. 635 0.313 0.000 78. 45 51.75 26.70 400 401 362.40 14 .00 222 17. 67 120 2 2. 635 0.313 6.067 51.75 35.78 9.91 401 402 321.81 5.00 0.00 120 2 2. 635 0.251 0.000 35.78 34 .51 1.26 402 403 213.07 8.00 0.00 120 2 2. 635 0.117 0.000 34 .51 33.50 1.01 403 404 116. 65 3.00 0.00 120 2 2. 635 0.038 0.000 33.50 33.43 0.07 404 405 64 .26 6.00 0.00 120 2 2. 635 0.013 0.000 33.43 33.36 0.08 405 406 64.26 3.00 22 4 .22 120 2 1.097 0. 907 0.000 33.36 26.81 6.55 406 407 36.52 10.00 222 5.10 120 1 1.049 0.396 0.000 26.81 20.83 5. 98 406 408 27.74 2.00 322 7.60 120 1 1.049 0.238 0.000 26.81 24 .54 2.27 403 409 96.42 3.00 32 9.00 120 1 1. 610 0.297 0.000 33.50 29. 94 3.56 409 410 66.97 6.00 0.00 120 1 1.380 0.320 0.000 29.94 28 .08 1. 87 410 411 28.58 3.00 222 5.10 120 1 1.049 0.251 0.000 28. 08 26.04 2. 04 410 412 38.39 4 .00 322 7.60 120 1 1.049 0.434 0.000 28. 08 23.03 5.05 409 413 29.45 1.00 322 7.60 120 1 1.049 0.266 0.000 29. 94 27. 66 2.29 402 414 56.11 1.00 32 5.90 120 1 1.049 0.877 0.000 34 .51 28.46 6.05 414 415 27.67 12.00 222 5.10 120 1 1.049 0.237 0.000 28. 46 24 .41 4.05 414 416 28.44 3.00 322 7.60 120 1 1.049 0.249 0.000 28. 46 25.78 2. 68 402 417 52. 64 6.00 32 5. 90 120 1 1.049 0.779 0.000 34 .51 25. 16 9.35 417 418 25. 65 14 .00 0.00 120 1 1.049 0.206 0.000 25. 16 22.24 2. 92 418 419 25. 65 1.00 222 5.10 120 1 1.049 0.206 0.000 22.24 20. 98 1.26 417 420 26. 99 1.00 322 7.60 120 1 1.049 0.226 0.000 25. 16 23.22 1. 94 401 421 40.59 3.00 32 7.50 120 1 1.380 0.127 0.000 35.78 34 .45 1.33 421 422 40.59 13.00 222 5.10 120 1 1.049 0.481 0.000 34 . 45 25.73 8.71 404 423 52.39 5.00 32 5.90 120 1 1.049 0.772 0.000 33. 43 25.02 8. 42 423 424 25. 60 15.00 222 5.10 120 1 1.049 0.205 0.000 25. 02 20. 90 4. 12 423 425 26.79 2.00 322 7. 60 120 1 1.049 0.223 0.000 25. 02 22.88 2. 14 A MAX. VELOCITY OF 21.81 ft./sec. OCCURS BETWEEN REF. PT. 405 AND 406 Sprinkler-CALC Release 7.2 Win By Walsh Engineering Inc. North Kingstown R.I. U.S.A. l f • WATER SUPPLY/DEMAND GRAPH FIRST FLOOR,WET PIPE,LIGHT HAZARD, TREAD' ELLS, NORTH ANDOVER, MA 150.00 ; .} _ _i .µ_ ¢. 140.00 130.00 =t� 120.00 1 ,. . w.. .. _. ,..._.. _. ._._ i P 110.00 _ + _ , R 100.00 __ __ ------ S M__ E 90.00 ...��.. �.. _ ___ �-�-- _.�_ --�__ S 70.00 U 60.00 -77' R 50.00 _ E 4a.0a ~ ------------- 30.0041 --- 20.00 10.00 0.00 a Sao 1000 1500 2000 ' Supply: 78.oo psi 1605.00 gpm FLOW Demand: 55.04 psi 'a 462.40 fpm rir kir- L` '� 1 F S � MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C C A L C U L A T I O N S C 0 V E R S H E E T ATTIC, DRY PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 B O O S T E R P U M P S NUMBER OF BOOSTER PUMPS 0 S P R I N K L E R S MINIMUM FLOW PER SPRINKLER (gpm) 38 MINIMUM PRESSURE PER SPRINKLER (psi) 22.56 THIS SYSTEM OPERATES AT A FLOW OF 232.59 gpm AT A PRESSURE OF 52.58 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 * MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ATTIC, DRY PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE--------------------------------------------------------------------------------------------- 1 SYSTEM ANALYSIS TO SHOW MAXIMUM FLOW WITH ZERO PRESSURE REMAINING --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 611 8.00 18.00 58.18 52.88 612 8.00 18.00 56.30 49.53 613 8.00 18.00 55. 62 48.32 614 8.00 18.00 58.16 52.85 615 8.00 18.00 56.28 49.49 616 8.00 18.00 55. 63 48.35 THE SPRINKLER SYSTEM FLOW IS 340.17 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 440.17 gpm AVAILABLE PRESSURE 98.04 psi AT 440.17 gpm OPERATING PRESSURE 98.04 psi AT 440.17 gpm PRESSURE REMAINING 0.00 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A. [✓] BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ATTIC, DRY PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE 2 ---------------------------------------------------------------------------------------------- HYDRAULIC CALCULATIONS AT SPECIFIED FLOW --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 611 8.00 18.00 39.83 24 .79 612 8.00 18.00 38.47 23.12 613 8.00 18.00 38.00 22.56 614 8.00 18.00 39.83 24 .78 615 8.00 18.00 38.47 23.12 616 8.00 18.00 38.00 22.56 THE SPRINKLER SYSTEM FLOW IS 232.59 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 332.59 gpm AVAILABLE PRESSURE 98.85 psi AT 332.59 gpm OPERATING PRESSURE 52.58 psi AT 332.59 gpm PRESSURE REMAINING 46.27 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [ J� BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ATTIC, DRY PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE 3 --------------------------------------------------------------------------------------------- FITTING Equivalent Length per NFPA 13 1994, 6-4.3 '-' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3='T' /Cross, 4=Butterfly Valve, S=Gate Valve, 6=Swing Check Valve FROM TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIC. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) --------------------------------------------------------------------------------------------- 1 2 232.59 200.00 3522 88. 14 140 111 6.400 0.001 0.000 52.58 52.18 0.40 2 3 232.59 3.00 22 17. 96 120 2 4.260 0.013 0.000 52. 18 51. 90 0.28 3 4 232.59 5.00 0.00 120 2 4 .260 0.013 0.000 51. 90 48.84 3. 07 4 5 232.59 2.00 0.00 120 2 4 .260 0.013 0.000 48.84 48.81 0. 03 5 6 232.59 8.00 2462 44 .83 100 2 4.260 0.019 0.000 48.81 47.83 0. 98 6 600 232.59 52.00 22222 32.03 100 2 4.260 0.019 0.000 47.83 46.27 1. 56 600 601 232.59 14 .00 2 6.41 100 2 4.260 0.019 7.800 46.27 38.10 0. 