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2210 FARADAY AVE; ; AS160117; Permit
City of Carlsbad Sprinkler Permit Permit No: AS160117 Job Address: 2210 FARADAY AV Permit Type: SPRINK Parcel No: 2121205500 Lot #: 0 Reference No.: Status: ISSUED Applied 5/4/2016 Approved: 5/31/2016 Issued: 5/31/2016 PC #: Inspector: Project Title: GENMARK T.I. OF EXISTING WAREHOUSE WITH ESFR SYSTEM TO BE TURNED INTO LABS. T-GRID CEILINGS WILL BE ADDED THROUGH OUT AND OCCUPANCIES ABOVE T- GRID WILL BE CONSIDERED LIGHT HAZARD. LABS TO BE DESIGNED TO .2GPM/1500 SF PER SEC 1.6 OF gENMARK HAZARDOUS MATERIALS REPORT. PROVIDED BY oCCUPATIONAL sERVICES. NEW MEZZANINE WILL BE SPRINKLED FROM EXISTING ESFR SYSTEM ABOVE AND NEW 3: MAIN WILL BE INTSTALLED BELOW TO SUPPLY NEW SPRINKLERS. EXTENDED COVERAGE SPRINKLERS WITH A MAX SPACING OF (20' X 20') WILL BE USED THROUGH OUT. Applicant: Owner: A & D FIRE SPRINKLERS P R E F RESEARCH CENTER L L C 7130 CONVOY CT SAN DIEGO, CA 4370 LA JOLLA VILLAGE DR #640 SAN DIEGO CA 858-277-3473 Fees ($) Add'l Fees ($) Total ($) Balance ($) 573 0 573 0 AS160117 1 9 Mani "ImAk "k9 k, 2210 FARADAY AVE Technical Report Hazardous Materials Summary Included FIRE SPRINKLERS INC. A&D FIRE SPRINKLERS 7130 CONVOY COURT SAN DIEGO CA 92111 (858) 277-3473 Job Name : GenMark Building Location System Contract Data File : Gen Mark Area 1 .WXF AS 160117 2210 FARADAY AV 120 Water SUPPIY•rVe C 0 A&D FIRE SPRINKLERS Page Gen Mark Date City Water Suppjy: Demand: Cl - Static Pressure : 104 Dl - Elevation : 11.477 C2 - Residual Pressure: 76.95 D2 - System Flow : 580.912 C2 - Residual Flow : 1190.5 D2 - System Pressure : 60.246 Hose ( Demand) D3 - System Demand : 580.912 Safety Margin : 36.582 150 140 130 p120 R11° C1 E 100 90 80 U 70 _ D2 R 60 E 50 40 30 20 10 Ul .i.... ........ ....... ___ 200 400 600 800 1000 1200 1400 1600 1800 FLOW (N A 1.85) Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Fittings Used nmary A&D FIRE SPRINKLERS Page 2 GenMark Date Fitting Legend Abbrev. Name % 1 1% 11/2 2 2% 3 3% 4 5 6 8 10 12 14 16 18 20 24 E NFPA 13 90' Standard Elbow 1 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61 T NFPA 139O' Flow thruTee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 Units Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute Pressure Units Pounds per Square Inch Note: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. Equivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors of 120 except as noted with *• The fittings marked with a * show equivalent lengths values supplied by manufacturers based on specific pipe diameters and CFactors and they require no adjustment. All values for fittings not marked with a * will be adjusted in the calculation for CFactors of other than 120 and diameters other than Sched 40 per NFPA. Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Pressure I Flow Summary - STANDARD A&D FIRE SPRINKLERS Page 3 Gen Mark Date "qWbde Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Req. DP01 9.5 14 32.7 na 80.06 0.1 400 32.7 S7 27.0 35.96 na EQ01 27.0 38.88 na DP03 9.5 14 32.7 na 80.06 0.1 400 32.7 S3 27.0 35.96 na EQ03 27.0 41.97 na DP02 9.5 14 32.7 na 80.06 0.1 400 32.7 S4 27.0 35.96 na EQ02 27.0 43.04 na 1 27.0 K = K @ EQ02 43.04 na 80.06 M14 27.0 46.28 na L14 25.17 47.47 na L13 25.17 47.57 na L12 25.17 47.65 na Lii 25.17 47.72 na L10 25.17 47.79 na L9 25.17 47.86 na L8 25.17 47.92 na L7 25.17 47.97 na L6 25.17 48.02 na L5 25.17 48.06 na L4 25.17 48.09 na L3 25.17 48.11 na L2 25.17 48.12 na Li 25.17 48.13 na Ml 27.0 47.36 na M38 27.0 47.99 na L38 25.17 48.8 na F2 25.17 48.8 na 21.25 50.51 na OR 0.5 60.25 na 2 27.0 K = K @ EQ01 42.93 na 84.13 3 27.0 K = K © EQ01 42.96 na 84.16 4 27.0 K = K © EQ01 43.6 na 84.78 M25 27.0 46.0 na L25 25.17 47.58 na L26 25.17 47.64 na L27 25.17 47.7 na L28 25.17 47.76 na L29 25.17 47.82 na L30 25.17 47.89 na L31 25.17 47.95 na L32 25.17 48.02 na L33 25.17 48.09 na L34 25.17 48.17 na L35 25.17 48.25 na L36 25.17 48.33 na L37 25.17 48.42 na L15 25.17 47.46 na L16 25.17 47.45 na L17 25.17 47.46 na L18 25.17 47.46 na L19 25.17 47.46 na M19 27.0 46.67 na M20 27.0 46.75 na L20 25.17 47.55 na L21 25.17 47.55 na L22 25.17 47.55 na L23 25.17 47.55 na L24 25.17 47.57 na M16 27.0 46.44 na 7 27.0 K = K © EQ03 44.6 na 82.53 ' 27.0 K = K © EQ03 44.58 na 82.51 27.0 K = K @ EQ03 44.82 na 82.74 23 27.0 46.29 na Flow Summary - Standard A&D FIRE SPRINKLERS Page 4 GenMark Date ode Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Rea. M17 27.0 46.67 na M22 27.0 46.75 na M18 27.0 46.67 na M21 27.0 46.75 na M15 27.0 46.68 na M24 27.0 46.77 na M13 27.0 46.78 na M26 27.0 46.84 na M12 27.0 46.86 na M27 27.0 46.9 na Mil 27.0 46.93 na M28 27.0 46.96 na M10 27.0 47.0 na M29 27.0 47.03 na M9 27.0 47.07 na M30 27.0 47.09 na M8 27.0 47.13 na M31 27.0 47.16 na M7 27.0 47.18 na M32 27.0 47.23 na M6 27.0 47.23 na M33 27.0 47.3 na M5 27.0 47.27 na M34 27.0 47.37 na M4 27.0 47.3 na M35 27.0 47.45 na M3 27.0 47.33 na M36 27.0 47.53 na 2 27.0 47.35 na 37 27.0 47.61 na The maximum velocity is 16.26 and it occurs in the pipe between nodes DP01 and S7 0 Final Calculations - Hazen-Williams - 2007 A&D FIRE SPRINKLERS Page 5 Gen Mark Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn *EQUIVALENT K'S DP01 80.06 1.418 3E 10.273 17.500 32.700 K Factor = 14.00 to 120.0 0.0 10.273 -7.579 S7 80.06 0.3902 0.0 27.773 10.837 Vel = 16.26 S7 0.0 1.418 T 6.849 0.630 35.958 to 120.0 0.0 6.849 0.0 EQ01 80.06 0.3902 0.0 7.479 2.918 Vel = 16.26 0.0 80.06 38.876 KFactor= 12.84 DP03 80.06 1.418 3E 10.273 17.500 32.700, K Factor = 14.00 to 120.0 0.0 10.273 -7.579 S3 80.06 0.3902 0.0 27.773 10.837 Vel = 16.26 S3 0.0 1.418 E 3.424 5.130 35.958 to 120.0 T 6.849 10.273 0.0 EQ03 80.06 0.3902 0.0 15.403 6.010 Vel = 16.26 0.0 80.06 41.968 KFactor= 12.36 DP02 80.06 1.418 3E 10.273 17.500 32.700 K Factor = 14.00 o 120.0 0.0 10.273 -7.579 S4 80.06 0.3902 0.0 27.773 10.837 Vel = 16.26 S4 0.0 1.418 E 3.424 7.870 35.958 to 120.0 T 6.849 10.273 0.0 EQ02 80.06 0.3902 0.0 18.143 7.079 Vel = 16.26 0.0 80.06 43.037 K Factor = 12.20 *REMOTE HEAD TO SUPPLY 1 136.45 2.635 T 16.474 46.880 43.037 K Factor @ node EQ02 to 120.0 0.0 16.474 0.0 M14 136.45 0.0512 0.0 63.354 3.243 Vel = 8.03 M14 0.0 3.26 T 20.159 1.830 46.280 to 120.0 0.0 20.159 0.793 L14 136.45 0.0181 0.0 21.989 0.399 VeI= 5.24 L14 46.96 4.26 0.0 11.000 47.472 to 120.0 0.0 0.0 0.0 L13 183.41 0.0085 0.0 11.000 0.093 Vel = 4.13 L13 -11.19 4.26 0.0 11.000 47.565 to 120.0 0.0 0.0 0.0 L12 172.22 0.0076 0.0 11.000 0.084 Vel = 3.88 L12 -8.90 4.26 0.0 11.000 47.649 to 120.0 0.0 0.0 0.0 LII 163.32 0.0068 0.0 11.000 0.075 Vel = 3.68 will -7.30 4.26 0.0 11.000 47.724 to 120.0 0.0 0.0 0.0 LIO 156.02 0.0064 0.0 11.000 0.070 Vel = 3.51 L10 -6.50 4.26 0.0 11.000 47.794 to 120.0 0.0 0.0 0.0 L9 149.52 0.0058 0.0 11.000 0.064 Vel = 3.37 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 6 Gen Mark Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn L9 -6.58 4.26 0.0 11.000 47.858 to 120.0 0.0 0.0 0.0 L8 142.94 0.0054 0.0 11.000 0.059 VeI= 3.22 L8 -7.55 4.26 0.0 11.000 47.917 to 120.0 0.0 0.0 0.0 L7 135.39 0.0049 0.0 11.000 0.054 VeI= 3.05 L7 -9.21 4.26 0.0 11.000 47.971 to 120.0 0.0 0.0 0.0 L6 126.18 0.0043 0.0 11.000 0.047 Vel = 2.84 L6 -11.44 4.26 0.0 11.000 48.018 to 120.0 0.0 0.0 0.0 L5 114.74 0.0035 0.0 11.000 0.039 Vel = 2.58 L5 -14.11 4.26 0.0 11.000 48.057 to 120.0 0.0 0.0 0.0 L4 100.63 0.0028 0.0 11.000 0.031 Vel = 2.27 L4 -17.19 4.26 0.0 11.000 48.088 to 120.0 0.0 0.0 0.0 3 83.44 0.0020 0.0 11.000 0.022 Vel = 1.88 L3 -20.57 4.26 0.0 11.000 48.110 to 120.0 0.0 0.0 0.0 L2 62.87 0.0012 0.0 11.000 0.013 Vel = 1.42 L2 -24.22 4.26 0.0 11.000 48.123 to 120.0 0.0 0.0 0.0 Li 38.65 0.0005 0.0 11.000 0.005 Vel = 0.87 Li 0.0 3.26 F 9.408 1.830 48.128 to 120.0 0.0 9.408 -0.793 Ml 38.65 0.0018 0.0 11.238 0.020 VeI= 1.49 Ml 0.0 2.635 2T 32.948 94.750 47.355 to 120.0 0.0 32.948 0.0 M38 38.65 0.0050 0.0 127.698 0.634 Vel = 2.27 M38 0.0 3.26 E 9.408 1.830 47.989 to 120.0 0.0 9.408 0.793 L38 38.65 0.0017 0.0 11.238 0.019 VeI= 1.49 L38 0.0 6.357 T 37.72 6.390 48.801 to 120.0 0.0 37.720 0.0 MF2 38.65 0.0001 0.0 44.110 0.003 Vel = 0.39 MF2 542.26 8.249 0.0 3.920 48.804 to 120.0 0.0 0.0 1.698 MF1 580.91 0.0028 0.0 3.920 0.011 Vel = 3.49 MEl 0.0 8.249 SE 105.706 153.210 50.513 to 120.0 0.0 105.706 8.987 ' OR 580.91 0.0029 0.0 258.916 0.746 Vel = 3.49 0.0 580.91 60.246 KFactor= 74.84 *NEW PATH Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 7 GenMark Date WHyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 1 -56.39 2.635 0.0 10.500 43.037 to 120.0 0.0 0.0 0.0 2 -56.39 -0.0100 0.0 10.500 -0.105 Vel = 3.32 2 84.13 2.635 0.0 12.000 42.932 K Factor @ node EQ01 to 120.0 0.0 0.0 0.0 3 27.74 0.0027 0.0 12.000 0.032 Vel = 1.63 3 84.16 2.635 0.0 18.000 42.964 K Factor @ node EQ01 to 120.0 0.0 0.0 0.0 4 111.9 0.0355 0.0 18.000 0.639 Vel = 6.58 4 84.79 2.635 T 16.474 7.370 43.603 K Factor @ node EQOI to 120.0 0.0 16.474 0.0 M25 196.69 0.1007 0.0 23.844 2.400 Vel = 11.57 M25 0.0 3.26 T 20.159 1.830 46.003 to 120.0 0.0 20.159 0.793 L25 196.69 0.0357 0.0 21.989 0.785 Vel = 7.56 L25 200.81 6.357 0.0 11.000 47.581 to 120.0 0.0 0.0 0.0 L26 397.5 0.0051 0.0 11.000 0.056 Vel = 4.02 0L26 11.19 6.357 0.0 11.000 47.637 to 120.0 0.0 0.0 0.0 L27 408.69 0.0054 0.0 11.000 0.059 VeI= 4.13 L27 8.91 6.357 0.0 11.000 47.696 to 120.0 0.0 0.0 0.0 L28 417.6 0.0055 0.0 11.000 0.061 VeI= 4.22 L28 7.30 6.357 0.0 11.000 47.757 to 120.0 0.0 0.0 0.0 L29 424.9 0.0057 0.0 11.000 0.063 Vel = 4.30 L29 6.49 6.357 0.0 11.000 47.820 to 120.0 0.0 0.0 0.0 L30 431.39 0.0059 0.0 11.000 0.065 Vel = 4.36 L30 6.59 6.357 0.0 11.000 47.885 to 120.0 0.0 0.0 0.0 L31 437.98 0.0061 0.0 11.000 0.067 Vel = 4.43 L31 7.54 6.357 0.0 11.000 47.952 to 120.0 0.0 0.0 0.0 L32 445.52 0.0063 0.0 11.000 0.069 Vel = 4.50 L32 9.21 6.357 0.0 11.000 48.021 to 120.0 0.0 0.0 0.0 L33 454.73 0.0065 0.0 11.000 0.072 Vel = 4.60 L33 11.44 6.357 0.0 11.000 48.093 to 120.0 0.0 0.0 0.0 AlkL34 466.17 0.0068 0.0 11.000 0.075 Vel = 4.71 L34 14.11 6.357 0.0 11.000 48.168 to 120.0 0.0 0.0 0.0 L35 480.28 0.0072 0.0 11.000 0.079 Vel = 4.85 fl _..........4-.. '.._-....._ L -. 1 1-_i- I - - fl- £4.I.II*I•II fill II'" Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 8 GenMark Date Hyd. Qa Dia. Fitting Pipe. Pt Pt Ref. nc'1 or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn L35 17.19 6.357 0.0 11.000 48.247 to 120.0 0.0 0.0 0.0 L36 497.47 0.0076 0.0 11.000 0.084 Vel = 5.03 L36 20.57 6.357 0.0 11.000 48.331 to 120.0 0.0 0.0 0.0 L37 518.04 0.0083 0.0 11.000 0.091 Vel= 5.24 L37 24.22 6.357 T 37.72 4.610 48.422 to 120.0 0.0 37.720 0.0 MF2 542.26 0.0090 0.0 42.330 0.382 Vel = 5.48 0.0 542.26 48.804 K Factor= 77.62 *NEW PATH L14 -46.97 4.26 0.0 11.000 47.472 to 120.0 0.0 0.0 0.0 L15 -46.97 -0.0007 0.0 11.000 -0.008 Vel = 1.06 L15 -13.49 4.26 0.0 11.000 47.464 to 120.0 0.0 0.0 0.0 Aft 16 -60.46 -0.0011 0.0 11.000 -0.012 Vel = 1.36 L16 98.76 4.26 0.0 11.000 47.452 to 120.0 0.0 0.0 0.0 L17 38.3 0.0005 0.0 11.000 0.005 Vel= 0.86 L17 -12.92 4.26 0.0 11.000 47.457 to 120.0 0.0 0.0 0.0 L18 25.38 0.0003 0.0 11.000 0.003 Vel= 0.57 L18 -12.72 4.26 0.0 11.000 47.460 to 120.0 0.0 0.0 0.0 L19 12.66 0.0 0.0 11.000 0.0 Vel= 0.28 L19 0.0 3.26 T 20.159 1.830 47.460 to 120.0 0.0 20.159 -0.793 M19 12.66 0.0002 0.0 21.989 0.005 Vel = 0.49 M19 0.0 2.635 2T 32.948 94.750 46.672 to 120.0 0.0 32.948 0.0 M20 12.66 0.0006 0.0 127.698 0.081 Vel = 0.74 M20 0.0 3.26 T 20.159 1.830 46.753 to 120.0 0.0 20.159 0.793 L20 12.66 0.0002 0.0 21.989 0.004 Vel= 0.49 L20 0.0 6.357 0.0 11.000 47.550 to 120.0 0.0 0.0 0.0 L21 12.66 0.0 0.0 11.000 0.0 VeI= 0.13 L21 12.72 6.357 0.0 11.000 47.550 to 120.0 0.0 0.0 0.0 L22 25.38 0.0001 0.0 11.000 0.001 Vel = 0.26 L22 12.92 6.357 0.0 11.000 47.551 to 120.0 0.0 0.0 0.0 L23 38.3 0.0001 0.0 11.000 0.001 Vel = 0.39 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 9 enMark Date WHyd Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn L23 149.02 6.357 0.0 11.000 47.552 to 120.0 0.0 0.0 0.0 L24 187.32 0.0012 0.0 11.000 0.013 VeI= 1.89 L24 13.49 6.357 0.0 11.000 47.565 to 120.0 0.0 0.0 0.0 L25 200.81 0.0015 0.0 11.000 0.016 Vel= 2.03 0.0 200.81 47.581 KFactor= 29.11 *NEW PATH L16 -98.76 3.26 T 20.159 1.830 47.452 to 120.0 0.0 20.159 -0.793 M16 -98.76 -0.0100 0.0 21.989 -0.219 Vel = 3.80 M16 0.0 2.635 T 16.474 48.880 46.440 to 120.0 0.0 16.474 0.0 7 -98.76 -0.0282 0.0 65.354 -1.840 Vel = 5.81 7 82.53 2.635 0.0 20.000 44.600 K Factor @ node EQ03 to 120.0 0.0 0.0 0.0 -16.23 -0.0010 0.0 20.000 -0.020 Vel = 0.95 6 82.51 2.635 0.0 18.000 44.580 K Factor @ node EQ03 to 120.0 0.0 0.0 0.0 5 66.28 0.0134 0.0 18.000 0.242 Vel = 3.90 5 82.73 2.635 T 16.474 7.870 44.822 K Factor @ node EQ03 to 120.0 0.0 16.474 0.0 M23 149.01 0.0603 0.0 24.344 1.467 VeI= 8.77 M23 0.0 3.26 T 20.159 1.830 46.289 to 120.0 0.0 20.159 0.793 L23 149.01 0.0214 0.0 21.989 0.470 Vel = 5.73 0.0 149.01 47.552 KFactor= 21.61 *NEW PATH L17 12.93 3.26 T 20.159 1.830 47.457 to 120.0 0.0 20.159 -0.793 M17 12.93 0.0003 0.0 21.989 0.006 Vel = 0.50 M17 0.0 2.635 2T 32.948 94.750 46.670 to 120.0 0.0 32.948 0.0 M22 12.93 0.0006 0.0 127.698 0.083 Vel = 0.76 M22 0.0 3.26 T 20.159 1.830 46.753 to 120.0 0.0 20.159 0.793 L22 12.93 0.0002 0.0 21.989 0.005 Vel = 0.50 0.0 47.551 KFactor= 1.88 • 12.93 *NEW PATH L18 12.72 3.26 T 20.159 1.830 47.460 to 120.0 0.0 20.159 -0.793 M18 12.72 0.0002 0.0 21.989 0.005 Vel= 0.49 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 