36 601 602 232.59 13.00 2 4 .20 100 2 2.635 0.193 0.000 38.10 34.79 3.32 602 603 232.59 2.00 0.00 100 2 2.635 0.193 0.000 34.79 34.40 0.39 603 604 232.59 3.00 0.00 100 2 2. 635 0.193 0.000 34 . 40 33. 82 0.58 604 605 0.00 13.00 0.00 100 2 2. 635 0.000 0.000 33.82 33. 82 0. 00 605 606 0.00 12.00 23 5.35 100 1 1.380 0.000 0.000 33. 82 33. 82 0.00 606 607 0.00 10.00 0. 00 100 1 1.049 0.000 0.000 33. 82 33.82 0. 00 607 608 0.00 2.00 2 1.21 100 1 1.049 0.000 0.000 33. 82 33.82 0.00 605 609 0.00 7.00 23 4 .21 100 1 1.049 0.000 0.000 33.82 33.82 0.00 604 610 232.59 9.00 32 14 .76 100 2 2.635 0.193 0.000 33.82 29.24 4.58 610 611 116.30 3.00 3 4 .57 100 1 1.610 0.589 0.000 29.24 24 .79 4 .45 611 612 76.47 6.00 0.00 100 1 1. 610 0.271 0.000 24 .79 23.12 1. 67 612 613 38.00 6.00 2 1.85 100 1 1.610 0.074 0.000 23. 12 22.56 0.56 610 614 116.30 3.00 3 4 .57 100 1 1.610 0.589 0.000 29.24 24 .78 4.46 614 615 76.47 6.00 0.00 100 1 1.610 0.271 0.000 24 .78 23.12 1. 66 615 616 38.00 6.00 2 1.85 100 1 1. 610 0.074 0.000 23.12 . 22.56 0.57 603 617 0.00 12.00 32 4 .21 100 1 1.049 0.000 0.000 34.40 34.40 0. 00 617 618 0.00 9.00 2 1.21 100 1 1.049 0.000 0.000 34 .40 34.40 0. 00 603 619 0.00 20.00 32 6.42 100 1 1. 610 0.000 0.000 34.40 34.40 0. 00 619 620 0.00 3.00 0.00 100 1 1.380 0.000 0.000 34 .40 34 .40 0. 00 620 621 0.00 10.00 32 4 .21 100 1 1.049 0.000 0.000 34.40 34.40 0. 00 620 622 0.00 8.00 32 4 .21 100 1 1.049 0.000 0.000 34.40 34 .40 0.00 A MAX. VELOCITY OF 18.32 ft. /sec. OCCURS BETWEEN REF. PT. 610 AND 611 Sprinkler-CALC Release 7.2 Win By Walsh Engineering Inc. North Kingstown R.I. U.S.A. WATER SUPPLY/DEMAND GRAPH ATTIC DRY PIPE LIGHT HAZARD,TREADWELLS NORTH ANDOVER MA • 15a.as b I i 140.00 l 130.00 _ - 1 120.00 = f l P 110.00 I_.� .. .. - __ R 100.00 1 E 90.00 � _, �+ _ 80.00 y- _ S 70.00 � � U Ga.as R 50.00 " _ } - - ( .. E 40.00 �- g 30.00 20.00 _ I 10.00 � 0.00 0 500 1000 1500 2000 Supply.: 78.00 psi 1605.00 gpmDemand: 52.58 psi ra-1 332.59 gpm FLOW tv rir�IIr-�L ire , : r; MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C C A L C U L A T I O N S C O V E R S H E E T LIGHT HAZ. , BUSINESS, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER, MA W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 � NOFI*44- qcy B O O S T E R P U M P S O MICHAEL J. G JOANIS NUMBER OF BOOSTER PUMPS 0 v FIRE PROTECTION No.39874 S P R I N K L E R S MAXIMUM SPACING OF SPRINKLERS (ft) 14 MAXIMUM SPACING OF SPRINKLER LINES (ft) 14 SPECIFIED DISCHARGE DENSITY (gpm/sq. ft. ) .1 THIS SPRINKLER SYSTEM WILL DELIVER A DENSITY OF .1 gpm/sq. ft. FOR A DESIGN AREA OF 900 SQ. FT. OF FLOOR AREA THIS SYSTEM OPERATES AT A FLOW OF 257.36 gpm AT A PRESSURE OF 61.84 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 } MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER LIGHT HAZ. , BUSINESS, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER, MA PAGE 1 --------------------------------------------------------------------------------------------- SPRINKLER SYSTEM ANALYSIS TO SHOW THE MAXIMUM DENSITY AVAILABLE WITH ZERO PRESSURE REMAINING --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 208 5.60 13.00 31.77 32.18 209 5.60 13.00 33.04 34.80 210 5. 60 13.00 31.28 31.22 210 5. 60 13.00 31.29 31.22 213 5.60 13.00 36.21 41.80 219 5.60 13.00 25.87 21.35 220 5. 60 13.00 25.95 21.47 221 5. 60 13.00 25. 85 21.31 222 5. 60 13.00 27.43 23. 99 223 5.60 13.00 29.55 27.85 225 5.60 13.00 39. 68 50.21 THE SPRINKLER SYSTEM FLOW IS 337. 93 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.132 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 437. 93 gpm AVAILABLE PRESSURE 98.06 psi AT 437. 93 gpm OPERATING PRESSURE 98.06 psi AT 437. 93 gpm PRESSURE REMAINING 0.00 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER LIGHT HAZ. , BUSINESS, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER, MA PAGE 2 ---------------------------------------------------------------------------------------------- HYDRAULIC CALCULATIONS AT SPECIFIED DENSITY --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 208 5. 60 13.00 24 . 17 18. 63 209 5. 60 13.00 25. 18 20.22 210 5. 60 13.00 23. 84 18.13 210 5. 60 13.00 23.84 18.13 213 5. 60 13.00 27. 68 24 .44 219 5. 60 13.00 19.58 12.22 220 5. 60 13.00 19. 62 12.27 221 5. 60 13.00 19. 60 12..25 222 5. 60 13.00 20. 89 13. 92 223 5. 60 13.00 22.57 16.24 225 5. 60 13.00 30.38 29.43 THE SPRINKLER SYSTEM FLOW IS 257.36 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.100 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 357.36 gpm AVAILABLE PRESSURE 98.68 psi AT 357.36 gpm OPERATING PRESSURE 61.84 psi AT 357.36 gpm PRESSURE REMAINING 36.84 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [� BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER LIGVT HAZ. , BUSINESS, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER, MA _PAGE 3 NNNNNNNryNNNNNN FITTING Equivalent Length per NFPA 13 1994, 6-4 .3 '-' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3='T'/Cross, 4=Butterfly Valve, 5=Gate Valve, 6=Swing Check Valve FROM TO TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIC. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) --------------------------------------------------------------------------------------------- 1 2 257.36 200.00 3522 88. 14 140 111 6.400 0.002 0. 000 61.84 61.36 0.48 2 3 257.36 5.00 22 17. 96 120 2 4 .260 0.016 0.000 61.36 61. 00 0.37 3 4 257.36 5.00 0.00 120 2 4 .260 0.016 0.000 61.00 57 . 