10 GenMark Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn M18 0.0 2.635 2T 32.948 94.750 46.672 to 120.0 0.0 32.948 0.0 M21 12.72 0.0006 0.0 127.698 0.081 Vel = 0.75 M21 0.0 3.26 T 20.159 1.830 46.753 to 120.0 0.0 20.159 0.793 L21 12.72 0.0002 0.0 21.989 0.004 Vel = 0.49 0.0 12.72 47.550 KFactor= 1.84 *NEW PATH L15 13.49 3.26 T 20.159 1.830 47.464 to 120.0 0.0 20.159 -0.793 M15 13.49 0.0003 0.0 21.989 0.006 Vel = 0.52 M15 0.0 2.635 2T 32.948 94.760 46.677 to 120.0 0.0 32.948 0.0 M24 13.49 0.0007 0.0 127.708 0.090 Vel = 0.79 M24 0.0 3.26 T 20.159 1.830 46.767 to 120.0 0.0 20.159 0.793 L24 13.49 0.0002 0.0 21.989 0.005 Vel = 0.52 0.0 13.49 47.565 KFactor= 1.96 *NEW PATH L13 11.19 3.26 T 20.159 1.830 47.565 to 120.0 0.0 20.159 -0.793 M13 11.19 0.0002 0.0 21.989 0.005 VeI= 0.43 M13 0.0 2.635 2T 32.948 94.750 46.777 to 120.0 0.0 32.948 0.0 M26 11.19 0.0005 0.0 127.698 0.064 Vel = 0.66 M26 0.0 3.26 T 20.159 1.830 46.841 to 120.0 0.0 20.159 0.793 L26 11.19 0.0001 0.0 21.989 0.003 Vel = 0.43 0.0 11.19 47.637 KFactor= 1.62 *NEW PATH L12 8.91 3.26 T 20.159 1.830 47.649 to 120.0 0.0 20.159 -0.793 M12 8.91 0.0001 0.0 21.989 0.003 Vel = 0.34 M12 0.0 2.635 2T 32.948 94.750 46.859 to 120.0 0.0 32.948 0.0 M27 8.91 0.0003 0.0 127.698 0.042 Vel = 0.52 M27 0.0 3.26 T 20.159 1.830 46.901 120.0 0.0 20.159 0.793 WL27 8.91 0.0001 0.0 21.989 0.002 Vel = 0.34 0.0 8.91 47.696 K Factor = 1.29 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page ii Gen Mark Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn *NEW PATH Lii 7.30 3.26 T 20.159 1.830 47.724 to 120.0 0.0 20.159 -0.793 Mil 7.3 0.0001 0.0 21.989 0.003 VeI= 0.28 Mil 0.0 2.635 2T 32.948 94.750 46.934 to 120.0 0.0 32.948 0.0 M28 7.3 0.0002 0.0 127.698 0.029 Vel = 0.43 M28 0.0 3.26 T 20.159 1.830 46.963 to 120.0 0.0 20.159 0.793 L28 7.3 0.0 0.0 21.989 0.001 VeI= 0.28 0.0 7.30 47.757 K Factor= 1.06 *NEW PATH LiO 6.49 3.26 T 20.159 1.830 47.794 to 120.0 0.0 20.159 -0.793 MIO 6.49 0.0001 0.0 21.989 0.002 Vel = 0.25 M10 0.0 2.635 2T 32.948 94.750 47.003 OPM29 120.0 0.0 32.948 0.0 6.49 0.0002 0.0 127.698 0.023 Vel = 0.38 M29 0.0 3.26 T 20.159 1.830 47.026 to 120.0 0.0 20.159 0.793 L29 6.49 0.0 0.0 21.989 0.001 Vel = 0.25 0.0 6.49 47.820 K Factor= 0.94 *NEW PATH L9 6.59 3.26 T 20.159 1.830 47.858 to 120.0 0.0 20.159 -0.793 M9 6.59 0.0001 0.0 21.989 0.002 Vel = 0.25 M9 0.0 2.635 2T 32.948 94.750 47.067 to 120.0 0.0 32.948 0.0 M30 6.59 0.0002 0.0 127.698 0.024 Vel = 0.39 M30 0.0 3.26 T 20.159 1.830 47.091 to 120.0 0.0 20.159 0.793 L30 6.59 0.0 0.0 21.989 0.001 Vel = 0.25 0.0 6.59 47.885 K Factor= 0.95 *NEW PATH L8 7.54 3.26 T 20.159 1.830 47.917 to 120.0 0.0 20.159 -0.793 M8 7.54 0.0001 0.0 21.989 0.003 VeI= 0.29 M8 0.0 2.635 2T 32.948 94.750 47.127 0 o 120.0 0.0 32.948 0.0 M31 7.54 0.0002 0.0 127.698 0.031 Vel = 0.44 M31 0.0 3.26 T 20.159 1.830 47.158 to 120.0 0.0 20.159 0.793 L31 7.54 0.0 0.0 21.989 0.001 Vel = 0.29 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 12 GenMark Date yd. Qa Dia. Fitting Pipe Pt Pt Ref. or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 0.0 7.54 47.952 K Factor = 1.09 *NEW PATH L7 9.21 3.26 T 20.159 1.830 47.971 to 120.0 0.0 20.159 -0.793 M7 9.21 0.0001 0.0 21.989 0.003 Vel = 0.35 M7 0.0 2.635 2T 32.948 94.750 47.181 to 120.0 0.0 32.948 0.0 M32 9.21 0.0004 0.0 127.698 0.045 Vel = 0.54 M32 0.0 3.26 T 20.159 1.830 47.226 to 120.0 0.0 20.159 0.793 L32 9.21 0.0001 0.0 21.989 0.002 Vel= 0.35 0.0 9.21 48.021 KFactor= 1.33 *NEW PATH L6 11.44 3.26 T 20.159 1.830 48.018 Alllllllll to 120.0 0.0 20.159 -0.793 M6 11.44 0.0002 0.0 21.989 0.004 Vel = 0.44 M6 0.0 2.635 2T 32.948 94.750 47.229 to 120.0 0.0 32.948 0.0 M33 11.44 0.0005 0.0 127.698 0.067 VeI= 0.67 M33 0.0 3.26 T 20.159 1.830 47.296 to 120.0 0.0 20.159 0.793 L33 11.44 0.0002 0.0 21.989 0.004 Vel = 0.44 0.0 11.44 48.093 K Factor = 1.65 *NEW PATH L5 14.12 3.26 T 20.159 1.830 48.057 to 120.0 0.0 20.159 -0.793 M5 14.12 0.0003 0.0 21.989 0.007 Vel = 0.54 M5 0.0 2.635 2T 32.948 94.750 47.271 to 120.0 0.0 32.948 0.0 M34 14.12 0.0008 0.0 127.698 0.098 Vel = 0.83 M34 0.0 3.26 T 20.159 1.830 47.369 to 120.0 0.0 20.159 0.793 L34 14.12 0.0003 0.0 21.989 0.006 VeI= 0.54 0.0 14.12 48.168 KFactor= 2.03 *NEW PATH L4 17.18 3.26 T 20.159 1.830 48.088 OPM4 120.0 0.0 20.159 -0.793 17.18 0.0004 0.0 21.989 0.009 VeI= 0.66 M4 0.0 2.635 2T 32.948 94.750 47.304 to 120.0 0.0 32.948 0.0 M35 17.18 0.0011 ._ 0.0 L-. I J.....s_ 127.698 I.. 0.142 AAA IA•_ 11 - ......#..A Vel = 1.01 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 13 Gen Mark Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "CI' or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn M35 0.0 3.26 T 20.159 1.830 47.446 to 120.0 0.0 20.159 0.793 L35 17.18 0.0004 0.0 21.989 0.008 Vel = 0.66 0.0 17.18 48.247 K Factor = 2.47 *NEW PATH L3 20.57 3.26 T 20.159 1.830 48.110 to 120.0 0.0 20.159 -0.793 M3 20.57 0.0005 0.0 21.989 0.012 Vel = 0.79 M3 0.0 2.635 2T 32.948 94.750 47.329 to 120.0 0.0 32.948 0.0 M36 20.57 0.0016 0.0 127.698 0.198 VeI= 1.21 M36 0.0 3.26 T 20.159 1.830 47.527 to 120.0 0.0 20.159 0.793 L36 20.57 0.0005 0.0 21.989 0.011 Vel = 0.79 0.0 20.57 48.331 K Factor= 2.96 *NEW PATH L2 24.23 3.26 T 20.159 1.830 48.123 to 120.0 0.0 20.159 -0.793 M2 24.23 0.0008 0.0 21.989 0.017 Vel = 0.93 M2 0.0 2.635 2T 32.948 94.750 47.347 to 120.0 0.0 32.948 0.0 M37 24.23 0.0021 0.0 127.698 0.267 VeI= 1.43 M37 0.0 3.26 T 20.159 1.830 47.614 to 120.0 0.0 20.159 0.793 L37 24.23 0.0007 0.0 21.989 0.015 Vel = 0.93 0.0 24.23 48.422 K Factor= 3.48 0 FIRE SPRINKLERS INC. A&D FIRE SPRINKLERS 7130 CONVOY COURT SAN DIEGO CA 92111 (858) 277-3473 Job Name GenMark Building Location System Contract Data File : GenMark Area 2.WXF fl S Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Water Supply ve C 0 A&D FIRE SPRINKLERS Page GenMark Date City Water Supply: Demand: Cl -Static Pressure : 104 Dl - Elevation : 4.114 C2 - Residual Pressure: 76.95 D2 - System Flow : 541.343 C2 - Residual Flow : 1190.5 D2 - System Pressure : 83.354 Hose ( Demand) D3 - System Demand : 541.343 Safety Margin : 14.351 150 140 130 p120 R11° c'r E 100 S90 - D2 s 80 U7° '____ R60 E 50 40 30 TTIT.. 20 10 . ... ................ .. 200 400 600 800 1000 1200 1400 1600 1800 FLOW (N - 1.85) Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Fittings Used marY 0 9 A&D FIRE SPRINKLERS Page 2 GenMark Date Fitting Legend Abbrev. Name 1/2 % 1 11/4 1Y2 2 21,4 3 31,4 4 5 6 8 10 12 14 16 18 20 24 E NFPA 139O'StandardElbow 1 2 2 3 4 5 6 7 8 10 12 14 18 22 27 35 40 45 50 61 T NFPA 13 90 Flow thru Tee 3 4 5 6 8 10 12 15 17 20 25 30 35 50 60 71 81 91 101 121 Units Summary Diameter Units Inches Length Units Feet Flow Units US Gallons per Minute Pressure Units Pounds per Square Inch Note: Fitting Legend provides equivalent pipe lengths for fittings types of various diameters. Equivalent lengths shown are standard for actual diameters of Sched 40 pipe and CFactors of 120 except as noted with *• The fittings marked with a * show equivalent lengths values supplied by manufacturers based on specific pipe diameters and CFactors and they require no adjustment. All values for fittings not marked with a * will be adjusted in the calculation for CFactors of other than 120 and diameters other than Sched 40 per NFPA. Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Pressure / Flow Summary - STANDARD A&D FIRE SPRINKLERS Page 3 enMark Date -Node Elevation K-Fact Pt Pn Flow Density Area Press No. Actual Actual Req. 20 10.0 5.6 25.59 na 28.33 0.2 130 7.0 20.1 10.0 27.44 na 15.1 10.0 27.45 na 21.1 10.0 28.17 na 16.1 10.0 28.25 na 19 10.0 34.08 na 11 10.0 34.28 na 11.1 0.0 38.88 na 12 10.0 35.16 na 13 10.0 36.77 na 14 25.17 70.51 na L21 25.17 70.59 na L22 25.17 70.68 na L23 25.17 70.75 na L24 25.17 70.82 na L25 25.17 70.89 na L26 25.17 70.95 na L27 25.17 .71.02 na L28 25.17 71.08 na L29 25.17 71.14 na L30 25.17 71.19 na L31 25.17 71.25 na L32 25.17 71.32 na L33 25.17 71.38 na L34 25.17 71.45 na L35 25.17 71.52 na L36 25.17 71.59 na L37 25.17 71.67 na 25.17 72.0 na *F2 1 21.25 73.71 na R 0.5 83.35 na 8 10.0 5.6 21.56 na 26.0 0.2 130 7.0 9 10.0 5.6 23.37 na 27.07 0.2 130 7.0 10 10.0 14 21.88 na 65.48 0.1 400 8.2 15 10.0 5.6 23.44 na 27.11 0.2 130 7.0 21 10.0 5.6 24.76 na 27.87 0.2 130 7.0 16 10.0 5.6 24.13 na 27.51 0.2 130 7.0 27A 10.0 14 9.36 na 42.83 0.1 400 8.2 27 0.0 14 24.59 na 69.42 0.1 400 8.2 24 10.0 14 25.27 na 70.37 0.1 400 8.2 25 10.0 14 21.01 na 64.17 0.1 400 8.2 26 10.0 33.91 na 18 10.0 33.97 na 17 10.0 14 21.67 na 65.18 0.1 400 8.2 L20 25.17 70.51 na M20 27.0 69.74 na M19 27.0 70.06 na L19 25.17 70.87 na L18 25.17 70.88 na L17 25.17 70.88 na L16 25.17 70.9 na L15 25.17 70.93 na L14 25.17 70.96 na L13 25.17 71.0 na L12 25.17 71.04 na Lii 25.17 71.09 na L10 25.17 71.14 na L9 25.17 71.19 na L8 25.17 71.24 na L7 25.17 71.28 na L6 25.17 71.32 na L5 25.17 71.35 na 4 25.17 71.38 na 25.17 71.4 na 2 25.17 71.41 na Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Flow Summary - Standard A&D FIRE SPRINKLERS enMark ode No. Elevation K-Fact Pt Actual Pn Li 25.17 71.42 na Ml 27.0 70.64 na M38 27.0 71.19 na L38 25.17 72.0 na M21 27.0 69.82 na M18 27.0 70.07 na M22 27.0 69.89 na M17 27.0 70.08 na M23 27.0 69.97 na 5 27.0 69.99 na 6 27.0 70.01 na 7 27.0 70.03 na M16 27.0 70.1 na M24 27.0 70.04 na M15 27.0 70.13 na M25 27.0 70.1 na 4 27.0 70.11 na 3 27.0 70.12 na 2 27.0 70.13 na 1 27.0 70.13 na M14 27.0 70.16 na M26 27.0 70.16 na M13 27.0 70.2 na M27 27.0 70.22 na M12 27.0 70.24 na M28 27.0 70.28 na Mil 27.0 70.29 na M10 27.0 70.34 na 9 27.0 70.34 na 030 27.0 70.39 na 27.0 70.4 na M8 27.0 70.44 na M31 27.0 70.46 na M7 27.0 70.49 na M32 27.0 70.52 na M6 27.0 70.53 na M33 27.0 70.58 na M5 27.0 70.57 na M34 27.0 70.65 na M4 27.0 70.6 na M35 27.0 70.72 na M3 27.0 70.62 na M36 27.0 70.79 na M2 27.0 70.63 na M37 27.0 70.86 na Page 4 Date Flow Density Area Press kctual Req. The maximum velocity is 24.51 and it occurs in the pipe between nodes 24 and 13 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams - 2007 A&D FIRE SPRINKLERS Page 5 oe Mark Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn *REMOTE HEAD TO SUPPLY 20 28.33 1.083 T 5.84 2.917 25.586 K Factor =5.60 to 120.0 0.0 5.840 0.0 20.1 28.33 0.2121 0.0 8.757 1.857 Vel= 9.87 20.1 0.0 1.728 0.0 0.500 27.443 to 120.0 0.0 0.0 0.0 15.1 28.33 0.0220 0.0 0.500 0.011 Vel = 3.88 15.1 27.11 1.728 0.0 9.500 27.454 to 120.0 0.0 0.0 0.0 21.1 55.44 0.0755 0.0 9.500 0.717 Vel = 7.58 21.1 27.87 1.728 0.0 0.500 28.171 to 120.0 0.0 0.0 0.0 16.1 83.31 0.1600 0.0 0.500 0.080 VeI= 11.40 16.1 27.51 1.728 T 11.29 10.167 28.251 to 120.0 0.0 11.290 0.0 19 110.82 0.2718 0.0 21.457 5.833 Vel = 15.16 19 129.34 3.334 0.0 4.230 34.084 011 120.0 0.0 0.0 0.0 240.16 0.0463 0.0 4.230 0.196 Vet = 8.83 11 65.48 3.334 0.0 3.750 34.280 to 120.0 0.0 0.0 4.331 11.1 305.64 0.0723 0.0 3.750 0.271 Vel= 11.23 11.1 53.07 3.334 0.0 6.250 38.882 to 120.0 0.0 0.0 -4.331 12 358.71 0.0974 0.0 6.250 0.609 Vet = 13.18 12 112.26 3.334 0.0 10.000 35.160 to 120.0 0.0 0.0 0.0 13 470.97 0.1610 0.0 10.000 1.610 Vel= 17.31 13 70.37 3.334 4E 41.977 106.570 36.770 to 120.0 2T 44.976 86.953 -6.570 14 541.34 0.2083 0.0 193.523 40.315 Vel= 19.89 14 -26.67 6.357 0.0 9.590 70.515 to 120.0 0.0 0.0 0.0 L21 514.67 0.0081 0.0 9.590 0.078 Vel = 5.20 L21 -25.06 6.357 0.0 11.000 70.593 to 120.0 0.0 0.0 0.0 L22 489.61 0.0075 0.0 11.000 0.082 Vet = 4.95 L22 -19.95 6.357 0.0 11.000 70.675 to 120.0 0.0 0.0 0.0 L23 469.66 0.0069 0.0 11.000 0.076 Vet = 4.75 L23 -16.65 6.357 0.0 11.000 70.751 0 120.0 0.0 0.0 0.0 L24 453.01 0.0065 0.0 11.000 0.071 VeI= 4.58 L24 -13.59 6.357 0.0 11.000 70.822 to 120.0 0.0 0.0 0.0 L25 439.42 0.0062 0.0 11.000 0.068 Vel = 4.44 Computer Programs by Hvdratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 6 enMark Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn L25 -10.80 6.357 0.0 11.000 70.890 to 120.0 0.0 0.0 0.0 L26 428.62 0.0058 0.0 11.000 0.064 Vet = 4.33 L26 -8.28 6.357 0.0 11.000 70.954 to 120.0 0.0 0.0 0.0 L27 420.34 0.0056 0.0 11.000 0.062 Vet = 4.25 L27 -6.00 6.357 0.0 11.000 71.016 to 120.0 0.0 0.0 0.0 L28 414.34 0.0055 0.0 11.000 0.060 Vel= 4.19 L28 -3.83 6.357 0.0 11.000 71.076 to 120.0 0.0 0.0 0.0 L29 410.51 0.0054 0.0 11.000 0.059 Vel= 4.15 L29 -0.98 6.357 0.0 11.000 71.135 to 120.0 0.0 0.0 0.0 L30 409.53 0.0054 0.0 11.000 0.059 Vel= 4.14 L30 3.25 6.357 0.0 11.000 71.194 to 120.0 0.0 0.0 0.0 L31 412.78 0.0055 0.0 11.000 0.060 Vel= 4.17 Mw L31 5.39 6.357 0.0 11.000 71.254 to 120.0 0.0 0.0 0.0 L32 418.17 0.0056 0.0 11.000 0.062 Vet = 4.23 L32 7.59 6.357 0.0 11.000 71.316 to 120.0 0.0 0.0 0.0 L33 425.76 0.0057 0.0 11.000 0.063 Vet = 4.30 L33 10.02 6.357 0.0 11.000 71.379 to 120.0 0.0 0.0 0.0 L34 435.78 0.0060 0.0 11.000 0.066 Vet = 4.41 L34 12.71 6.357 0.0 11.000 71.445 to 120.0 0.0 0.0 0.0 L35 448.49 0.0064 0.0 11.000 0.070 Vet = 4.53 L35 15.69 6.357 0.0 11.000 71.515 to 120.0 0.0 0.0 0.0 L36 464.18 0.0068 0.0 11.000 0.075 Vet = 4.69 L36 18.92 6.357 0.0 11.000 71.590 to 120.0 0.0 0.0 0.0 L37 483.1 0.0073 0.0 11.000 0.080 Vel= 4.88 L37 22.37 6.357 T 37.72 4.610 71.670 to 120.0 0.0 37.720 0.0 MF2 505.47 0.0079 0.0 42.330 0.335 Vel= 5.11 MF2 35.87 8.249 0.0 3.920 72.005 to 120.0 0.0 0.0 1.698 Fl 541.34 0.0023 0.0 3.920 0.009 Vet = 3.25 MFI 0.0 8.249 SE 105.706 153.210 73.712 to 120.0 0.0 105.706 8.987 BOR 541.34 0.0025 0.0 258.916 0.655 Vet = 3.25 Computer Programs by Hydratec Inc. Rq!..te 