92 3.08 4 5 .257.36 1.50 0.00 120 2 4 .260 0.016 0.000 57. 92 57. 89 0.02 5 6 257.36 8.00 2462 62.84 120 2 4 .260 0.016 0.000 57.89 0. 43 57.46 6 200 257.36 36.00 22 11.78 120 2 2. 635 0.166 5. 633 0.43 43. 10 -48.30 200 201 257.36 50.00 22 11.78 120 2 2. 635 0.166 0. 000 43.10 32. 85 10.25 201 202 226.98 14.00 0.00 120 2 2. 635 0.132 0.000 32.85 31. 15 1.70 202 203 124.72 6.00 22 11.78 120 2 2. 635 0.043 0.000 31.15 30.33 0.82 203 204 97.04 5.50 0.00 120 2 2. 635 0.027 0.000 30.33 30. 18 0.15 204 205 97.04 13.00 3 6.40 120 1 1. 610 0.300 0.000 30.18 24 . 35 5.83 205 206 49.36 12.00 0.00 120 1 1.380 0.182 0.000 24 .35 22. 13 2.22 206 207 24 .17 12.00 0. 00 120 1 1.049 0.184 0.000 22.13 19. 94 2.19 207 208 24 .17 2.00 222 5. 10 120 1 1.049 0. 184 0.000 19. 94 18. 63 1.31 206 209 25.18 2.00 322 7. 60 120 1 1.049 0.199 0.000 22.13 20.22 1. 91 205 210 47. 68 2.00 322 7. 60 120 1 1.049 0. 649 0. 000 24.35 18. 13 6.23 203 211 27. 68 1.00 3 5.30 120 1 1.380 0.062 0. 000 30.33 29. 91 0.42 211 212 27. 68 7.00 0.00 120 1 1.049 0.237 0. 000 29. 91 28.25 1.66 212 213 27.68 11.00 222 5.10 120 1 1.049 0.237 0.000 28.25 24 . 44 3.82 202 214 102.26 12.00 3 6.40 120 1 1. 610 0.331 0.000 31.15 25. 06 6.09 214 215 102.26 17.00 22 5.20 120 1 1. 610 0.331 0.000 25.06 17.72 7.35 215 216 79.69 12.00 0.00 120 1 1. 610 0.208 0.000 17.72 15.20 2.52 216 217 58.80 9.50 0.00 120 1 1. 610 0.119 0. 000 15.20 14 . 04 1.16 217 218 39.20 0.50 0.00 120 1 1.380 0.119 0.000 14.04 13. 98 0.05 218 219 19.58 9.00 222 5.10 120 1 1.049 0. 125 0.000 13.98 12.22 1.76 218 220 19.62 6.00 322 7. 60 120 1 1. 049 0.125 0.000 13. 98 12.27 1.71 217 221 19. 60 5.00 3222 9.30 120 1 1. 049 0.125 0.000 14 .04 12.25 1.79 216 222 20.89 1.50 322 7. 60 120 1 1. 049 0.141 0. 000 15.20 13. 92 1.28 215 223 22.57 1.50 322 7. 60 120 1 1.049 0.162 0.000 17.72 16.24 1.48 201 224 30.38 15.50 3 6.40 120 1 1. 610 0.035 0.000 32.85 32.08 0.77 224 225 30.38 6.00 22 3.40 120 1 1.049 0.282 0.000 32.08 29. 43 2. 65 A MAX. VELOCITY OF 17. 69 ft./sec. OCCURS BETWEEN REF. PT. 205 AND 210 Sprinkler-CALC Release 7.2 Win By Walsh Engineering Inc. North Kingstown R.I. U.S.A. J • WATER SUPPLWDEMAND GRAPH LIGHT HOZ.,BUSINESS,WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER, MA 1 150.00 140.00 130.00 }, 120.00i . P 110.00 t - ; R l 00.00 ; -- -� � �.. _,_ � � �. E 00.00 - -__ S 80.00 7i- < ._y. 1 S 70.00 U G0.00 _. # i R 50.00i E 40.00 - - - --- W_.. _... 30.00 —- -- 3 20.00 ( 10.00 0.00 a 501 1000 1500 2000 Supply: 78.00 psi 1605.00 gpm Demand: 61.84 psi �-a 357.36 gpm FLOW i rirtillr- L' 7 ' k Y w MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C C A L C U L A T I O N S C O V E R S H E E T ORD. HAZ. II, FUTURE RETAIL, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 B O O S T E R P U M P S NUMBER OF BOOSTER PUMPS 0 S P R I N K L E R S MAXIMUM SPACING OF SPRINKLERS (ft) 10 MAXIMUM SPACING OF SPRINKLER LINES (ft) 13 SPECIFIED DISCHARGE DENSITY (gpm/sq. ft. ) .2 THIS SPRINKLER SYSTEM WILL DELIVER A DENSITY OF .2 gpm/sq. ft. FOR A DESIGN AREA OF 1000 SQ. FT. OF FLOOR AREA THIS SYSTEM OPERATES AT A FLOW OF 301.05 gpm AT A PRESSURE OF 71.31 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ORD•. HAZ. II, FUTURE RETAIL, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER PAGE--------------------------------------------------------------------------------------------- 1 SPRINKLER SYSTEM ANALYSIS TO SHOW THE MAXIMUM DENSITY AVAILABLE WITH ZERO PRESSURE REMAINING --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 103 5. 60 14 .00 38.30 46.77 104 5. 60 14 .00 36.39 42.23 105 5. 60 14 .00 35.09 39.26 106 5. 60 14 .00 33.76 36.34 107 5. 60 14.00 32.41 33.48 108 5. 60 14 .00 31. 12 30.89 109 5. 60 14 .00 37.33 44.44 110 5. 60 14 .00 35.11 39.30 111 5. 60 14.00 39. 93 50. 83 112 5. 60 14 .00 39. 65 50. 13 THE SPRINKLER SYSTEM FLOW IS 359.10 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 250.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.239 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 609.10 gpm AVAILABLE PRESSURE 96.39 psi AT 609. 10 gpm OPERATING PRESSURE 96.39 psi AT 609. 10 gpm PRESSURE REMAINING 0.00 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE ' MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ORD'. HAZ. II, FUTURE RETAIL, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER PAGE 2 --------------------------------------------------------------------------------------------- HYDRAULIC CALCULATIONS AT SPECIFIED DENSITY NNNNNNNNNNryNNNNNryNryNNNOPERATINGNIN.NNNNNry THEFOLLOWINGSPRINKLERSARE [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ) REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 103 5.60 14 .00 32.16 32. 98 104 5. 60 14 .00 30.49 29. 64 105 5. 60 14 .00 29.45 27. 65 106 5. 60 14 .00 28.28 25.49 107 5. 60 14.00 27.06 23.35 108 5.60 14 .00 26.00 21.55 109 5.60 14 .00 31.34 31.32 110 5.60 14 .00 29.40 27.55 111 5.60 14.00 33.55 35.88 112 5.60 14 .00 33.32 35.39 THE SPRINKLER SYSTEM FLOW IS 301.05 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 250.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.200 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 551.05 gpm AVAILABLE PRESSURE 97.01 psi AT 551.05 gpm OPERATING PRESSURE 71.31 psi AT 551.05 gpm PRESSURE REMAINING 25.70 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [� BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ORD% HAZ. II, FUTURE RETAIL, WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER PAGE 3 ------------------------.