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 7 oenar Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 0.0 541.34 83.354 KFactor= 59.29 *NEWPATH 8 26.00 1.083 0.0 10.000 21.556 K Factor =5.60 to 120.0 0.0 0.0 0.0 9 26.0 0.1810 0.0 10.000 1.810 VeI= 9.06 9 27.07 1.083 T 5.84 10.667 23.366 K Factor = 5.60 to 120.0 0.0 5.840 4.331 11.1 53.07 0.6776 0.0 16.507 11.185 Vel= 18.48 0.0 53.07 38.882 K Factor = 8.51 *NEWPATH 10 65.48 1.083 E 2.336 4.230 21.878 K Factor = 14.00 to 120.0 T 5.84 8.176 0.0 11 65.48 0.9997 0.0 12.406 12.402 VeI= 22.81 0.0 34.280 KFactor= 11.18 • 65.48 NEW PATH 15 27.11 1.083 2E 4.672 10.000 23.442 K Factor= 5.60 to 120.0 T 5.84 10.512 0.0 15.1 27.11 0.1956 0.0 20.512 4.012 VeI= 9.44 0.0 27.11 27.454 KFactor= 5.17 *NEW PATH 21 27.87 1.083 T 5.84 10.710 24.765 K Factor =5.60 to 120.0 0.0 5.840 0.0 21.1 27.87 0.2058 0.0 16.550 3.406 Vel= 9.71 0.0 27.87 28.171 K Factor = 5.25 *NEWPATH 16 27.51 1.083 2E 4.672 10.000 24.130 K Factor =5.60 to 120.0 T 5.84 10.512 0.0 16.1 27.51 0.2009 0.0 20.512 4.121 Vel = 9.58 0.0 27.51 28.251 K Factor = 5.18 *NEW PATH 27A 42.83 1.083 E 2.336 21.580 9.359 K Factor = 14.00 to 120.0 0.0 2.336 4.331 27 42.83 0.4558 0.0 23.916 10.901 Vel = 14.92 69.43 S 1.418 T 6.849 13.583 24.591 K Factor = 14.00 120.0 0.0 6.849 -4.331 12 112.26 0.7292 0.0 20.432 14.900 VeI= 22.81 0.0 112.26 35.160 KFactor= 18.93 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 8 LenMark Date WHyd Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn *NEW PATH 24 70.37 1.083 T 5.84 4.230 25.268 K Factor = 14.00 to 120.0 0.0 5.840 0.0 13 70.37 1.1422 0.0 10.070 11.502 VeI= 24.51 0.0 70.37 36.770 K Factor= 11.60 *NEW PATH 25 64.17 1.083 E 2.336 5.230 21.007 K Factor = 14.00 to 120.0 T 5.84 8.176 0.0 26 64.17 0.9628 0.0 13.406 12.907 Vel = 22.35 26 0.0 3.334 0.0 14.000 33.914 to 120.0 0.0 0.0 0.0 18 64.17 0.0040 0.0 14.000 0.056 Vel = 2.36 18 65.17 3.334 0.0 7.750 33.970 to 120.0 0.0 0.0 0.0 19 129.34 0.0147 0.0 7.750 0.114 Vel = 4.75 0.0 40 129.34 34.084 KFactor= 22.15 *N EWPATH 17 65.18 1.083 E 2.336 4.230 21.675 K Factor = 14.00 to 120.0 T 5.84 8.176 0.0 18 65.18 0.9911 0.0 12.406 12.295 Vel= 22.70 0.0 65.18 33.970 KFactor= 11.18 *NEW PATH 14 26.68 6.357 0.0 1.410 70.515 to 120.0 0.0 0.0 0.0 L20 26.68 0.0 0.0 1.410 0.0 Vel = 0.27 L20 0.0 3.26 T 20.159 1.830 70.515 to 120.0 0.0 20.159 -0.793 M20 26.68 0.0009 0.0 21.989 0.020 Vel = 1.03 M20 0.0 2.635 2T 32.948 94.750 69.742 to 120.0 0.0 32.948 0.0 M19 26.68 0.0025 0.0 127.698 0.319 VeI= 1.57 M19 0.0 3.26 T 20.159 1.830 70.061 to 120.0 0.0 20.159 0.793 L19 26.68 0.0009 0.0 21.989 0.019 Vel = 1.03 L19 0.0 4.26 0.0 11.000 70.873 to 120.0 0.0 0.0 0.0 L18 26.68 0.0003 0.0 11.000 0.003 Vel = 0.60 4OL18 25.06 4.26 0.0 11.000 70.876 to 120.0 0.0 0.0 0.0 L17 51.74 0.0007 0.0 11.000 0.008 Vel = 1.16 L17 19.95 4.26 0.0 11.000 70.884 to 120.0 0.0 0.0 0.0 L16 71.69 0.0015 0.0 11.000 0.017 Vel = 1.61 Computer Programs by Hvdratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 9 enMark Date ' Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C,' or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn L16 16.64 4.26 - 0.0 11.000 70.901 to 120.0 0.0 0.0 0.0 L15 88.33 0.0022 0.0 11.000 0.024 Vel = 1.99 L15 13.59 4.26 0.0 11.000 70.925 to 120.0 0.0 0.0 0.0 L14 101.92 0.0029 0.0 11.000 0.032 Vel = 2.29 L14 10.80 4.26 0.0 11.000 70.957 to 120.0 0.0 0.0 0.0 L13 112.72 0.0035 0.0 11.000 0.038 Vet = 2.54 L13 8.28 4.26 0.0 11.000 70.995 to 120.0 0.0 0.0 0.0 L12 121.0 0.0039 0.0 11.000 0.043 Vel= 2.72 L12 6.00 4.26 0.0 11.000 71.038 to 120.0 0.0 0.0 0.0 Lii 127.0 0.0044 0.0 11.000 0.048 VeI= 2.86 Lii 3.83 4.26 0.0 11.000 71.086 to 120.0 0.0 0.0 0.0 kliLio 130.83 0.0045 0.0 11.000 0.050 VeI= 2.94 L10 0.99 4.26 0.0 11.000 71.136 to 120.0 0.0 0.0 0.0 L9 131.82 0.0046 0.0 11.000 0.051 Vel = 2.97 L9 -3.26 4.26 0.0 11.000 71.187 to 120.0 0.0 0.0 0.0 L8 128.56 0.0045 0.0 11.000 0.049 Vel = 2.89 L8 -5.39 4.26 0.0 11.000 71.236 to 120.0 0.0 0.0 0.0 L7 123.17 0.0041 0.0 11.000 0.045 VeI= 2.77 L7 -7.59 4.26 0.0 11.000 71.281 to 120.0 0.0 0.0 0.0 L6 115.58 0.0035 0.0 11.000 0.039 VeI= 2.60 L6 -10.01 4.26 0.0 11.000 71.320 to 120.0 0.0 0.0 0.0 L5 105.57 0.0031 0.0 11.000 0.034 VeI= 2.38 L5 -12.72 4.26 0.0 11.000 71.354 to 120.0 0.0 0.0 0.0 L4 92.85 0.0025 0.0 11.000 0.027 Vet = 2.09 L4 -15.69 4.26 0.0 11.000 71.381 to 120.0 0.0 0.0 0.0 L3 77.16 0.0017 0.0 11.000 0.019 VeI= 1.74 L3 -18.92 4.26 0.0 11.000 71.400 120.0 0.0 0.0 0.0 fL2 58.24 0.0010 0.0 11.000 0.011 Vel = 1.31 L2 -22.37 4.26 0.0 11.000 71.411 to 120.0 0.0 0.0 0.0 Li 35.87 0.0005 0.0 11.000 0.005 Vet = 0.81 Computer Programs by Hvdratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 10 enMark Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn Li 0.0 3.26 E 9.408 1.830 71.416 to 120.0 0.0 9.408 -0.793 Mi 35.87 0.0015 0.0 11.238 0.017 VeI= 1.38 Ml 0.0 2.635 2T 32.948 94.750 70.640 to 120.0 0.0 32.948 0.0 M38 35.87 0.0043 0.0 127.698 0.552 VeI= 2.11 M38 0.0 3.26 E 9.408 1.830 71.192 to 120.0 0.0 9.408 0.793 L38 35.87 0.0015 0.0 11.238 0.017 Vel = 1.38 L38 0.0 6.357 T 37.72 6.390 72.002 to 120.0 0.0 37.720 0.0 MF2 35.87 0.0001 0.0 44.110 0.003 VeI= 0.36 0.0 35.87 72.005 K Factor = 4.23 *NEW PATH L21 25.06 3.26 T 20.159 1.830 70.593 AlI o 21 120.0 0.0 20.159 -0.793 25.06 0.0008 0.0 21.989 0.018 Vel= 0.96 M21 0.0 2.635 T 16.474 94.750 69.818 to 120.0 0.0 16.474 0.0 M18 25.06 0.0022 0.0 111.224 0.248 Vel = 1.47 M18 0.0 3.26 T 20.159 1.830 70.066 to 120.0 0.0 20.159 0.793 L18 25.06 0.0008 0.0 21.989 0.017 Vel = 0.96 0.0 25.06 70.876 K Factor = 2.98 *NEW PATH L22 19.95 3.26 T 20.159 1.830 70.675 to 120.0 0.0 20.159 -0.793 M22 19.95 0.0005 0.0 21.989 0.012 Vel= 0.77 M22 0.0 2.635 2T 32.948 94.750 69.894 to 120.0 0.0 32.948 0.0 M17 19.95 0.0015 0.0 127.698 0.187 Vel= 1.17 M17 0.0 3.26 T 20.159 1.830 70.081 to 120.0 0.0 20.159 0.793 L17 19.95 0.0005 0.0 21.989 0.010 VeI= 0.77 0.0 19.95 70.884 K Factor = 2.37 *NEW PATH L23 16.65 3.26 T 20.159 1.830 70.751 OPM23 120.0 0.0 20.159 -0.793 16.65 0.0004 0.0 21.989 0.009 VeI= 0.64 M23 0.0 2.635 T 16.474 7.870 69.967 to 120.0 0.0 16.474 0.0 5 16.65 0.0010 0.0 24.344 0.025 Vel = 0.98 Computer Programs by Hvdratec Inc. Route 111 Windham N.H. USA 0310.17 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 11 denMark Date ''Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C' or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 5 0.0 2.635 0.0 18.000 69.992 to 120.0 0.0 0.0 0.0 6 16.65 0.0011 0.0 18.000 0.019 Vel= 0.98 6 0.0 2.635 0.0 20.000 70.011 to 120.0 0.0 0.0 0.0 7 16.65 0.0011 0.0 20.000 0.021 Vel = 0.98 7 0.0 2.635 T 16.474 48.880 70.032 to 120.0 0.0 16.474 0.0 M16 16.65 0.0010 0.0 65.354 0.068 Vel = 0.98 M16 0.0 3.26 T 20.159 1.830 70.100 to 120.0 0.0 20.159 0.793 L16 16.65 0.0004 0.0 21.989 0.008 Vel = 0.64 0.0 16.65 70.901 K Factor = 1.98 *NEW PATH L24 13.59 3.26 T 20.159 1.830 70.822 ALL, 120.0 0.0 20.159 -0.793 wvle-t 13.59 0.0003 0.0 21.989 0.007 Vel = 0.52 M24 0.0 2.635 2T 32.948 94.760 70.036 to 120.0 0.0 32.948 0.0 M15 13.59 0.0007 0.0 127.708 0.091 Vel = 0.80 M15 0.0 3.26 T 20.159 1.830 70.127 to 120.0 0.0 20.159 0.793 L15 13.59 0.0002 0.0 21.989 0.005 VeI= 0.52 0.0 13.59 70.925 K Factor = 1.61 *NEW PATH L25 10.80 3.26 T 20.159 1.830 70.890 to 120.0 0.0 20.159 -0.793 M25 10.8 0.0002 0.0 21.989 0.004 Vel = 0.42 M25 0.0 2.635 T 16.474 7.370 70.101 to 120.0 0.0 16.474 0.0 4 10.8 0.0005 0.0 23.844 0.011 Vel= 0.64 4 0.0 2.635 0.0 18.000 70.112 to 120.0 0.0 0.0 0.0 3 10.8 0.0004 0.0 18.000 0.008 Vel = 0.64 3 0.0 2.635 0.0 12.000 70.120 to 120.0 0.0 0.0 0.0 2 10.8 0.0005 0.0 12.000 0.006 Vel = 0.64 2 0.0 2.635 0.0 10.500 70.126 of, 120.0 0.0 0.0 0.0 10.8 0.0005 0.0 10.500 0.005 Vel = 0.64 1 0.0 2.635 T 16.474 46.880 70.131 to 120.0 0.0 16.474 0.0 M14 10.8 0.0005 0.0 63.354 0.030 Vel = 0.64 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 12 oenar Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn M14 0.0 3.26 T 20.159 1.830 70.161 to 120.0 0.0 20.159 0.793 L14 10.8 0.0001 0.0 21.989 0.003 Vel = 0.42 0.0 10.80 70.957 K Factor = 1.28 *NEW PATH L26 8.28 3.26 T 20.159 1.830 70.954 to 120.0 0.0 20.159 -0.793 M26 8.28 0.0001 0.0 21.989 0.003 Vel = 0.32 M26 0.0 2.635 2T 32.948 94.750 70.164 to 120.0 0.0 32.948 0.0 M13 8.28 0.0003 0.0 127.698 0.036 Vel = 0.49 M13 0.0 3.26 T 20.159 1.830 70.200 to 120.0 0.0 20.159 0.793 L13 8.28 0.0001 0.0 21.989 0.002 Vel = 0.32 0.0 8.28 70.995 K Factor= 0.98 NEW PATH L27 6.00 3.26 T 20.159 1.830 71.016 to 120.0 0.0 20.159 -0.793 M27 6.0 0.0 0.0 21.989 0.001 Vel= 0.23 M27 0.0 2.635 2T 32.948 94.750 70.224 to 120.0 0.0 32.948 0.0 M12 6.0 0.0002 0.0 127.698 0.021 Vel = 0.35 M12 0.0 3.26 T 20.159 1.830 70.245 to 120.0 0.0 20.159 0.793 L12 6.0 0.0 0.0 21.989 0.0 Vel = 0.23 0.0 6.00 71.038 K Factor= 0.71 *NEW PATH L28 3.83 3.26 T 20.159 1.830 71.076 to 120.0 0.0 20.159 -0.793 M28 3.83 0.0 0.0 21.989 0.001 Vel= 0.15 M28 0.0 2.635 2T 32.948 94.750 70.284 to 120.0 0.0 32.948 0.0 Mill 3.83 0.0001 0.0 127.698 0.009 Vel= 0.23 Mill 0.0 3.26 T 20.159 1.830 70.293 to 120.0 0.0 20.159 0.793 Lii 3.83 0.0 0.0 21.989 0.0 Vel= 0.15 0.0 3.83 71.086 K Factor = 0.45 NEW PATH LiO -0.99 3.26 T 20.159 1.830 71.136 to 120.0 0.0 20.159 -0.793 MiO -0.99 0.0 0.0 21.989 0.001 Vel= 0.04 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 13 -GenMark Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn M10 0.0 2.635 2T 32.948 94.750 70.344 to 120.0 0.0 32.948 0.0 M29 -0.99 0.0 0.0 127.698 -0.001 Vet = 0.06 M29 0.0 3.26 T 20.159 1.830 70.343 to 120.0 0.0 20.159 0.793 L29 -0.99 0.0 0.0 21.989 -0.001 Vet = 0.04 0.0 -0.99 71.135 KFactor= -0.12 *NEW PATH L9 3.25 3.26 T 20.159 1.830 71.187 to 120.0 0.0 20.159 -0.793 M9 3.25 0.0 0.0 21.989 0.001 VeI= 0.12 M9 0.0 2.635 2T 32.948 94.750 70.395 to 120.0 0.0 32.948 0.0 M30 3.25 0.0001 0.0 127.698 0.007 Vel = 0.19 M30 0.0 3.26 T 20.159 1.830 70.402 o 120.0 0.0 20.159 0.793 30 3.25 0.0 0.0 21.989 -0.001 Vel = 0.12 0.0 3.25 71.194 K Factor = 0.39 *NEW PATH L8 5.39 3.26 T 20.159 1.830 71.236 to 120.0 0.0 20.159 -0.793 M8 5.39 0.0 0.0 21.989 0.001 Vel = 0.21 M8 0.0 2.635 2T 32.948 94.750 70.444 to 120.0 0.0 32.948 0.0 M31 5.39 0.0001 0.0 127.698 0.017 Vel = 0.32 M31 0.0 3.26 T 20.159 1.830 70.461 to 120.0 0.0 20.159 0.793 L31 5.39 0.0 0.0 21.989 0.0 VeI= 0.21 0.0 5.39 71.254 K Factor = 0.64 *NEW PATH L7 7.59 3.26 T 20.159 1.830 71.281 to 120.0 0.0 20.159 -0.793 M7 7.59 0.0001 0.0 21.989 0.002 VeI= 0.29 M7 0.0 2.635 2T 32.948 94.750 70.490 to 120.0 0.0 32.948 0.0 M32 7.59 0.0002 0.0 127.698 0.031 Vel = 0.45 M32 0.0 3.26 T 20.159 1.830 70.521 OPL32 120.0 0.0 20.159 0.793 7.59 0.0001 0.0 21.989 0.002 Vel = 0.29 0.0 7.59 71.316 KFactor= 0.90 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 14 denMark Date 'Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. "C" or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn *NEW PATH L6 10.02 3.26 T 20.159 1.830 71.320 to 120.0 0.0 20.159 -0.793 M6 10.02 0.0002 0.0 21.989 0.004 Vel = 0.39 M6 0.0 2.635 2T 32.948 94.750 70.531 to 120.0 0.0 32.948 0.0 M33 10.02 0.0004 0.0 127.698 0.052 Vel = 0.59 M33 0.0 3.26 T 20.159 1.830 70.583 to 120.0 0.0 20.159 0.793 L33 10.02 0.0001 0.0 21.989 0.003 Vel = 0.39 0.0 10.02 71.379 KFactor= 1.19 *NEW PATH L5 12.72 3.26 T 20.159 1.830 71.354 to 120.0 0.0 20.159 -0.793 M5 12.72 0.0003 0.0 21.989 0.006 VeI= 0.49 M5 0.0 2.635 2T 32.948 94.750 70.567 0 120.0 0.0 32.948 0.0 M34 12.72 0.0006 010 127.698 0.081 Vel = 0.75 M34 0.0 3.26 T 20.159 1.830 70.648 to 120.0 0.0 20.159 0.793 L34 12.72 0.0002 0.0 21.989 0.004 Vel = 0.49 0.0 12.72 71.445 KFactor= 1.50 *NEW PATH L4 15.69 3.26 T 20.159 1.830 71.381 to 120.0 0.0 20.159 -0.793 M4 15.69 0.0004 0.0 21.989 0.008 VeI= 0.60 M4 0.0 2.635 21 32.948 94.750 70.596 to 120.0 0.0 32.948 0.0 M35 15.69 0.0009 0.0 127.698 0.119 VeI= 0.92 M35 0.0 3.26 T 20.159 1.830 70.715 to 120.0 0.0 20.159 0.793 L35 15.69 0.0003 0.0 21.989 0.007 Vel = 0.60 0.0 15.69 71.515 KFactor 1.86 *NEW PATH L3 18.92 3.26 1 20.159 1.830 71.400 to 120.0 0.0 20.159 -0.793 M3 18.92 0.0005 0.0 21.989 0.011 Vel = 0.73 M3 0.0 2.635 2T 32.948 94.750 70.618 o 120.0 0.0 32.948 0.0 M36 18.92 0.0013 0.0 127.698 0.169 Vel = 1.11 M36 0.0 3.26 T 20.159 1.830 70.787 to 120.0 0.0 20.159 0.793 L36 18.92 0.0005 0.0 21.989 0.010 VeI= 0.73 Computer Programs by Hvdratec Inc. Route 111 Windham N.H. USA 03087 Final Calculations - Hazen-Williams A&D FIRE SPRINKLERS Page 15 enMark Date Hyd. Qa Dia. Fitting Pipe Pt Pt Ref. f1cli or Ftng's Pe Pv ******* Notes Point Qt Pf/Ft Eqv. Ln. Total Pf Pn 0.0 18.92 71.590 K Factor = 2.24 *NEW PATH L2 22.37 3.26 T 20.159 1.830 71.411 to 120.0 0.0 20.159 -0.793 M2 22.37 0.0007 0.0 21.989 0.015 Vel = 0.86 M2 0.0 2.635 2T 32.948 94.750 70.633 to 120.0 0.0 32.948 0.0 M37 22.37 0.0018 0.0 127.698 0.230 Vel = 1.32 M37 0.0 3.26 T 20.159 1.830 70.863 to 120.0 0.0 20.159 0.793 L37 22.37 0.0006 0.0 21.989 0.014 VeI= 0.86 0.0 22.37 71.670 KFactor= 2.64 Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 tqCO Worldwide Fire Protection Contacts Products www.tyco-fire.com S Series EC-11 and Extended Covera! General Description TYCO Series EC-11 and EC-14 Extended Coverage Upright and Pendent Sprinklers are decorative glass-bulb sprinklers designed for use in light or ordinary hazard occu- pancies. They are intended for use in automatic sprinkler systems designed in accordance with standard installa- tion rules (e.g., NFPA 13) for a maximum coverage area of 400 ft2 (37,2 m2), as compared to the