-----------------------------------------------------I---------------- FITTING Equivalent Length per NFPA 13 1994, 6-4 .3 '-' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3='T'/Cross, 4=Butterfly Valve, S=Gate Valve, 6=Swing Check Valve -------------------------------------- FROM TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIC. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) --------------------------------------------------------------------------------------------- 1 2 301.05 200.00 3522 88. 14 140 111 6. 400 0.002 0.000 71.31 70. 67 0. 64 2 3 301.05 5.00 22 17. 96 120 2 4 .260 0.021 0.000 70. 67 70.18 0. 49 3 4 301.05 5.00 0.00 120 2 4 .260 0.021 0.000 70.18 67. 07 3.11 4 5 301.05 1.50 0.00 120 2 4 .260 0.021 0. 000 67.07 66. 94 0.13 5 6 301.05 8.00 2462 62.84 120 2 4 .260 0.021 0.000 66. 94 65. 43 1.52 6 100 301.05 78.00 2222 23.56 120 2 2. 635 0.222 6. 067 65.43 36. 82 22.54 100 101 234.18 12.10 0.00 120 2 2. 635 0.139 0.000 36.82 35.25 1.57 101 102 62. 65 12. 10 0.00 120 2 2. 635 0.012 0.000 35.25 35. 08 0. 18 102 103 62. 65 3.00 22 4.40 120 1 1.380 0.283 0.000 35.08 32. 98 2.09 103 104 30.49 10.00 2 1.70 120 1 1.049 0.283 0. 000 32. 98 29. 64 3. 34 101 105 110.79 7.00 33 12.80 120 1 1. 610 0.384 0.000 35.25 27. 65 7. 60 105 106 81.34 , 10.00 0.00 120 1 1. 610 0.217 0.000 27. 65 25. 49 2.16 106 107 53.06 10.00 0.00 120 1 1.380 0.208 0.000 25.49 23.35 2.14 107 108 26.00 7.00 2 1.70 120 1 1.049 0.211 0.000 23.35 21.55 1.80 101 109 60.74 4 .00 33 10. 60 120 1 1.380 0.267 0.000 35.25 31. 32 3. 93 109 110 29.40 10.00 3 4 .20 120 1 1.049 0.265 0.000 31.32 27.55 3.77 100 111 33.55 7.00 332 15.40 120 1 1. 610 0.042 0.000 36.82 35.88 0. 94 100 112 33.32 4 .00 332 12.80 120 1 1.380 0.088 0.000 36.82 35.39 1.44 A MAX. VELOCITY OF 17.71 ft. /sec. OCCURS BETWEEN REF. PT. 6 AND 100 Sprinkler-CALC Release 7.2 Win By Walsh Engineering Inc. North Kingstown R.I. U.S.A. j MATER SUPPLY/DEMAND GRAPH ORD. HAS. II, FUTURE RETAIL,WET PIPE, UPPER LEVEL, 1025 OSGOOD ST, N. ANDOVER t 150.00y5[ .. ... . . 3 kk `c 140.00 130.00 I - - T _ _,... __... __... 120.00 , _! ..-.. _ ..._ P 110.00 ,q.6. ... ......y.. i _..... £ _ ._ .. .... ... ._. .. .._._,_.._, C .._.., i tE 1{ R 100.00 _ } .. 4 j S 80.00 1µ S 70.00 60.00 ... , . ... _ ....�. ;...... _ w. . R 50.00 _ .__ E 40.00 30.00 u 20.00 } ' 10.00 - s _ ._ - ___ _. _ _..------- 0.00 0 500 1000 1500 2000 Supply: 78.00 psi 1605.00 gpm FLOWDemand: 71.31 psi @5', 551.05 gpm s fir~ s : t E r c.. s MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C C A L C U L A T I O N S C 0 V E R S H E E T Y PIPE 1025 OSGOOD ST N. ANDOVER MA ATTIC SYSTEM, DR , , W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 B O O S T E R P U M P S NUMBER OF BOOSTER PUMPS 0 S P R I N K L E R S MAXIMUM SPACING OF SPRINKLERS (ft) 20 MAXIMUM SPACING OF SPRINKLER LINES (ft) 19 SPECIFIED DISCHARGE DENSITY (gpm/sq. ft. ) .1 THIS SPRINKLER SYSTEM WILL DELIVER A DENSITY OF .1 gpm/sq. ft. FOR A DESIGN AREA OF 1500 SQ. FT. OF FLOOR AREA THIS SYSTEM OPERATES AT A FLOW OF 283.57 gpm AT A PRESSURE OF 63.55 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ATTIC SYSTEM, DRY PIPE, 1025 OSGOOD ST, N. ANDOVER, MA PAGE 1 ~~N~~NNNryNNry ~ NNN SPRINKLERSYSTEMANALYSISTOSHOWTHEMAXIMUMDENSITYAVAILABLE WITH ZERO PRESSURE REMAINING --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 315 8.00 28.00 52.49 43.04 316 8.00 28.00 50.81 40.33 317 8.00 28.00 50.21 39.38 318 8.00 28.00 52.49 43.04 319 8.00 28.00 50.80 40.33 , 320 8.00 28.00 50.22 39.40 325 8.00 28.00 66. 68 69.47 THE SPRINKLER SYSTEM FLOW IS 373. 69 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.132 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 473. 69 gpm AVAILABLE PRESSURE 97.75 psi AT 473. 69 gpm OPERATING PRESSURE 97.75 psi AT 473. 69 gpm PRESSURE REMAINING 0.00 psi THE/ ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [✓] BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE • MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ATTIC SYSTEM, DRY PIPE, 1025 OSGOOD ST, N. ANDOVER, MA PAGE 2 --------------------------------------------------------------------------------------------- HYDRAULIC CALCULATIONS AT SPECIFIED DENSITY --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 315 8.00 28.00 39.83 24 .78 316 8.00 28.00 38. 49 23.14 317 8.00 28.00 38.00 22.56 318 8.00 28.00 39.82 24.77 319 8.00 28.00 38.49 23.14 320 8.00 28.00 38.00 22.56 325 8.00 28.00 50. 95 40.56 THE SPRINKLER SYSTEM FLOW IS 283.57 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT NO. 1 IS 100.00 -gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.100 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 383.57 gpm AVAILABLE PRESSURE 98.49 psi AT 383.57 gpm OPERATING PRESSURE 63.55 psi AT 383.57 gpm PRESSURE REMAINING 34.94 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [,] BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ATTIC SYSTEM, DRY PIPE, 1025 OSGOOD ST, N. ANDOVER, MA PAGE 3 N~~NN~~~N~~~NN~NNNFITTING Equivalent Length per NFPA 13 1994, 6-4 .3 '-' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3='T' /Cross, 4=Butterfly Valve, 5=Gate Valve, 6=Swing Check Valve ---------------------------- FROM TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIC. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) --------------------------------------------------------------------------------------------- 1 2 283.57 200.00 3522 88. 14 140 111 6.400 0.002 0.000 63.55 62. 98 0.57 2 3 283.57 5.00 22 17. 96 120 2 4.260 0.019 0.000 . 62. 98 62.54 0.44 3 4 283.57 5.00 0.00 120 2 4 .260 0.019 0.000 62.54 59.44 3.10 4 5 283.57 1.50 0.00 120 2 4 .260 0.019 0.000 59.44 59.42 0.03 5 7 283.57 3.00 0.00 120 2 4 .260 0.019 0.000 59.42 59.36 0. 06 7 8 283.57 10.00 2562 35.42 100 2 4 .260 0.027 0.000 59.36 58.16 1.20 8 300 283.57 41.00 222 19.22 100 2 4 .260 0.027 6.500 58. 16 50.04 1. 62 300 301 283.57 20.00 2 6.41 100 2 4 .260 0.027 0.000 50.04 49.33 0.71 301 302 232. 62 35.00 2 4 .20 100 2 2. 635 0.193 0.000 49.33 41.77 7.56 302 303 0.00 29.00 0.00 100 2 2. 635 0.000 0.000 41.77 41.77 0. 00 303 304 0.00 20.00 0.00 100 2 2. 635 0.000 0.000 41.77 41.77 0. 00 304 305 0.00 8.00 22 8.40 100 2 2. 635 0.000 3.033 41.77 38.73 -0. 00 305 306 0.00 3.00 32 6.42 100 1 1. 610 0.000 0.000 38.73 38.73 0.00 305 307 0.00 3.00 32 6.42 100 1 1. 610 0.000 0.000 38.73 38.73 0. 00 303 308 0.00 15.00 32 14 .76 100 2 2. 635 0.000 5. 633 41.77 36.13 -0.00 308 309 0.00 2.00 3 4 .57 100 1 1. 610 0.000 0.000 36.13 36.13 0.00 309 310 0.00 6.00 0.00 100 1 1. 610 0.000 0.000 36.13 36.13 0. 00 310 311 0.00 6.00 2 1.85 100 1 1. 610 0.000 0.000 36. 13 36.13 0.00 308 312 0.00 4.00 3 4 .57 100 1 1. 610 0.000 0.000 36. 13 36.13 0.00 312 313 0.00 6.00 2 1.85 100 1 1. 610 0.000 0.000 36. 13 36.13 0.00 302 314 232. 62 21.00 32 14 .76 100 2 2. 635 0.193 5.633 41.77 29.24 6. 90 314 315 116.31 3.00 3 4.57 100 1 1. 610 0.589 0.000 29.24 24 .78 4. 45 315 316 76.49 6.00 0.00 100 1 1. 610 0.271 0.000 24.78 23.14 1. 64 316 317 38.00 6.00 2 1.85 100 1 1. 610 0.074 0.000 23. 14 22.56 0.58 314 318 116.31 3.00 3 4 .57 100 1 1. 610 0.589 0.000 29.24 24 .77 4 . 46 318 319 76.49 6.00 0.00 100 1 1. 610 0.271 0.000 24 .77 23.14 1. 63 319 320 38.00 6.00 2 1.85 100 1 1. 610 0.074 0.000 23.14 22.56 0.58 301 321 50. 95 1.10 3 15.07 100 2 4 .260 0.001 0.000 49.33 49.31 0.02 321 322 50. 95 21.00 32 14 .76 100 2 2. 635 0.012 5. 633 49.31 43.30 0.38 322 323 50. 95 3.00 3 4 .57 100 1 1. 610 0.128 0.000 43.30 42.33 0. 97 323 324 50. 95 6.00 0.00 100 1 1. 610 0.128 0.000 42.33 41.56 0.77 324 325 50.95 6.00 2 1.85 100 1 1. 610 0.128 0.000 41.56 40.56 1.00 322 326 0.00 3.00 3 4 .57 100 1 1. 610 0.000 0.000 43.30 43.30 0.00 326 327 0.00 6.00 0.00 100 1 1. 610 0.000 0.000 43.30 43.30 0.00 327 328 0.00 6.00 2 1.85 100 1 1. 610 0.000 0.000 43.30 43.30 0.00 A MAX. VELOCITY OF 18.32 ft. /sec. OCCURS BETWEEN REF. PT. 314 AND 315 Sprinkler-CALC Release 7.2 Win By Walsh Engineering Inc. North Kingstown R.I. U.S.A. WA,TER SUPPL'YrCaEMANGmGRAPH�.._ , ATTIC SYSTEM,DRY' PIPE, 1025 OSGOOD ST,N.ANDOVER, MA 5a.as ..__ ,_ .. . F 140.00 i 130.00 _.. . _... .. ___...__ ------- 120.00 we 120.00 P 110.00 — a .. : ,. ..: 3 ... .... f R 100.00 r E 90.00 S 80.00 0.00 a I U 60.00 R 50.00 j E 40.00 } 30.00 ---- ------- 20.00 — � 10.00 0.00 0 500 1000 1500 2000 Supply: 7S.aa psi 1605.00 gpm tV_� Demand: 53.55 psis 35 ._57 gRm v�� FLa y rir ki LC,T Wiry MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C C A L C U L A T I O N S C 0 V E R S H E E T BASEMENT, WET PIPE, ORD. HAZ. GRPl, TREADWELLS, NORTH ANDOVER, MA W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 B O O S T E R P U M P S NUMBER OF BOOSTER PUMPS 0 S P R I N K L E R S MAXIMUM SPACING OF SPRINKLERS (ft) 14 MAXIMUM SPACING OF SPRINKLER LINES (ft) 9 SPECIFIED DISCHARGE DENSITY (gpm/sq. ft. ) .15 THIS SPRINKLER SYSTEM WILL DELIVER A DENSITY OF .15 gpm/sq. ft. FOR A DESIGN AREA OF 900 SQ. FT. OF FLOOR AREA J THIS SYSTEM OPERATES AT A FLOW OF 189.51 gpm AT A PRESSURE OF 31.18 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 a MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER BASEMENT, WET PIPE, ORD. HAZ. GRP1, TREADWELLS, NORTH ANDOVER, MA PAGE 1 --------------------------------------------------------------------------------------------- SPRINKLER SYSTEM ANALYSIS TO SHOW THE MAXIMUM DENSITY AVAILABLE WITH ZERO PRESSURE REMAINING --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 505 5.60 3.00 39.74 50.36 506 5.60 3.00 37.11 43. 90 507 5.60 3. 00 38. 61 47.52 508 5. 60 3.00 36.05 41.43 510 5.60 3.00 41.27 54 .30 511 5. 60 3.00 38.55 47.37 512 5. 60 3.00 42.28 56. 99 513 5. 60 3.00 39.53 49.83 514 5.60 3.00 45.27 65.33 THE SPRINKLER SYSTEM FLOW IS 358.39 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 250.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.286 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT . 1605.00 gpm TOTAL SYSTEM FLOW 608.39 gpm AVAILABLE PRESSURE 96.39 psi AT 608.39 gpm OPERATING PRESSURE 96.39 psi AT 608.39 gpm PRESSURE REMAINING 0.00 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [�J BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER BASEMENT, WET PIPE, ORD. HAZ. GRP1, TREADWELLS, NORTH ANDOVER, MA PAGE 2 ---------------------------------------------------------------------------------------------- HYDRAULIC CALCULATIONS AT SPECIFIED DENSITY --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 505 5. 60 3.00 21.01 14 .07 506 5. 60 3.00 19.50 12.13 507 5. 60 3.00 20.36 13.22 508 5. 60 3.00 18.90 11.39 510 5.60 3.00 21.88 15.26 511 5. 60 3.00 20.32 13.16 512 5. 60 3.00 22.48 16. 11 513 5. 60 3.00 20.87 13.88 514 5. 60 3.00 24 .20 18. 67 THE SPRINKLER SYSTEM FLOW IS 189.51 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 250.