maximum coverage area of 130 ft2 (12,1 m2) for standard coverage sprinklers used in ordinary hazard occupancies or 225 ft2 (20,6 m2) for standard coverage sprinklers used in light hazard occupancies. Series EC-11 and EC-14 Sprinklers feature a UL and C-UL Listing that permits their use with unobstructed or non-combustible obstructed ceiling construction as defined and permitted by NFPA 13, as well as a specific appli- cation listing for use under concrete tees. Series EC-11 and EC-14 Extended Coverage Sprinklers have been fire tested to compare their performance to that of standard coverage spray sprin- klers. These tests have shown that the protection provided is equal to or more effective than standard coverage spray sprinklers. IMPORTANT Always refer to Technical Data Sheet TFP 700 for the "INSTALLER WARNING" that provides cautions with respect to handling and instal- lation of sprinkler systems and components. Improper handling and installation can permanently damage a sprinkler system or its compo- nents and cause the sprinkler to fail to operate in a fire situation or cause it to operate prematurely. Page 1 of 8 EC-14 Sprinklers, Upright and je Light and Corrosion-resistant coatings, where applicable, help extend the life of copper alloy sprinklers beyond that which occurs when exposed to corrosive atmospheres. Although corro- sion-resistant coated sprinklers passed standard corrosion tests of the appli- cable approval agencies, this testing is not representative of all possible corrosive atmospheres. Consequently, it is recommended that the end user be consulted with respect to the suitability of these corrosion-resistant coatings for any given corrosive environment. The effects of ambient temperature, concentration of chemicals, and gas/ chemical velocity should be consid- ered, along with the corrosive nature of the chemical to which the sprinklers will be exposed. NOTICE Series EC-11 and EC-14 Extended Coverage Sprinklers described herein must be installed and maintained in compliance with this document, as well as with the applicable standards of the National Fire Protection Association, in addition to the standards of any other authorities having jurisdiction. Failure to do so may impair the performance of these devices. The owner is responsible for main- taining their fire protection system and devices in proper operating condition. Contact the installing contractor or product manufacturer with any questions. NOVEMBER 2014 'jIV!1 I$II Sprinkler Identification Numbers (SINs) TY5137 - Upright, 11.2K 1Y5237 - Pendent, 11.2K TY6137 - Upright, 14.0K TY6237 - Pendent, 14.0K TY5137 is a re-designation for C5137, G1894, and S2510. TY5237 is a re-designation for C5237, G1893, and S2511. TY6137 is a re-designation for C6137, G1896, and S2610. TY6237 is a re-designation for C6237, G1895, and S2611. TFP22O 112 K and 140 K Pendent Ordinary Hazard WRENCH FLAT TFP22O Page 2 of 8 3/4 ESCUTCHEON PLATE NPT** SEATING SURFACE 2-7/16 (61,9 mm) UPRIGHT & PENDENT 1/2(12,7mm) J NOMINAL MAKE-IN UPRIGHT 16 nm) - 5 114 6* CROSS PENDENT SECTION Components: 1 - Frame 2 - Button 3 - Sealing Assembly 4 - Bulb 5 - Compression Screw 6 - Deflector * Temperature rating is indicated on Deflector. ** Pipe thread connections per ISO 7-1 can be provided on special request. FIGURE 1 SERIES EC-11 AND EC-14 EXTENDED COVERAGE SPRINKLERS 11.2 K-FACTOR UPRIGHT (TY5137) AND PENDENT (TY5237) 14.0 K-FACTOR UPRIGHT (TY6137) AND PENDENT (TY6237) ASSEMBLY Technical Data Approvals TYCO Series EC-11 and EC-14 Extended Coverage Upright, Pendent, and Recessed Pendent Sprinklers are UL and C-UL Listed. Refer to Table A for complete sprinkler approval infor- mation including corrosion-resistant status. The approvals apply to the service conditions indicated in the Design Criteria section. Series EC-11 and EC-14 Extended Coverage Upright and Pendent Sprinklers are FM Approved. Refer to Table A for complete sprinkler approval information including corrosion-resis- tant status. The approvals apply to the service conditions indicated in the Design Criteria section. The Style 60 Two-Piece Flush Escutcheon (Figure 4) is UL Listed and FM Approved for use with the Series EC-11 and EC-14 Pendent Sprinklers. Maximum Working Pressure 175 psi (12,1 bar) Pipe Thread Connection 3/4 inch NPT Discharge Coefficients K = 11.2 gpm/psi1/2 (161,3 1pm/barl/2) K = 14.0 gpm/p5i1/2 (201,6 1pm/bar1/2) Temperature Ratings Refer to Table A. Finish Sprinkler: Refer to Table A. Recessed or Flush Escutcheon: White-Coated, Chrome-Plated, and Brass-Plated Physical Characteristics Frame .......................Bronze Button.......................Bronze Sealing Assembly.......Beryllium Nickel w/TEFLON Bulb ...................Glass (3 mm) Compression Screw............Bronze Deflector......................Brass Operation The glass bulb contains a fluid that expands when exposed to heat. When the rated temperature is reached, the fluid expands sufficiently to shatter the glass bulb, which then allows the sprinkler to activate and flow water. Design Criteria TYCO Series EC-11 and EC-14 Extended Coverage Sprinklers must only be installed in accordance with the applicable UL and C-UL Listing or FM Approval requirements as indicated below. Only Style 30 or 40 Recessed Escutcheons are to be used for recessed installation, as applicable. Refer to Tables A, B, and C. 0 TFP22O Page 3 of 8 Hazard Type Temperature Bulb Liquid Sprinkler Finish (See Note 5) Natural Brass I Chrome Plated Polyester* Lead Coated Upright K=11.2 (TY5137) 135°F (57°C) Orange 1,2,3",4 ___________________________________ __________ _ 155°F(68°C) Red 175°F (79°C) Yellow Light Pendent Table B describes K11.2 (TY5237) K=14.0 (TY6237) 1,2,4 1, 2,4 200°F (93°C) Green 286°F(141°C) UL and C-UL Blue Recessed Pendent K=11.2 (TY5237) K14.0 (TY6237) With Style 30 Escutcheon 135°F (57°C) Orange 1,2,3,4 1, 2, 4 N/A Sensitivity Rating Table C describes FM Sensitivity Rating 155°F (68°C) Red 175°F (79°C) Yellow 200°F (93°C) Green 286°F (141°C) Blue Ordinary Upright K11.2 (TY5137) K=14.0 (TY6137) Pendent 135°F (57°C) Orange 1,2, 3,4 1,2,3,4 155°F (68°C) Red 175°F (79°C) Yellow 200°F (93°C) Green Table B describes UL and CUL Sensitivity Rating Table C describes FM Sensitivity Rating K=11.2 (TY5237) K=14.0 (TY6237) 1, 2,4 286°F (141°C) Blue Kr11.2 (TY5237) K14.0 (TY6237) With Style 30 or 40 Recessed Pendent 135°F (57°C) Orange 1, 2, 4 N/A 155°F (68°C) Red 175°F (79°C) Yellow Escutcheon 200°F (93°C) Green Notes (5). Where Polyester Coated or Lead Coated Sprinklers are noted to be UL and C-UL Listed, the sprinklers are UL and C-UL Listed as Cor- Listed by Underwriters Laboratories, Inc. (UL) rosion Resistant Sprinklers Listed by Underwriters Laboratories, Inc. for use in Canada (C-UL) ° Frame and Deflector only. Approved by Factory Mutual Research Corporation (FM) Pendent Only Approved by the City of New York under MEA 17703E N/A: Not Available TABLE A LABORATORY LISTINGS AND APPROVALS Light Hazard Ordinary Hazard Area Style 135°F 155°F 175°F 200°F 286°F 135°F 155°F 175°F 200°F 286°F (57°C) (68°C) (79°C) (93°C) (141°C) (57°C) (68°C) (79°C) (93°C) (141°C) Upright or Pendent - - - - - OR QR QR QR QR 14 x 14 Style 30 Recessed - - - - - OR OR OR OR OR Style 40 Recessed - - - - - OR OR OR OR OR Upright or Pendent QR- QR* QR* OR* OR* SR SR SR SR SR 16 x 16 Style 30 Recessed OR° OR* OR* QR* OR* SR SR SR SR SR Style 40 Recessed N/A N/A N/A N/A N/A SR SR SR SR SR Upright or Pendent OR* OR* QR* QR* QR* SR SR SR SR SR 18x18 Style 30 Recessed OR* QR* QR* QR* QR* SR SR SR SR SR Style 40 Recessed N/A N/A N/A N/A N/A SR SR SR SR SR Upright or Pendent QR* QR* OR" SR* SR* SR SR SR SR SR 20 x 20 Style 30 Recessed QR* OR" QR* SR* SR* SR SR SR SR SR Style 40 Recessed N/A N/A N/A N/A N/A SR SR SR SR SR OR: Quick Response SR: Standard Response N/A: Not Applicable ° Does not apply to Upright K=14.0 TABLE B SENSITIVITY RATING FOR UL AND C-UL LISTING OF SERIES EC- li OR EC-14 SPRINKLERS (Refer to Table D for Permitted K-Factor/Area Combinations) TFP22O Page 4 of 8 HC-1 Linear Spacing Area Spacing Ceiling Height Ceiling Type K-factor Style Response Min Max Min Max 10 20 100 400 Up to 30 Noncombustible Unobstructed, Noncombustible Obstructed, or 11.2 EC Pendent or Combustible Unobstructed 14.0 EC Upright Noncombustible Unobstructed, 11 2 EC . Pendent 10 20 100 400 Up to 30 Noncombustible Obstructed, or 14.0 EC Recessed Combustible Unobstructed Style 30 10 20 100 400 Up to 30 Combustible obstructed 11.2 EC EC Quick 14.0 Pendent or Upright 10 20 100 400 Up to 30 Combustible obstructed 11.2 EC 14.0 EC Pendent Recessed Style 30 10 20 100 400 Over 30 and up to 45 Noncombustible Unobstructed 11.2 EC 14.0 EC Upright HC-2 Linear Spacing Area Spacing Ceiling Height Ceiling Type K-factor Style Response Min Max Min Max 10 20 100 400 Up to 30 Noncombustible Unobstructed, 11.2 EC Upright Quick 10 20 100 400 Up to 30 14.0 EC Pendent or Upright Combustible Unobstructed 10 16 100 256Over 30 and up to 45 1.2 EC h40 EC Upright HC-3 Linear Spacing Area Spacing Ceiling Height Ceiling Type K-Factor Style Response Min Max Min Max 10 16 100 256 Up to 30 Noncombustible Unobstructed, Combustible Unobstructed 11.2 EC Upright Quick 10 20 100 400 Up to 30 14.0 EC Pendent or 10 16 100 256 Over 30 and up to 45 __________ 11.2 EC, 14.0 EC Upright I NOTE The design for K 11.2 EC (K 160 EC) sprinklers should not include fewer than six sprinklers or have a design pressure of less than 12 psi (0,8 bar) similarly the design for K 14.0 EC (K 200 EC)sprinklers should not include fewer than four sprinklers or have a design pressure of less than 18 psi (1,2 bar). For flow criteria, refer to FM Loss Prevention Data Sheet 3-26. TABLE C SENSITIVITY RATING FOR FM APPROVAL OF SERIES EC- 11 OR EC-14 SPRINKLERS (Note: Refer to FM Loss Prevention Data Sheet 2-0 for permitted K-factor/area combinations) S UL and C-UL Listing Requirements Series EC-11 and EC-14 Sprinklers may be used for the coverage areas shown in Table D, based on main- taining the minimum specified flow rate as a function of coverage area and hazard group for all sprinklers in the design area. Series EC-11 and EC-14 Sprinklers are permitted to be used with unobstructed or non-combustible obstructed ceiling construction as defined and permitted by NFPA 13; for example: Unobstructed, combustible or noncombustible, ceiling construc- tion with a deflector to ceiling/roof deck distance of 1 to 12 inches (25 to 300 mm). Obstructed, non-combustible, ceiling construction with a deflector location below struc- tural members of 1 to 6 inches (25 to 150 mm) and a maximum deflector to ceiling/roof deck distance of 22 inches (550 mm). Series EC-11 and EC-14 Sprinklers, specifically tested and listed for non-combustible obstructed construction, are permitted to be used within trusses or bar joists having non-combustible web members greater than 1 inch (25.4 mm) when applying the 4 times obstruction criteria rule defined under "Obstructions to Sprinkler Discharge Pattern Development". To prevent cold soldering, the minimum allowable spacing between Series EC-11 and EC-14 Sprinklers, is 8 feet (2,4 m) for upright sprinklers and 9 feet (2,7 m) for pendent sprinklers. TFP22O Page 5 of 8 Description Area Light Hazard 0.10 gpmlft2 Group I Ordinary Hazard 0.15 gpm/ft2 Group II Ordinary Hazard 0.20 gpm/ft2 gpm psi gpm psi gpm psi 14x14 30 7.2 30 7.2 39 12.1 16 x 16 30 7.2 39 12.1 51 20.7 TY5137 (K=11.2) Upright 18 x 18 33 8.7 49 19.1 65 33.7 20x20 40 12.8 60 28.7 80 51.0 14 x 14 30 7.2 30 7.2 39 12.1 16 x 16 30 7.2 39 12.1 51 20.7 TY5237 (K=11.2) Pendent 18 x 18 33 8.7 49 19.1 65 33.7 20x20 40 12.8 60 28.7 80 51.0 14 x 14 N/A N/A 39 7.8 51 13.3 TY6137 16x16 N/A N/A 39 7.8 51 13.3 (K=14.0) Upright 18x18 N/A N/A 49 12.3 65 21.6 20 x 20 N/A N/A 60 18.4 80 32.7 14 x 14 37 7.0 39 7.8 51 13.3 16x16 37 7.0 39 7.8 51 13.3 TY6237 (K=14.0) Pendent 18 x 18 37 7.0 49 12.3 65 21.6 20x20 40 8.2 60 18.4 80 32.7 1 ft. = 0.3048 m 1 psi = 0.06895 bar 1 ft.2 =0.093 m2 1 gpm = 3.785 1pm 1 gpm/ft2 = 40.74 mm/mm TABLE D FLOW CRITERIA FOR UL AND C-UL LISTING OF SERIES EC-Il AND EC-14 SPRINKLERS 5. Series EC-11 and EC-14 Sprinklers are to be installed in accordance with all other requirements of NFPA 13 for extended coverage upright and pendent sprinklers; For example, obstructions to sprinkler discharge, obstructions to sprinkler pattern development, obstructions to prevent sprinkler discharge from reaching hazard and clearance to storage. UL and C-UL Specific Application Listing Requirements for Installation under Concrete Tees Series EC-11 and EC-14 Extended Coverage Upright and Pendent Sprinklers (TY5137, TY5237, TY6137 and TY6237) have a UL and C-UL Specific Application Listing for use under concrete tees when installed as follows: 1. Stems of the concrete tee construc- tion must spaced at less than 7.5 feet (2,3 m) on center but more than 3 feet (0,9 m) on center. The depth of the concrete tees must not exceed 30 inches (762 mm). The maximum permitted concrete tee length is 32 feet (9,8 m). However, where the concrete tee length exceeds 32 feet (9,8 m), non-combustible baffles, equal in height to the depth of the tees, can be installed so that the space between the tees does not exceed 32 feet (9,8 m) in length. The sprinkler deflectors are to be located in a horizontal plane at or above 1 inch (25,4 mm) below the bottom of the concrete tee stems. When the sprinkler deflectors are located higher than a horizontal plane 1 inch (25,4 mm) beneath the bottom of the concrete tee stems, the obstruction to sprinkler discharge criteria requirements of NFPA 13 for extended coverage upright and pendent sprinklers applies. FM Approval Requirements Series EC-11 and EC-14 Extended Coverage Sprinklers are to be installed in accordance with the applicable Factory Mutual Loss Prevention Data Sheet for limited use in buildings of specific roof construction and for the protection of certain specific ordinary hazard (non-storage and/or non-flam- mable or combustible liquid) occu- pancies. Information provided in the FM Loss Prevention Data Sheets relates to, but not limited to, hydraulic design, ceiling slope, and obstructions, minimum and maximum allowable spacing, and deflector-to-ceiling distance. These criteria may differ from UL and/or NFPA criteria. Therefore, the designer should review and become familiar with Factory Mutual requirements before proceeding with design. 