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.150 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 439.51 gpm AVAILABLE PRESSURE 98.05 psi AT 439.51 gpm OPERATING PRESSURE 31.18 psi AT 439.51 gpm PRESSURE REMAINING 66.86 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [ V� BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER BASEMENT, WET PIPE, ORD. HAZ. GRP1, TREADWELLS, NORTH ANDOVER, MA PAGE 3 --------------------------------------------------------------------------------------------- FITTING Equivalent Length per NFPA 13 1994, 6-4.3 '-' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3='T'/Cross, 4=Butterfly Valve, 5=Gate Valve, 6=Swing Check Valve FROM TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIC. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) --------------------------------------------------------------------------------------------- 1 2 189.51 200.00 3522 88. 14 140 111 6.400 0.001 0.000 31. 18 30. 91 0.27 2 3 189.51 3.00 22 17. 96 120 2 4 .260 0.009 0.000 30. 91 30.72 0. 19 3 4 189.51 5.00 0.00 120 2 4 .260 0.009 0.000 30.72 27. 68 3. 05 4 5 189.51 2.00 0.00 120 2 4.260 0.009 0.000 27. 68 27. 66 0.02 5 7 189.51 3.00 0.00 120 2 4.260 0.009 0.000 27. 66 27. 67 -0. 02 7 8 189.51 10.00 2562 49. 64 120 2 4.260 0.009 0.000 27.67 27.13 0. 54 8 500 189.51 37. 00 2222 23.56 120 2 2. 635 0.094 1.300 27. 13 20.13 5. 70 500 501 165.31 8.50 0.00 120 2 2. 635 0.073 0.000 20.13 19.48 0. 65 501 502 121.97 12.50 22 11.78 120 2 2. 635 0.042 0.000 19.48 18.45 1. 03 502 503 79.77 8.50 0.00 120 2 2. 635 0.019 0.000 18.45 18.29 0. 16 503 504 40.51 8.50 0.00 120 2 2. 635 0.005 0.000 18.29 18.24 0. 05 504 505 40.51 7.00 2 1.70 120 1 1.049 0.480 0. 000 18.24 14.07 4 . 17 505 506 19.50 14 .00 2 1.70 120 1 1.049 0.124 0.000 14.07 12.13 1. 94 503 507 39.26 7.00 3 4 .20 120 1 1.049 0.453 0.000 18.29 13.22 5. 07 507 508 18. 90 14 .00 2 1.70 120 1 1.049 0.117 0.000 13.22 11.39 1. 83 502 509 42.20 3.00 3 5.30 120 1 1.380 0.136 0.000 18. 45 17.33 1. 12 509 510 42.20 4 .00 0.00 120 1 1.049 0.517 0.000 17.33 15.26 2. 07 510 511 20.32 14 .00 2 1.70 120 1 1.049 0.134 0.000 15.26 13.16 2. 10 501 512 43.34 2.00 3 4 .20 120 1 1.049 0.544 0.000 19.48 16.11 3.37 512 513 20.87 14 .00 2 1.70 120 1 1.049 0.140 0.000 16.11 13.88 2.22 500 514 24 .20 2.00 32 5. 90 120 1 1.049 0.185 0.000 20.13 18. 67 1. 46 A MAX. VELOCITY OF 16.08 ft./sec. OCCURS BETWEEN REF. PT. 501 AND 512 Sprinkler-CALC Release 7.2 Win By Walsh Engineering, Inc. North Kingstown R.I. U.S.A. WATER SUPPLY/DEMAND GRAPH ? 1 BA,SEMENT,WET PIPE. ORD. HA?. GRP1, TREA.DWELLS, NORTH ANDOVER, MA, 150.as _ f 4- 140.00 130.00 I.._. .__ _ ' -.-.. w. 120.00 - --- z P -T— AIL I _ ___ ._ . R 100.00 , E 90.00 _. ... ---------- S 80.00 i S 70.00 U 60.00 _ �. _ _. .. ..._... 50.00 ' E -14 40.00 _ } , { 30.00 � 20.00 i 10.00 0.00 0 500 1000 1500 2000 Supply: 78.00 psi 1605.00 gpm FLOWtv Demand: 31.18 psi @ 435.51 qpm F l _ 5rir�kir= L 1h MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ` 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C C A L C U L A T I O N S C 0 V E R S H E E T FIRST FLOOR, WET PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 B O O S T E R P U M P S NUMBER OF BOOSTER PUMPS 0 S P R I N K L E R S MAXIMUM SPACING OF SPRINKLERS (ft) 16 MAXIMUM SPACING OF SPRINKLER LINES (ft) 16 SPECIFIED DISCHARGE DENSITY (gpm/sq. ft. ) .1 THIS SPRINKLER SYSTEM WILL DELIVER A DENSITY OF .1 gpm/sq. ft. FOR A DESIGN AREA OF 1000 SQ. FT. OF FLOOR AREA THIS SYSTEM OPERATES AT A FLOW OF 362.40 gpm AT A PRESSURE OF 85.04 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER FIRST FLOOR, WET PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE--------------------------------------------------------------------------------------------- 1 SPRINKLER SYSTEM ANALYSIS TO SHOW THE MAXIMUM DENSITY AVAILABLE WITH ZERO PRESSURE REMAINING -------------------------------------------------------------------------------ti------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 407 8.00 14 .00 39. 62 24. 53 408 5. 60 14 .00 30.06 28. 81 411 5. 60 14 .00 30. 98 30. 60 412 8.00 14 .00 41. 64 27.09 413 5. 60 14 .00 31. 91 32. 46 415 5. 60 14 .00 29. 93 28.56 416 5. 60 14 .00 30.78 30.20 419 5. 60 14 .00 27.87 24 .77 420 5. 60 14 .00 29.23 27.24 422 8.00 14 .00 43. 90 30. 12 424 5.60 14 .00 27.77 24.59 425 5. 60 14.00 29.05 26. 92 THE SPRINKLER SYSTEM FLOW IS 392.75 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ J YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.108 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 492.75 gpm AVAILABLE PRESSURE 97.57 psi AT 492.75 gpm OPERATING PRESSURE 97.57 psi AT 492.75 gpm PRESSURE REMAINING 0.00 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [JJ BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER s FIRST FLOOR, WET PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE 2 ---------------------------------------------------------------------------------------------- HYDRAULIC CALCULATIONS AT SPECIFIED DENSITY --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 407 8.00 14.00 36.52 20.83 408 5. 60 14 .00 27.74 24 .54 411 5. 60 14 .00 28.58 26.04 412 8.00 14 .00 38.39 23.03 413 5. 60 14.00 29.45 27. 66 415 5. 60 14.00 27. 67 24.41 416 5. 60 14.00 28 .44 25.78 419 5. 60 14.00 25. 65 20. 98 420 5. 60 14 .00 26. 99 23.22 422 8.00 14.00 40.59 25.73 424 5. 60 14.•00 25. 60 20.90 425 5. 