2-7/8' DIA. (73,0 mm) 2-1/4' DIA. (57,2 mm) MOUNTING 1/8' SURFACE (3,2 mm) I CLOSU RE 3/4" NPT 25/16(587mm) -MOUNTING 1-13/16" (46,0 mm) PLATE INTERNAL DIMENSIONS OF STYLE 60 ESCUTCHEON ACCOMMODATE CLASS 150 MALLEABLE - IRON REDUCING SPRINKLER FITTING TFP22O Page 6 of 8 2-7/8 DIA. 1/2±1/8 (73,0 mm) 1/2 (12,7 mm) (12,7±3,2 mm) - 2-1/4 DIA. 1/4' (6,4 mm) FACE OF (57,2 mm) SPRINKLER L ..J 1/8" FITTING ). (3,2 mm) Mir I FF 77 I MOUNTING SURFACE MOUNTING PLATE CLOSURE 1-3/8(34,9mm) 1-1/8" (28,6 mm) FIGURE 2 SERIES EC-11 AND EC-14 RECESSED PENDENT SPRINKLER ASSEMBLY WITH TWO-PIECE 1/2 INCH TOTAL ADJUSTMENT STYLE 30 RECESSED ESCUTCHEON 2-7/8' DIA. 5/8±1/4 (73,0 mm) 3/4" (19,1 mm) - (15,9±6,4 mm) 2-1/4" DIA. 1/4' (6,4 mm) FACE OF (57,2 mm) SPRINKLER ç 1/8' FITTING (3,2 mm) Elm MOUNTING MOUNTING SURFACE PLATE CLOSURE 1-3/8' (34,9 mm) 7/8' (22,2 mm) FIGURE 3 SERIES EC- Il AND EC-14 RECESSED PENDENT SPRINKLER ASSEMBLY WITH TWO-PIECE 3/4 INCH TOTAL ADJUSTMENT STYLE 40 RECESSED ESCUTCHEON S FACE OF SPRINKLER FITTING: 3/8" (9,5 mm) ABOVE TO 1/8" (3,2 mm) BELOW MOUNTING SURFACE ESCUTCHEON PLATE = SEATING SURFACE: 1/4" (6,4 mm) ABOVE TO 1/2" (12,7 mm) BELOW MOUNTING SURFACE; 3/4" (19,1 mm) TOTAL ADJUSTMENT Installation Series EC-11 and EC-14 Sprinklers must be installed in accordance with this section. General Instructions Do not install any bulb-type sprinkler if the bulb is cracked or there is a loss of liquid from the bulb. With the sprinkler held horizontally, a small air bubble should be present. The diameter of the air bubble is approximately 1/16 inch (1,6 mm) for the 135°F (57°C) to 3/32 inch (2,4 mm) for the 286°F (141°C) temperature ratings. A leak-tight 3/4 inch NPT sprinkler joint should be obtained by applying a minimum-to-maximum torque of 10 to 20 ft.-lbs. (13,4 to 26,8 Nm). Higher levels of torque may distort the sprinkler inlet with consequent leakage or impairment of the sprinkler. Do not attempt to compensate for insufficient adjustment in an Escutcheon Plate by under or over- tightening the Sprinkler. Re-adjust the position of the sprinkler fitting to suit. Step 1. Install the sprinkler with the deflector parallel to the mounting surface. Install pendent sprinklers in the pendent position; install upright sprin- klers in the upright position. Step 2. After installing the Style 30, 40, or 60 mounting plate (or other "FITTING SIDE" TOWARDS SPRINKLER FITTING 01 /\ WRENCH RECESS / (ENDA") FIGURE 5 W- TYPE 3 SPRINKLER WRENCH WRENCH RECESS - WRENCH HEX FIGURE 6 W-TYPE 22 RECESSED SPRINKLER WRENCH applicable escutcheon) over the sprinkler pipe threads and with pipe- thread sealant applied to the pipe threads, hand-tighten the sprinkler into the sprinkler fitting. Step 3. For upright or pendent sprin- klers wrench-tighten using only the FIGURE 4 SERIES EC- 11 AND EC- 14 PENDENT SPRINKLER ASSEMBLY WITH 3/4 INCH TOTAL ADJUSTMENT STYLE 60 TWO-PIECE FLUSH ESCUTCHEON TFP22O Page 7 of 8 PIN 51 - XXX -X -XXX F SIN SPRINKLER TEMPERATURE FINISH RATING 893 11.2K PENDENT TY5237 1 NATURAL BRASS 135 135°F(57°C) 894 11.2K UPRIGHT TY5137 4 SIGNAL WHITE (RAL9003) 155 155°F (68°C) POLYESTER 895 14.0K PENDENT TY6237 5 JET BLACK (RAL9005) 175 175°F (79°C) POLYESTER 896 14.0K UPRIGHT TY6137 7 LEAD COATED 200 200°F (93°C) * Escutcheon ordered separately 9 CHROME-PLATED 286 286°F (141°C) 000 OPEN** ** OPEN indicates sprinkler assembly without glass bulb, button, and sealing assembly. TABLE E SERIES EC- 11 AND EC- 14 UPRIGHT AND PENDENT SPRINKLERS PART NUMBER SELECTION W-Type 3 (End A) Sprinkler Wrench. For the pendent sprinkler installed with Style 30, 40, or 60 Escutcheon, wrench-tighten the sprinkler using only the W-Type 22 Sprinkler Wrench. Apply the wrench recess of the appli- cable sprinkler wrench (Figure 5 and 6) to the sprinkler wrench flats (Figure 1). Care and Maintenance TYCO Series EC-11 and EC-14 Sprinklers must be maintained and serviced in accordance with this section. Before closing a fire protection system main control valve for maintenance work on the fire protection system that it controls, obtain permission to shut down the affected fire protection systems from the proper authorities and notify all personnel who may be affected by this action. Sprinklers which are found to be leaking or exhibiting visible signs of corrosion must be replaced. Automatic sprinklers must never be painted, plated, coated, or otherwise altered after leaving the factory. Modified sprinklers must be replaced. Sprinklers that have been exposed to corrosive products of combustion, but have not operated, should be replaced if they cannot be completely cleaned by wiping the sprinkler with a cloth or by brushing it with a soft bristle brush. Care must be exercised to avoid damage to the sprinklers before, during, and after installation. Sprinklers damaged by dropping, striking, wrench twist/slippage, or the like, must be replaced. Also, replace any sprinkler that has a cracked bulb or that has lost liquid from its bulb. (Ref. Installation Section.) Frequent visual inspections are recom- mended to be initially performed for corrosion resistant coated sprin- klers, after the installation has been completed, to verify the integrity of the corrosion resistant coating. Thereafter, annual inspections per NFPA 25 should suffice; however, instead of inspecting from the floor level, a random sampling of close-up visual inspections should be made, so as to better determine the exact sprinkler condition and the long term integrity of the corrosion resistant coating, as it may be affected by the corrosive conditions present. The owner is responsible for the inspection, testing, and maintenance of their fire protection system and devices in compliance with this document, as well as with the applicable standards recognized by the Approval agency (e.g., NFPA 25), in addition to the standards of any authorities having jurisdiction. Contact the installing contractor or product manufacturer with any questions. Automatic sprinkler systems are recom- mended to be inspected, tested, and maintained by a qualified Inspection Service in accordance with local requirements and/or national codes. Limited Warranty For warranty terms and conditions, visit www.tyco-fire.com. Ordering Procedure Contact your local distributor for availability. When placing an order, indicate the full product name and Part Number (P/N). Sprinkler Assemblies with NPT Thread Connections Specify: Series EC-11 or EC-14 (specify) Sprinkler, SIN (specify), (specify) K-factor, Pendent or Upright (specify) Extended Coverage, (specify) temper- ature rating, (specify) finish, P/N (from to Table F) Recessed Escutcheon, Two-Piece Specify: Style (30 or 40) Two-Piece Recessed Escutcheon with (specify) finish, P/N (specify*) Flush Escutcheon, Two-Piece Specify: Style 60 Two-Piece Flush Escutcheon with (specify) finish, P/N (specify*) *Refer to Technical Data Sheet TFP778 Sprinkler Wrenches Specify: W-Type 3 Sprinkler Wrench, P/N 56-895-1-001 Specify: W-Type 22 Recessed Sprinkler Wrench, P/N 56-665-7-001 TFP22O Page 8 of 8 is S GLOBAL HEADQUARTERS 11400 Pennbrook Parkway, Lansdale, PA 19446 I Telephone +1-215-362-0700 Copyright © 2014 Tyco Fire Products, LP. All rights reserved. tjt]L1i iJF I TECHNICAL REPORT HAZARDOUS MATERIALS SUMMARY I For I GenMark Diagnostics, Inc. 2210 Faraday Avenue, Suite 120, Carlsbad, CA 92008 (August 25, 2015) (Rev. 2 September 29, 2015) OCCUPA TIONAL AS1 60117 2210 FARADAY AV 120 GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 2 Table of Contents OSI's Cas2CIass Database used to Produce Technical Reports..............................4 1.1. Report Preparation Process ................................................................................... 4 1.2. Company Information.............................................................................................4 1.3. Report Submission to the Carlsbad Fire Department.............................................4 1.4. Executive Summary...............................................................................................5 1.5. Construction Scope of Work ..................................................................................5 1.6. Deferred Submittal Items .......................................................................................5 1.7. Hazardous Materials Information ...........................................................................6 1.8. Control Area Information........................................................................................6 1.9. Hazardous Materials Business Plan ......................................................................6 Hazard Classification Process...................................................................................6 Table 1 Chemical Classification Form Control Area I ...............................................7 Table 1.1 Chemical Classification Summary Sheet (Control Area 1) ........................8 Table 1.2 Chemical Classification Summary Totals-(Control Area 1)......................12 Table 2 Chemical Classification Form (Mechanical Yard).......................................14 Table 2.1 Chemical Classification Summary Sheet (Mechanical Yard)...................14 Table 2.2 Chemical Classification Summary Totals-(Mechanical Yard)..................14 Table 3 Summary Sheet Non-Reg. Hazard Classes-(Control Area 1) ....................15 Bulking and Dispensing of Hazardous Materials and Wastes.................................16 Table 4 Bulking and Dispensing Area Locations.....................................................16 Table 5 List of Hazardous Materials to be Bulked and/or Dispensed......................16 Building/Facility Information ....................................................................................17 Attachment Information...........................................................................................17 Operational Information...........................................................................................18 Operational Controls ...............................................................................................20 16.1 Automatic Fire Extinguishing System for buildings ..............................................20 16.2 Seismic Bracing and Shelf Construction for hazardous materials ......................... 20 16.3 Separation of Incompatible Materials...................................................................20 16.4 Empty Containers ................................................................................................21 16.5 Security ................................................................................................................ 21 16.6 Portable Fire Extinguishers..................................................................................21 16.7 Approved Flammable Liquid and Hazardous Materials Storage Cabinets........... 21 16.8 Compressed Gases.............................................................................................21 16.9 Corrosive Materials..............................................................................................21 16.10 Cryogenic Fluids..................................................................................................22 16.11 Organic Peroxides ............................................................................................... 22 -- 16.13 Highly Toxic& Toxic Materials 22 16.14 Water Reactive Solids and Liquids ......................................................................22 16.15 Laboratory Fume Hoods and Building Exhaust and Ventilation...........................23 16.16 Sources of Ignition ...............................................................................................25 16.17 Spill Control, Drainage, Secondary Containment ................................................. 25 16.18 Explosion Control.................................................................................................25 16.19 Limit Controls.......................................................................................................26 16.20 Pressure Controls ................................................................................................26 16.21 Treatment Systems..............................................................................................26 16.22 Protection from Vehicles......................................................................................26 GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 3 16.23 Employee Training and Response Procedures/Hazard Communication .............26 16.24 Storage of Hazardous Materials...........................................................................27 17. Hazardous Materials Information Summary............................................................ 27 Attachment I (Project Site Vicinity Map).........................................................................29 Attachment 1.1 (Facility Site Location)............................................................................30 Attachment 2 (First Floor Control Area Plan)..................................................................31 Attachment 2.1 (Mechanical Yard Area Plan) ...................................... ........................... 32 Attachment 2.2 (Hazardous Materials Facility Site Map Symbols)..................................33 Attachment 3 (Curriculum Vitae).....................................................................................34 Attachment 4 (NCSA Certificate Number CFC0306.13) .................................................35 0 GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 4 1. OSI's Cas2CIass Database used to Produce Technical Reports Occupational Services, Inc. ("OSI") owns a custom-designed Microsoft Access database that has been continually improved, updated and amended to reflect the current California Fire Code. Over 125,000 chemicals are currently recognized and classified by their Chemical Abstract Service Number (CAS No.) in Os,, s database, called "CAS2Class." The foundation of OS I's Technical Report is the Physical Hazard Summary and Health Hazard Summary reports produced by CAS2Class. 1.1. Report Preparation Process Before presenting a Technical Report to a Code Official, OSI collects the tenant's "proposed" chemical inventory and imports the inventory into CAS2Class. OSI then makes a proper hazard determination for every unclassified chemical. OSI uses trained and degreed HazMat professionals to determine the hazard categories, which are based on the chemical's Material Safety Data Sheet (MSDS), the manufacturer's product literature, and textbooks, along with the concentration, physical state, chemical properties and health hazards of that chemical. OSI also refers to NIOSH, OSHA, EPA and DOT hazard classifications. OSI uses all these physical and chemical references to properly classify the chemical according to the categories listed in Appendix E of the 2013 California Fire Code (CFC). When 100% of the tenant's chemical inventory is properly classified, OSI generates these two tables: Physical Hazard Summary and Health Hazard Summary. OSI then compares the tenant's summaries to the Maximum Allowable Quantity (MAQ) per Control Area of Hazardous Materials Posing a Physical Hazard listed in Table 5003.1.1 (1) & 5003.1.1(3) of the • 2013 CFC and the Maximum Allowable Quantity per Control Area of Hazardous Materials Posing a Health Hazard in Table 5003.1.1(2) & 5003.1.1(4) of the 2013 California Fire Code (CFC).. If the entire inventory does not exceed the MAQs, OSI advises the architect to design and construct one control area. If the MAQs are exceeded, OSI advises the architect to design more control areas until the inventory does not exceed MAQs. Many hours of technical expertise are spent designing the quantity and one-hour boundaries of the control areas. OSI and the architect use this CAS2Class report at the beginning of the design process and the information is used to form the basis of the building design. 1.2. Company Information GenMark Diagnostics, Inc. is located in city of Carlsbad California and is a leading provider of automated, multiplex molecular diagnostic testing systems that detect and measure DNA and RNA targets to diagnose disease and optimize patient treatment. Utilizing GenMark Diagnostic's proprietary eSensor® detection technology, eSensor® XT-8 system is designed to support a broad range of molecular diagnostic tests with a compact, easy-to-use workstation and self-contained, disposable test cartridges. GenMark Diagnostics, Inc. currently markets three tests that are FDA cleared for lVD use: Cystic Fibrosis Genotyping Test, Warfann Sensitivity Test, and Thrombophilia Risk Test. A Respiratory Viral Panel (RVP) has been submitted to the FDA for 510(k) clearance. GenMark Diagnostics, Inc. performs a number of other tests, including HCV Genotyping and 2C19, versions of which are available for research use only, and KRAS, are in development for IVD use. 1.3. Report Submission to the Carlsbad Fire Department OSI and GenMark Diagnostics Inc., understand the Carlsbad Fire Department will review this Hazardous Materials Opinion and Technical Report and that the Building Official will request Carlsbad • Fire Department's approval on this Hazardous Material Opinion and Technical Report. GenMark Diagnostics, Inc. will file the San Diego Regional Hazardous Materials Questionnaire DEH HM-9171 with the San Diego County Department of Environmental Health. The Hazardous Material Questionnaire will have the County Health stamp provided in the 'RELEASED FOR BUILDING PERMIT GenMark Diagnostics, Inc. September 29, 2015 Technical Report/ Hazardous Materials Summary (Rev.2) Page 5 BUT NOT FOR OCCUPANCY'. The Business Plan will be processed by the Client with the County Health Department'while construction occurs, and will be completed prior to the Certificate of Occupancy is obtained, and provided to the Fire Official. A completed copy of the Hazardous Materials Business Plan and this Technical Opinion Report will be submitted to the Carlsbad Fire Department: City of Carlsbad Fire Department Fire Prevention Division 1635 Faraday Avenue Carlsbad, CA 92008-7314 www.firemaiI(ä.carIsbadca. -gov P: (760) 602-4665 F: (760) 602-8561 1.4. Executive Summary GenMark Diagnostics, Inc. is submitting this Technical Report as part of a tenant improvement to remodel (24,727 ft) of the existing building (186,392 ft2). The GenMark Diagnostics, Inc., facility Suite 120 will occupy a total area of (30,947 ft2) of the (186,392 ft2) building located at 2210 Faraday Avenue, in the city of Carlsbad CA, 92008 has This Technical Opinion Report was prepared by Ricky R. Francis Sr., Certified California Fire Code Inspector (CFC0306.13), AS, CCFCI, (Curriculum Vitae attached), of Occupational Services, Inc. (OSI), 6397 Nancy Ridge Drive, San Diego CA 92121, and (858) 558-6736. This report includes: Building/facility information, Operational information, Hazardous Materials information for 2210 Faraday Avenue, Suite 120, Carlsbad CA 92008. This report does not include any High Piled Combustible Storage requirements. 1.5. Construction Scope of Work Construction of new lab and clean room medical device research & development spaces within existing previously improved tenant space at the first floor level work include non-load bearing interior walls and partitions, suspended acoustical ceiling systems and associated that there is no change to the total existing floor area of the building. Construction of new interior mechanical equipment mezzanine and access stair. New equipment yard and screened enclosure at existing loading dock area, associated structural, mechanical, plumbing and electrical work. Existing previous office improvements including restrooms and break room area are to remain unchanged. There is no scope of work in the area of the existing improvements. 1.6. De1erredSUt5ffittfltems Fire Sprinkler System, design in accordance with 2013 CFC, Section 903, and NFPA 13, 2013 edition. Fire Alarm System, 2013 CFC, Sections 907.1 through 907.9 (which includes all other uses and occupancy groups associated with this project), and NFPA 72, 2.013 edition. • Commodity in warehouse to be classified in accordance with the NFPA 13, 2013 edition, Section 5.6.1.2 for mixed commodities and applied to Table 13.2.1 for discharge criteria for miscellaneous storage 12 feet or less in height. GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 6 1.7. Hazardous Materials Information GenMark Diagnostics, Inc. will store, use and handle Hazardous Materials at different locations within the facility. Hazardous Materials will be stored, used and handled in accordance with the 2013 California Fire Code (CFC). None of the Hazardous Materials stored, used or handled within tenant space (Control Area) exceed the Maximum Allowable Quantities (MAQs) per Control Area of Hazardous Materials posing a Physical Hazard listed in 2013 CFC Table 5003.1.1(1), 5003.1.1(3) and 2013 (CBC) Table 307.1 (1) or the Maximum Allowable Quantities (MAQs) per Control Area of Hazardous Materials posing a Health Hazard in 2013 (CFC) Table 5003.1.1(2), 5003.1 .1(4) and 2013 (CBC) Table 307.1 (2). 1.8. Control Area Information There is one (1) control area inside the GenMark Diagnostics, Inc.'s facility and a Mechanical Yard enclosure listed below. The Chemical Classification Form Table 1 list all chemicals stored, used or handled within the GenMark Diagnostics, Inc.'s facility located at 2210 Faraday Avenue, Suite 120, in the city of Carlsbad California. Control Area I (Suite 120) Mechanical Yard Based on the volume of Hazardous Materials on site, the design and operation of GenMark Diagnostics, Inc.'s facility will be in compliance with the 2013 California Fire Code and 2013 California Building Code. There will be no hazardous materials stored or used in the Mezzanine area of the GenMark Diagnostics' facility 1.9. Hazardous Materials Business Plan Based on the proposed tenant improvements and use of discloseable quantities of hazardous materials at 2210 Faraday Avenue, Suite 120, Carlsbad CA 92008 GenMark Diagnostics, Inc. will be required to update the current Hazardous Materials Business Plan within the San Diego County Department of Environmental Health (DEH) California Environmental Reporting System (CERS). GenMark Diagnostics, Inc. is not updating the Business Plan at this time; however GenMark Diagnostics, Inc. commits to updating the Business Plan within the San Diego County Department of Environmental Health (DEH) California Environmental Reporting System (CERS) prior to final occupancy and understands that the Building Department and Carlsbad Fire Department will not grant a final Certificate of Occupancy until the updated Business Plan has been submitted within the San Diego County Department of Environmental Health (DEH) California Environmental Reporting System (CERS). 2. Hazard Classification Process Table I and Table 2 (Chemical Classification Forms) of this Technical Report is a list of every chemical inside GenMark Diagnostics, Inc. facility and Mechanical Yard located at 2210 Faraday Avenue, Suite 120, Carlsbad CA 92008. The chemical inventory is sorted alphabetically, and then by Control Area. Included in Table I is the Chemical Name, Percent Concentration (% Conc.), CAS Number (Chemical Abstract Service Number), Quantity (QTY), Units of Measure, Hazard Classification, Storage and Use Location of Chemical in Control Area. The majority of the inventory items have more than one hazard class. For example, Isopropanol is listed in Table I (Chemical Classification Form) has three hazard • classes, Flammable Class I-B (FL-lB) (chemical liquid has a flash point below 73 degrees Fahrenheit and boiling point of above 100 degrees Fahrenheit), Irritants (lRR) (acute chemical exposure irritates the skin), and Other Health Hazards (OHH) (chronic chemical exposure causes affect the human body- GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 18 Attachment 2.1 is a copy of the outside Mechanical Yard Area Plan for GenMark Diagnostics, Inc. indicating proposed outside Mechanical yard Area Plan Control Area within 2210 Faraday Avenue, Suite 120, Carlsbad, CA 92008. Attachment 2.2 is a copy of the Facility Hazardous Materials Site Map Symbols Legend for GenMark Diagnostics, Inc. located at 2210 Faraday Avenue, Suite 120, Carlsbad, CA 92008. Attachment 3 is a copy of Curriculum Vitae for Ricky R. Francis Sr., AS, CCFCI Attachment 4 is a copy of NCSA Certificate Number CFC01 80.07 for Ricky R. Francis Sr., Certified California Fire Code Inspector 15. Operational Information GenMark Diagnostics, Inc. manufactures markets and distributes generic pharmaceutical formulations. GenMark Diagnostics, Inc. located at 2210 Faraday Avenue, Suite 120, Carlsbad CA 92008 will store, use and handle Hazardous Materials within the building/facility. An operational permit is required to store, transport on site, dispense, use or handle hazardous materials in excess of the amounts listed below in Table 105.6.20. GenMark Diagnostics, Inc., will stored, used and handled Hazardous Materials in accordance with the 2013 California Fire Code (CFC) and all state, federal, and local regulations. Table 105.6.20 PERMIT AMOUNTS FOR HAZARDOUS MATERIALS Table 105.6.20 PERMIT AMOUNTS FOR HAZARDOUS MATERIALS TYPE OF MATERIAL AMOUNT Combustible Liquids See Section 2013 CFC 105.6.16 Corrosive materials Gases See Section 2013 CFC 105.6.8 Liquids 55 gallons Solids 500 pounds Explosive materials See Section 2013 CFC 105.6.14 Flammable materials Gases See Section 2013 CFC 105.6.8 Liquids See Section 2013 CFC 105.6.16 Solids 100 pounds Highly toxic materials Gases See Section 2013 CFC 105.6.8 liquids AnyAmount Solids Any Amount Oxidizing materials See Section 2013 CFC 105.6.8 Gases Liquids Any Amount I gallon Class 4 10 gallons Class 3 55 gallons Class 2 Class I Any Amount Solids 10 pounds Class 4 100 pounds n 0 GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 19 Table 105.6.20 PERMIT AMOUNTS FOR HAZARDOUS MATERIALS TYPE OF MATERIAL AMOUNT Class 3 500 pounds Class 2 Class I Organic peroxides Liquids Class I Any Amount Class II Any Amount Class III 1 gallon Class IV 2 gallons Class V No Permit Required Solids Class I Any Amount Class II Any Amount Class III 10 pounds Class IV 20 pounds Class V No Permit Required Pyrophoric materials Gases Any Amount Liquids Any Amount Solids Any Amount Toxic materials Gases See Section 2013 CFC 105.6.8 Liquids 10 gallons Solids 100 pounds Unstable (reactive) materials Liquids -CIaSS4 -Any-Amount Class 3 Any Amount Class 2 5ga110ns Class 1 10 gallons Solids Class 4 Any Amount Class 3 Any Amount Class 2 50 pounds Class 1 100 pounds GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 20 Table 105.6.20 PERMIT AMOUNTS FOR HAZARDOUS MATERIALS TYPE OF MATERIAL AMOUNT Water-reactive materials Liquids Any Amount Class 3 5 gallons Class 2 55 gallons Class I Solids Class 3 Any Amount Class 2 50 pounds Class 1 500 pounds 16. Operational Controls The following controls will be installed at 2210 Faraday Avenue) Suite 120, Carlsbad CA 92008 16.1 Automatic Fire Extinguishing System for buildings . 