60 14.00 26.79 22.88 THE SPRINKLER SYSTEM FLOW IS 362.40 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE MINIMUM DENSITY PROVIDED BY THIS SYSTEM IS 0.100 gpm/sq. ft. THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 462.40 gpm AVAILABLE PRESSURE 97.85 psi AT 462.40 gpm OPERATING PRESSURE 85.04 psi AT 462.40 gpm PRESSURE REMAINING 12.81 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [ vTl BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER FIRST FLOOR, WET PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE 3 --------------------------------------------------------------------------------------------- FITTING Equivalent Length per NFPA 13 1994, 6-4.3 '-' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3='T'/Cross, 4=Butterfly Valve, S=Gate Valve, 6=Swing Check Valve ---------------------- FROM TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIC. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) -------------------------------------------------------------------------ti------------------- 1 2 362.40 200.00 3522 88.14 140 111 6.400 0.003 0.000 85. 04 84 . 14 0.90 2 3 362.40 3.00 22 17.96 120 2 4 .260 0.030 0.000 84 . 14 83.51 0. 63 3 4 362.40 5.00 0.00 120 2 4 .260 0.030 0.000 83. 51 80.35 3.15 4 5 362.40 2.00 0.00 120 2 4 .260 0.030 0.000 80.35 80.29 0.06 5 7 362.40 3.00 0.00 120 2 4 .260 0.030 0.000 80.29 80.20 0. 09 7 8 362.40 10.00 2562 49. 64 120 2 4 .260 0.030 0.000 80.20 78.45 1.75 8 400 362.40 50.00222222 35.34 120 2 2. 635 0.313 0.000 78. 45 51.75 26.70 400 401 362. 40 14.00 222 17. 67 120 2 2. 635 0.313 6.067 51.75 35.78 9. 91 401 402 321.81 5.00 0.00 120 2 2. 635 0.251 0.000 35.78 34 .51 1.26 402 403 213.07 8.00 0.00 120 2 2. 635 0.117 0.000 34 .51 33.50 1.01 403 404 116.65 3.00 0.00 120 2 2. 635 0.038 0.000 33. 50 33.43 0. 07 404 405 64 .26 6.00 0.00 120 2 2.635 0.013 0.000 33. 43 33.36 0.08 405 406 64.26 3.00 22 4 .22 120 2 1.097 0.907 0.000 33.36 26.81 6.55 406 407 36.52 10.00 222 5.10 120 1 1.049 0.396 0.000 26. 81 20.83 5. 98 406 408 27.74 2.00 322 7. 60 120 1 1.049 0.238 0.000 26. 81 24 .54 2.27 403 409 96.42 3.00 32 9.00 120 1 1. 610 0.297 0.000 33. 50 29. 94 3.56 409 410 66.97 6.00 0.00 120 1 1.380 0.320 0.000 29. 94 28.08 1. 87 410 411 28.58 3.00 222 5.10 120 1 1.049 0.251 0.000 28. 08 26.04 2.04 410 412 38.39 4 .00 322 7. 60 120 1 1.049 0.434 0.000 28. 08 23.03 5.05 409 413 29.45 1.00 322 7. 60 120 1 1.049 0.266 0.000 29. 94 27 . 66 2.29 402 414 56.11 1.00 32 5. 90 120 1 1.049 0.877 0.000 34 .51 28.46 6.05 414 415 27. 67 12.00 222 5.10 120 1 1.049 0.237 0.000 28. 46 24 .41 4.05 414 416 28.44 3.00 322 7. 60 120 1 1.049 0.249 0.000 28. 46 25.78 2. 68 402 417 52. 64 6.00 32 5. 90 120 1 1.049 0.779 0.000 34 . 51 25.16 9.35 417 418 25. 65 14 .00 0.00 120 1 1.049 0.206 0.000 25. 16 22.24 2. 92 418 419 25. 65 1.00 222 5.10 120 1 1.049 0.206 0.000 22. 24 20. 98 1.26 417 420 26. 99 1.00 322 7. 60 120 1 1.049 0.226 0.000 25. 16 23.22 1. 94 401 421 40.59 3.00 32 7.50 120 1 1.380 0.127 0.000 35.78 34 .45 1.33 421 422 40.59 13.00 222 5.10 120 1 1.049 0.481 0.000 34 . 45 25.73 8.71 404 423 52.39 5.00 32 5. 90 120 1 1.049 0.772 0.000 33. 43 25.,02 8. 42 423 424 25. 60 15.00 222 5.10 120 1 1.049 0.205 0.000 25. 02 20. 90 4. 12 423 425 26.79 2.00 322 7. 60 120 1 1.049 0.223 0.000 25. 02 22.88 2. 14 A MAX. VELOCITY OF 21.81 ft. /sec. OCCURS BETWEEN REF. PT. 405 AND 406 Sprinkler-CALC Release 7.2 Win By Walsh Engineering Inc. North Kingstown R.I. U.S.A. MATER SUPPLY/DEMAND GRAPH j FIRST FLOOR,'v,�rET PIPE LIGHT HARD,TREAD+�ELLS, NORTH ANDOVER MA 150.x0 I b . I _ . . ;. _ _ I 140.00 100.00 _. }... 120.00 P 110.00 .... _. 1............._... R 100.00 =-- — E 90.00 r _ — _ m 1 S 80.00 70.00 _.. �._ w ' __._.... U 60.00 .I i € F �.. s . R 5000 . ..» w � E 40.0030.00 20.00 > 10.00 0.00 a 500 1000 1500 2000 Supply: 75.00 psi @) 1605.00 gpm FLOWDemand: 55.04 psi462.40 gpm D' hlkk L inti ti MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER 12 Settlers Ridge Road, Windham, NH 03087 H Y D R A U L I C C A L C U L A T I O N S C O V E R S H E E T ATTIC, DRY PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA W A T E R S U P P L Y STATIC PRESSURE (psi) 100 RESIDUAL PRESSURE (psi) 78 RESIDUAL FLOW (gpm) 1605 _B 0 0 S T E R P U M P S NUMBER OF BOOSTER PUMPS 0 S P R I N K L E R S MINIMUM FLOW PER SPRINKLER (gpm) 38 MINIMUM PRESSURE PER SPRINKLER (psi) 22.56 THIS SYSTEM OPERATES AT A FLOW OF 232.59 gpm AT A PRESSURE OF 52.58 psi AT THE BASE OF THE RISER (REF. PT. 1) PIPES USED FOR THIS SYSTEM 111 DUCTILE IRON (350) 002 SCHEDULE 10 001 SCHEDULE 40 MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ATTIC, DRY PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE 1 --------------------------------------------------------------------------------------------- SYSTEM ANALYSIS TO SHOW MAXIMUM FLOW WITH ZERO PRESSURE REMAINING --------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING IN: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 611 8.00 18.00 58.18 52.88 612 8.00 18.00 56.30 49.53 613 8.00 18.00 55. 62 48.32 614 8.00 18.00 58. 16 52.85 615 8.00 18.00 56.28 49.49 616 8.00 18.00 55. 63 48.35 THE SPRINKLER SYSTEM FLOW IS 340. 17 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 440. 17 gpm AVAILABLE PRESSURE 98.04 psi AT 440. 17 gpm OPERATING PRESSURE 98.04 psi AT 440. 17 gpm PRESSURE REMAINING 0. 