12013 CFC 9032 NFPA 131 The building is fully equipped with an existing, approved) automatic wet fire extinguishing system. 16.2 Seismic Bracing and Shelf Construction for hazardous materials [2013 CFC 5003.9.91 Shelves greater than six feet high will be braced and anchored and be of substantial construction. Shelves will be provided with lips or guards. The facility will be equipped with adequately braced and anchored shelving of substantial noncombustible construction with a chemical resistant coating. Shelves will be provided with a lip or guards. Shelf storage of hazardous materials will be maintained in an orderly manner and in compliance with the Code. 16.3 Separation of Incompatible Materials [2013 CFC 5003.9.81 Incompatible materials will be separated from each other in storage in (FM) approved self- closing storage cabinets, or in separate (UL) listed or (DOT) approved waste collection incompatible materials: Storage in separate approved self-closing storage cabinets as follows: Flammable/Combustible liquids (Class I, II, and Ill-A) will be stored in approved flammable liquids cabinets, Acids will be stored in acid cabinets, Bases will be stored in base cabinets. Trained personnel will further distinguish between incompatible materials (i.e. acids and bases; oxidizers and flammables; acids and flammables) and store them in an appropriate manner with adequate distance to avoid incompatible reactions. Incompatible gases will be separated by a distance of more than twenty feet GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 21 Incompatibles will be separated using noncombustible partitions/barrier greater than 18" high. Employees will receive chemical safety instruction on the separation of incompatible materials. 16.4 Empty Containers [2013 CFC 5003.2.5] The storage of empty containers and containers previously used for the storage of flammable or combustible liquids, unless free from explosive vapors, will be stored as required for filled tanks and containers. Tank and containers, when emptied will have the covers or plugs immediately replaced in openings. 16.5 Security [NFPA 730 & NFPA 731] The building/facility will be equipped with lock(s) to prevent unauthorized entry, security cameras and motion detectors. The security measures in place at 2210 Faraday Avenue, Suite 120, Carlsbad CA, 92008 are within compliance of the Code. 16.6 Portable Fire Extinguishers [2013 CFC 906] The facility will be equipped with portable dry chemical fire extinguishers. There will be an appropriate amount of approved fire extinguishers mounted not more than 75 feet apart within the GenMark Diagnostics, Inc. facility, located at 2210 Faraday Avenue, Suite 120, Carlsbad CA 92008. The appropriate amount and type fire extinguishers will be located throughout the building; designated dispensing areas and laboratories. 16.7 Approved Flammable Liquid and Hazardous Materials Storage Cabinets [2013 CFC 5003.8.7.2, 5704.3.2] Flammable and combustible liquids will be stored in approved flammable liquid storage cabinets. Doors will be well fitted, self-closing, and equipped with a latch. Cabinets shall be clearly identified in an approved manner with red letters on contrasting background to read: HAZARDOUS-KEEP FIRE AWAY. 16.8 Compressed Gases [2013 CFC 5301.1) Storage, use and handling of compressed gas containers, cylinders, tank and systems shall comply with the 2013 CFC Chapter 53. Partially full compressed gas containers, cylinders or tanks containing residual gases shall be considered as full containers for the purposes of the controls required. Compressed gases in service and in storage will be stored upright and adequately secured with one or more support straps and/or chains to prevent cylinders from Wing or being knocked-DvaT.--CyfWeTs,—including-empty-ones,-w*df-have-#Teirraps-in-ptace-aTTd valves tightly closed. Cylinder will always be secured. Cylinders will only be moved by properly trained GenMark Diagnostics, Inc. employees and Licensed Commercial Contractors with an approved cylinder cart and/or dolly. The storage, use and handling of compressed gases at GenMark Diagnostics, Inc., shall be in accordance with the 2013 CFC and the 2013 NFPA 55. 16.9 Corrosive Materials [2013 CFC 5403.1] The storage and use of corrosive materials in amounts not exceeding the maximum S Allowable quantity per control area indicated in the 2013 CFC Section 5003.1 shall be in Accordance with the 2013 CFC Sections 5001, 5003, and 5401. GenMark Diagnostics, Inc., will store and use corrosive materials in quantities below maximum allowable quantities indicated in the 2013 CFC Table 5003.1.1(2). Corrosive materials will be stored, used GenMark Diagnostics, Inc. September 29, 2015 . Technical Report / Hazardous Materials Summary (Rev.2) Page 22 and handled in accordance with the 2013 CFC Sections 5001, 5003, and 5401. 16.10 Cryogenic Fluids [2013 CFC 5501.1] Storage, use and handling of cryogenic fluids shall comply with the 2013 CFC Chapter 55. Cryogenic fluids classified as hazardous materials shall also comply with the general requirements of the 2013 CFC Chapter 50. Partially full containers containing residual cryogenic fluids shall be considered as full containers for the purposes of the controls required. Cryogenic fluid containers in service and in storage within GenMark Diagnostics, Inc. facility will be properly stored in accordance with the 2013 Chapters 50 and 55. Containers, including empty ones, will have their caps in place and valves properly positioned in accordance with manufacturer specifications. Containers will only be moved by properly trained GenMark Diagnostics, Inc. employees and Licensed Commercial Contractors. The storage, use and handling of cryogenic fluids at GenMark Diagnostics, Inc., shall be in accordance with the 2013 CFC and the 2013 NFPA 55. 16.11 Organic Peroxides [2013 CFC 6201] The storage and use of organic peroxides in amounts not exceeding the maximum Allowable quantity per control area indicated in the 2013 CFC Section 5003.1 shall be in accordance with the 2013 CFC Sections 5001, 5003, 6201 and 6203. GenMark Diagnostics, Inc., will store and use organic peroxides in quantities below maximum allowable quantities indicated in the 2013 CFC Table 5003.1.1(1). Organic Peroxides will be stored, used . and handled in accordance with the 2013 CFC Sections 5001, 5003, 6201 and 603. 16.12 Oxidizing Materials [2013 CFC 6303] The storage and use of oxidizing materials in amounts not exceeding the maximum Allowable quantity per control area indicated in the 2013 CFC Section 5003.1 shall be in accordance with the 2013 CFC Sections 5001, 5003, 6301 and 6303. GenMark Diagnostics, Inc., will store and use oxidizing materials in quantities below maximum allowable quantities indicated in the 2013 CFC Table 5003.1.1(1). Oxidizing materials will be stored, used and handled in accordance with the 2013 CFC Sections 5001, 5003, 6301 and 6303. 16.13 Highly Toxic & Toxic Materials [2013 CFC 6303] The indoor storage or use of toxic solids or liquids in amounts not exceeding the Maximum Allowable quantity per control area indicated in the 2013 CFC Table 5003.1.1 (2) shall be in accordance with the 2013 CFC Section 5001, 5003 and 6001. GenMark Diagnostics, Inc., will store and use highly toxic and toxic solids and liquids in quantities below Maximum allowable quantities indicated in the 2013 CFC Table 5003.1.1(2). Toxic materials will be stored, used and handled in accordance with the 2013 CFC Sections 5001, 5003 and 6001. 16.14 Water Reactive Solids and Liquids (2013 CFC 67031 The storage and use of water-reactive solids and liquids in amounts not exceeding the Maximum Allowable Quantity per control area indicated in the 2013 CFC Section 5003.1 shall be in accordance with the 2013 CFC Sections 5001, 5003, 6701 and 6703. GenMark Diagnostics, Inc., will store and use water-reactive materials in quantities below Maximum allowable quantities indicated in the 2013 CFC Table 5003.1.1(1). Oxidizing Materials will be stored, used and handled in accordance with the 2013 CFC Sections 5001, GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 23 5003, 6701 and 6703. 16.15 Laboratory Fume Hoods and Building Exhaust and Ventilation and Types of Material Exhausted [2013 CMC Chapter 5] Fume Hood Exhaust System Specifications. Fume Hood Exhaust Duct System shall be designed in accordance with the 2013 California Mechanical Code. . Fume Hood Exhaust System does not convey flammable dusts. Fume Hood Exhaust Ducting shall be independent and completely separate from Environmental Air Ducts and shall not extend into or through plenums. Flammable Gases and Vapors in the Exhaust Systems. Flammable vapor or fumes is the concentration of flammable constituents in air that exceeds twenty-five percent (25%) of its Lower Flammability Limit (LFL). The Fume Hood Exhaust and Ventilation System at GenMark Diagnostics, Inc. will comply with the 2013 California Mechanical Code and the California Energy Commission Standards. Scientists will be trained not to exhaust incompatibles into the ventilation systems. Bench scale laboratory reactions will be performed in the fume hoods at GenMark Diagnostics, Inc. and will be in compliance with the . Code of Federal Regulations Volume 29 Part 19 10.1450. The storage and use of flammable and combustible liquids and gases in hoods and exhaust ducts will be limited to the smallest amounts needed each day. Concentrations of gases and vapors will be diluted to less than 25% of the Lower Explosive Limit (L.E.L.) for each compound. Therefore, no automatic fire protection systems will be required in the fume hoods or exhaust ducts. C. Corrosive Materials Corrosives will be used in the chemical fume hoods. Corrosives will be neutralized in the chemical experiments and the corrosives will not be exhausted untreated directly into the fume hoods at concentrations that could attack the ducting or accumulate and drip. The corrosives are used in milliliters quantities for pH adjustment and not at original strength nor heated and exhausted untreated where they could attack the ducting. Heating Th-rnateria!eingexbaustedoLbebeaterLaboM.a.standar.droomtemp.eratuLe Mechanical exhaust will be provided where Class I, II, or III liquids are used (in any amount) in Group B, or portions thereof. Under normal operating conditions explosive vapor-air mixtures will not develop in the exhaust system at GenMark Diagnostics, Inc. The majority of the work involving Class I, II, or Ill-A flammable liquids will be performed in chemical fume hoods, not in the open laboratories as indicated in Section 10 (Bulking and Dispensing of Hazardous Materials and Wastes) of this technical opinion report. The exhaust ventilation will be sufficient to maintain non-flammable and non-explosive vapor concentrations throughout the entire exhaust duct system. GenMark Diagnostics, Inc. activities will not require elevated temperatures, therefore separate and distinct exhaust systems are not required. Calculations to determine necessary CFM required to maintain levels 25% LEL for Class GenMark Diagnostics, Inc. September 29, 2015 . Technical Report I Hazardous Materials Summary (Rev.2) Page 24 I, II, Ill-A Flammable liquids Hoods and Building Exhaust Systems and Types of Material Exhausted Calculations to Determine Required CFM to Maintain Levels <25% LEL for Flammable Liquids The following report contains calculations for the volume of air in cubic feet per minute (CFM) required to dilute flammable liquid vapors to 25% or below their lower explosive limit. These calculations represent a spill scenario in which a one-gallon container of flammable liquid was to shatter in fume hood, releasing the entire contents. The calculations are based on the release being vaporized consistently for a one-hour period. Table 6 Flammable Liquids Stored in 2210 Faraday Avenue, Suite 120, Carlsbad CA 92008 Flammable/Combustible Liquid Molecular Weight Specific Gravity Lower Explosive Limit Vapor Density ACETONE 58.08 0.791 2 2 ACETONITRILE 41.18 0.786 3 1.42 ISOPROPANOL 60.1 0.785 2 2.03 METHANOL 32.04 1 0.791 1 6 1.11 Calculating the Required CFM The following calculations were made to determine the minimum ventilation required to assure that the . aforementioned flammable liquids are maintained below 25% of the Lower Explosive Limit. Requirements were based on the cubic feet of air required per gallon of evaporation. The calculation used was taken from 2011 NFPA 86 "Ovens and Furnaces" Method for Determining Solvent Safety Ventilation Rates Section 11.6.8.4. 