00 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [N] BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE r MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER ATTIC, DRY PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE 2 H~~N~~~~~~N~~~NNNNNNNN ~ ~~~~~~~~~NNNN~~~N~N~NN~NN~~~~~~~~N HYDRAULICCALCULATIONSATSPECIFIEDFLOW -------------------------------------------------------------------------------------------- THE FOLLOWING SPRINKLERS ARE OPERATING I.N: [ ] TEST AREA 1 [ ] TEST AREA 2 [ ] TEST AREA 3 [ ] REMOTE AREA Elevation of sprinklers = Elevation above water test. REF. PT. K ELEV. FLOW PRESSURE ft gpm psi 611 8.00 18.00 39.83 24.79 612 8.00 18.00 38.47 23. 12 613 8.00 18.00 38.00 22.56 614 8.00 18.00 39.83 24.78 615 8.00 18.00 38. 47 23. 12 616 8.00 18.00 38.00 22.56 THE SPRINKLER SYSTEM FLOW IS 232.59 gpm THE OUTSIDE HOSE FLOW AT REFERENCE POINT N0. 1 IS 100.00 gpm [ ] THE INSIDE HOSE [ ] RACK SPKLR'S. [ ] YARD HYDT. FLOW IS 0.00 gpm THE FOLLOWING PRESSURES & FLOWS OCCUR ---> AT REF. PT. 1 <--- STATIC PRESSURE 100.00 psi RESIDUAL PRESSURE 78.00 psi AT 1605.00 gpm TOTAL SYSTEM FLOW 332.59 gpm AVAILABLE PRESSURE 98.85 psi AT 332.59 gpm OPERATING PRESSURE 52.58 psi AT 332.59 gpm PRESSURE REMAINING 46.27 psi THE ABOVE RESULTS INCLUDE 3.00 psi FRICTION LOSS AT REF. PT. # 3 FOR A [ ]V BACKFLOW PREVENTER [ ] METER [ ] DETECTOR CHECK VALVE [ ] OTHER DEVICE • MICHAEL J. JOANIS, PE FIRE PROTECTION ENGINEER 4 ATTIC, DRY PIPE, LIGHT HAZARD, TREADWELLS, NORTH ANDOVER, MA PAGE 3 --------------------------------------------------------------------------------------------- FITTING Equivalent Length per NFPA 13 1994, 6-4.3 '-' Indicates Equivalent Length. 'T' Indicates Threaded Fitting 1=45 Elbow, 2=90 Elbow, 3='T' /Cross, 4=Butterfly Valve, S=Gate Valve, 6=Swing Check Valve FROM TO FLOW PIPE FITS EQV. H-W PIPE DIA. FRIC. ELEV. FROM TO DIFF (gpm) (ft) (ft) C TYPE (in) (psi) (psi) (psi) (psi) (psi) j ~~ NryN2232592O0.OO352288.141401116.4000.001 O.000 52 58 52. 18 NNHHrvNNN � MNNNNryMNNNry ~HNNNNNNNryNNN l 0.40 2 3 232.59 3.00 22 17. 96 120 2 4.260 0.013 0.000 52.18 51. 90 0.28 3 4 232.59 5.00 0.00 120 2 4 .260 0.013 0.000 51. 90 48.84 3.07 4 5 232.59 2.00 0.00 120 2 4 .260 0.013 0.000 48. 84 48. 81 0.03 5 6 232.59 8.00 2462 44 . 83 100 2 4 .260 0.019 0.000 48. 81 47. 83 0. 98 6 600 232.59 52.00 22222 32.03 100 2 4 .260 0.019 0.000 47. 83 46.27 1.56 600 601 232.59 14. 00 2 6. 41 100 2 4 .260 0.019 7.800 46.27 38. 10 0.36 601 602 232.59 13..00 2 4 .20 100 2 2.635 0.193 0.000 38.10 34.79 3.32 602 603 232.59 2.00 0.00 100 2 2. 635 0.193 0.000 34.79 34 .40 0.39 603 604 232.59 3.00 0.00 100 2 2.635 0. 193 0.000 34 .40 33. 82 0.58 604 605 0.00 13.00 0.00 100 2 2.635 0.000 0.000 33.82 33. 82 0.00 605 606 0.00 12.00 23 5.35 100 1 1.380 0.000 0.000 33.82 33. 82 0.00 606 607 0.00 10.00 0.00 100 1 1.049 0.000 0.000 33.82 33. 82 0. 00 607 608 0.00 2.00 2 1.21 100 1 1.049 0.000 0.000 33.82 33.82 0.00 605 609 0.00 7.00 23 4 .21 100 1 1.049 0.000 0.000 33.82 33. 82 0.00 604 610 232.59 9.00 32 14 .76 100 2 2.635 0.193 0.000 33.82 29.24 4 .58 610 611 116.30 3.00 3 4 .57 100 1 1.610 0.589 0.000 29.24 24 .79 4 . 45 611 612 76.47 6.00 0.00 100 1 1.610 0.271 0.000 24.79 23. 12 1. 67 612 613 38.00 6.00 2 1.85 100 1 1.610 0.074 0.000 23. 12 22.56 0.56 610 614 116.30 3.00 3 4 .57 100 1 1. 610 0.589 0.000 29.24 24.78 4 .46 614 615 76.47 6.00 0.00 100 1 "1. 610 0.271 0.000 24 .78 23.12 1. 66 615 616 38.00 6.00 2 1.85 100 1 1. 610 0.074 0. 000 23. 12 22.56 0.57 603 617 0.00 12.00 32 4 .21 100 1 1.049 0.000 0.000 34.40 34.40 0.00 617 618 0.00 9.00 2 1.21 100 1 1.049 0.000 0. 000 34. 40 34.40 0.00 603 619 0.00 20.00 32 6.42 100 1 1.610 0.000 0. 000 34.40 34.40 0.00 619 620 0.00 3.00 0.00 100 1 1.380 0.000 0.000 34.40 34.40 0.00 620 621 0.00 10.00 32 4 .21 100 1 1.049 0.000 0.000 34. 40 34 .40 0.00 620 622 0.00 8.00 32 4 .21 100 1 1.049 0.000 0.000 34 .40 34 . 40 0.00 A MAX. VELOCITY OF 18.32 ft. /sec. OCCURS BETWEEN REF. PT. 610 AND 611 Sprinkler-CALC Release 7.2 Win By Walsh Engineering Inc. North Kingstown R.I. U.S.A. �vrATER SUPPLY/DEMAND GRAPH ATTIC DRY PIPE LIGHT HAZARD TREADWELLS, NORTH ANDOVER MA 150.00 140.00 "T --130.00 120.00 �wm _ P 110.00 _ j R 100.00 -- 90.00 £ , S 80.00 S 70.00 SU Go.on R 50.00 £ a !. E 40.00 30.00 A 20.0010.00 . 0.00 0 500 1000 1500 2000 Supply 78.00 psi ._1605.00 gpm Demand: 52.58 psi r, 332.55 gpm FLOW fi z . brir 'kl'er-'SLC 7 ' ire x-vactover Adover, Mass., COC MIC KE WICK A.V x,95 RATED PS BOARD OF HEALTH PERMIT T D Food/Kitchen Septic System BUILDING INSPECTOR 0O O 101,00THIS CERTIFIES THAT......../0.4f....... .............�............................:HIS CERTIFIES THAT........ . Foundation has permission to erect....................................:7buildings on .Oz . .....`..�........ . . .. ..._................... Rough Chimney to be occupied as................ .tshall.-In. ........ / ./' ..+ ...�......................................................... y provided that the person accepting7his-Aparm. it every espec!conform to the terms of the application on file in Final this office, and to the provisions of the Codes and By-Laws relating to the Inspection, Alteration and Construction of Buildings in the Town of North Andover. PLUMBING INSPECTOR VIOLATION of the Zoning or Building Regulations Voids this Permit. Rough Final 31'L� PERMIT EXPIRES IN 6 MO THS ELECTRICAL INSPECTOR UNLESS CONS P ARTS Rough ..................... ........................................... Service G INSPECTOR Final Occupancy Permit Required to Occupy Building GAS INSPECTOR Rough Display in a Conspicuous Place on the Premises — Do Not Remove Final No Lathing or Dry Wall To Be Done FIRE DEPARTMENT Until Inspected and Approved by the Building Inspector. Burner Street No. SEE REVERSE SIDE Smoke Det.