41_8.33 ')(spG (bOO_LEL') / CFM to maintain <25% LEL = 0.075) VD A LEL 60 nun Where: 4.0 = Safety Factor to Account for 25% LEL 8.33 = Weight of 1 gallon of water 0.075 = Weight of dry air in 29.9 in. Hg SpGr: Specific gravity VD = Vapor Density LEL = Lower Explosion Limit Table 6.1 is a worst-case scenario in which the CFM calculated was to account for a gallon of flammable liquid being released in a fume hood over a one hour period. Table 6.1 Minimum Required Ventilation in CFM to maintain concentrations of Flammable Liquids below 25% Lower Explosive Limit (LEL) during a one-gallon spill situation released over a one-hour period Table 6.1 Minimum CFM Required to Maintain Flammable Liquids below 25% Lower Explosive Umit (LEL Required CFM to maintain below 25% LEL -Flammable/Combustible Liquid & at 25% LEL/G for one-hour GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 25 Table 6.1 Minimum CFM Required toMaintain Flammable Liquids below 25% Lower Explosive Limit (LEL Flammable/Combustible Liquid ft3 at 25% LEUG Required CFM to maintain below 25% LEL for ofle-hour ACETONE 8610 143 ACETONITRILE 7951 132 ISOPROPANOL 8255 137 METHANOL 4960 83 The worst case scenario spilt for the flammable liquids stored in a fume hood at GenMark Diagnostics, Inc. facility is a one gallon release of ACETONE. To ensure that such a spill be maintained at 25% the tower explosive limit, fume hoods must provide an airflow of a minimum of 143 cubic feet fresh air, per minute. All of GenMark Diagnostics, Inc. fume hoods will exhaust more than 143 CFM. Since the exhaust volumes will be greater than 143 CFM, the duct work is classified as Class I or Class 5 Ducts. Table 6.2 below indicates proposed materials to be used within GenMark Diagnostics, Inc. fume hoods located at 2210 Faraday Avenue, Suite 120, Carlsbad California, 92008. Table 6.2 Proposed Hazardous Materials used within GenMark Diagnostics, Inc. Fume Hoods Hazardous Material/Chemical - Hazardous Classifications Compatible/incompatible with other, Chemicals listed in Table 6.1 ACETONE FLAMMABLE LIQUID CLASS IC COMPATIBLE ACETONITRILE FLAMMABLE LIQUID CLASS lB COMPATIBLE ISOPROPANOL FLAMMABLE LIQUID CLASS lB COMPATIBLE METHANOL FLAMMABLE LIQUID CLASS IS COMPATIBLE HAZ.WASTE FLAMMABLE LIQUIDS FLAMMABLE LIQUID CLASS lB COMPATIBLE Proposed Hazardous Materials listed above in Table 6.2 are used in different experiments and/or processes within all GenMark Diagnostics, Inc. fume hoods and designated areas located at 2210 Faraday Avenue, Suite 120, Carlsbad California, 92008. 16.16 Sources of Ignition [2013 CFC 5704.2.41 In locations where flammable vapors could be present, precautions will be taken to prevent ignition by eliminating or controlling sources of ignition. Adequate grounding and bonding will be provided to prevent the accumulation of static electricity wherever Class I or II liquids are bulked and/or dispensed. Smoking and open flames will be prohibited in locations where flammable vapors could be present. 16.17 Spill Control, Drainage, Secondary Containment 12013EC_5O0.L2JQQ42_2 _&50O42.2 1 Carts and trucks transporting liquids shall be capable of containing a spill from the largest single container transported. GenMark Diagnostics, Inc. will never store vessels containing hazardous materials greater than 55 gallons inside facility building. The vessels exceeding 1.1 gallon capacity in the (designated bulking and/or dispensing areas) used for flammable liquids will be equipped with secondary containment. S 16.18 Explosion Control [2013 CFC 5005.2.1.2] Explosion control shall be provided in accordance with the 2013 CFC Section 5004.6 when explosive environment can occur because of the characteristics or nature of the hazardous GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 26 materials dispensed or used, or as a result of the dispensing or use process. Flammables, oxidizers, unstable reactive compounds, and water-reactive compounds will be stored in approved explosion proof or flammable liquid cabinets. The explosion controls will be in compliance with the 2013 CFC Sections 911, 5004.6 and 5005.2.1.2. 16.19 Limit Controls (2013. CFC 5005.1.41 Temperature Controls will be maintained in the event of a power failure. Temperature controls will be in compliance with the Code. 16.20 Pressure Controls (2013 CFC 5004.8.21 Stationary tanks and equipment containing hazardous materials that can generate pressure exceeding design limits because of exposure fires or internal reaction shall have some form of construction or other approved means that will relieve excessive internal pressure. The means of pressure relief shall vent to an approved location. The pressure controls for the cryogenic liquid tank will be in compliance with the California Fire Code and all Federal, State and Local regulations. 16.21 Treatment Systems [TITLE 22 CCR CH-12 ARTICLE-1 {66262.I0] GenMark Diagnostics, Inc. will properly manage any hazardous waste generated at 2210 Faraday Avenue, Suite 120, Carlsbad CA 92008 in accordance with Federal State and Local regulations. 16.22 Protection from Vehicles [2013 CFC 312] GenMark Diagnostics, Inc. will install an 8' (foot) high chain link equipment enclosure equipped with 42" (inch) steel pipe guardrail & swinging gate around the mechanical yard area. GenMark Diagnostics, Inc., will store a 316 gallon diesel generator, compressed gas, and 3000 gallon tank of liquid nitrogen within the mechanical yard enclosure as illustrated on Attachment 2.1. All vehicle impact protection needed will be in compliance with the 2013 CFC 312. 16.23 Employee Training and Response Procedures/Hazard Communication [2013 CFC 406, 2013 CFC 407, and Title 8 CCR §5194] Persons responsible for the operational of areas in which hazardous materials are stored, bulked, dispensed, handled, or used shall be trained initially and annually on the chemical hazards of the materials and the appropriate spill mitigation procedures. The supplied training will be in compliance with 2013 CFC 406, 2013 CFC 407, and Cal/OSHA Title 8 CCR §5194. GenMark B agnostics Inc has-provided-eal/OSHA-cornpliant-Hazard-Gomrnunication-safety training course and will continue to provide refresher courses every year. The following information is taught to each hazmat employee in the building: In the event of a FIRE: First, notify local fire department by dialing 911 from a landline when possible, versus a mobile phone. Next, if possible, have an employee trained on the proper use of a fire extinguisher extinguish the fire with an ABC fire extinguisher. If the fire cannot be extinguished safely with one extinguisher, evacuate all personnel from the building. SMALL SPILL: Use the emergency spill kits compatible with the spilled materials. Refer to Material Safety Data Sheets (MSDSs) for protective clothing and clean up guidelines. Waste products will be handled and disposed of as hazardous waste. Notify the Fire Department by GenMark Diagnostics, Inc. September 29, 2015 Technical Report / Hazardous Materials Summary (Rev.2) Page 27 dialing (911) if the spill represents a fire hazard or hazardous materials are released outside of the building. LARGE SPILL: Secure the area and warn others away. Contact Samantha Chua of GenMark Diagnostics, Inc. 760-448-4300 to develop a clean-up plan. Notify the Fire Department by dialing (911) if the spill represents a fire hazard or hazardous materials are released outside of the building. Arrangements will be made with a licensed waste disposal firm for assistance with cleanup and disposal of hazardous wastes. 16.24 Storage of Hazardous Materials [2013 CFC Chapter 50] Hazardous Materials are not stored in quantities greater than the exempt amount for "B," "A3" and "S-I" Occupancy. Hazardous Materials will not be stored and/or used on second floor of this building within GenMark Diagnostics, Inc. All Hazardous Materials will be stored in (FM) approved and/or (UL) Listed self-closing safety cabinets or containers in accordance with the 2013 CFC. 17. Hazardous Materials Information Summary GenMark Diagnostics, Inc. will store, transport on site, use and handle Hazardous Materials in accordance with the 2013 California Fire Code and all federal, state and local regulations in its facility located at 2210 Faraday Avenue, Suite 120 in the city of Carlsbad California. This hazardous material technical opinion report is based on 2013 CBC Tables 307.1(1) and 307.1(2) and the 2013 CFC Tables 5003.1.1(1) through 5003.1.1(4). None of the hazardous materials exceed the Maximum Allowable Quantities (MAQs) for Physical or Health Hazards for storage or use. The report identifies hazardous materials by chemical name and all classifications were based on hazard categories delineated in 2013 CFC Appendix E "Hazard Categories." Aggregate quantities of each hazardous material and each hazard category have been specified. The aggregate quantity in use and storage shall not exceed the quantity listed for storage. Hazardous Materials have been identified as: in use, open system use, closed system use in accordance with the 2013 CFC. The Hazardous Materials storage, use, and handling at GenMark Diagnostics, Inc. will be in accordance with the 2013 CFC, Federal, State and Local Regulations. I certify that all information contained herein, including the attachments, is true and correct. I have the Authority to act on behalf of GenMark Diagnostics, Inc., relative to matters involved in this Technical Opinion Report. A copy of my Curriculum Vitae (Attachment 3) is attached along with a copy of current certification as a Certified tCalifornia Fire Code lnspectorfrom rNational Code Services AssocitrtAttachrnent3). Approved: Ricky R. Francis Sr., AS, CCFCI Certified California Fire Code Inspector Occupational Services, Inc. 6397 Nancy Ridge Drive San Diego, CA 92121 Tel: 858-558-6736/Fax: 858-558-6756 1 www.occserv.com GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 28 Reviewed and Approved: V. Chad Hansen, MS, CIH, CSP, CPE Director, EH&S Services Occupational Services, Inc. 6397 Nancy Ridge Drive San Diego, CA 92121 Tel: 858-558-6736/Fax: 858-558-6756 I www.occserv.com As a Representative of GenMark Diagnostics, Inc., I certify that I have reviewed and approve all of the information contained herein, including the attachments of this Technical Opinion Report. I act on behalf of GenMark Diagnostics, Inc., relative to matters involved in this Technical Opinion Report. Samantha Chua Senior Manager EHS GenMark Diagnostics, Inc. 5964 La Place Court Carlsbad, CA 92008 Tel: 760-448-4300 I GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 29 0 Attachment I (Project Site Vicinity Map) Attachment I is a copy of a Vicinity Map Project Site location for the GenMark Diagnostics, Inc. Located at 2210 Faraday Avenue, Suite 120, Carlsbad, CA 92008. VICINITY MAP 0 NUK 0 NOT TO SCALE 2210 Faraday Avenue, Suite 120, Carlsbad CA 92008 0 GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 30 Attachment 1.1 (Facility Site Location) Attachment 1.1 is a copy of the facility site location for GenMark Diagnostics, Inc. located at 2210 Faraday Avenue, Suite 120, Carlsbad CA 92008 Liquid Om Nitrogen 3000 Diesel Generator Parking nerator staging Area Parking Area )( XXK Not aPart GenMark Not a Part of Diagnostics, in1 of GenMark 210FaradayAve.l GenMark Commercial Building Suite 160 Suite 120 I SUIt6 100 2200 Faraday Ave - ft1llIll] AE M [•Parking Area Parking Area • 2214 I I ° I Panting Area 02~24~J ~ixo FARADAY AVENUE fOfljROd V. Mis. I GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (R6v.2) Page 31 Attachment 2 (First Floor Control Area Plan) Attachment 2 is a copy of the First Floor Control Area Plan and Hazardous Materials storage, handling, bulking and dispensing locations for GenMark Diagnostics, Inc. indicating existing building First Floor Plan Control Area within 2210 Faraday Avenue, Suite 120, Carlsbad, CA 92008. [ ]]] 2 H [ III 141 Hallway 140 _ Lj Ze ow Dc t 1 [ lH 1i.. HLWJ [j I Shell Space 6own Formulation ....4148.I SPLLK ri<0~ Gown' Shipping/Receiving l 130 QCSet.Up ' 168 in I j 145 IHM4 I G ncomln fig C6 QC EED QC I Mi ISO 267 Amplicon sp. 139 10 E 151 66 tHVSJ !hv ay 1 F EIR9 127 *12n 9ic! J129 ak 133 anr Hallway 153 r Vestibule S it Hallway 122 Bller/LRM Shell Space EPLIX yHallway 161 158 255 120 t135 Ti Open office 121 Shell Space 136 :i;;VlP1~11;;; aldocki Supplies 163 D.y Room 162 -, 157 -Ne Hazardous-Mate na l-is-stoced-or-used-on-Sec-ond--F-Ioor of this Building S GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 32 Attachment 2.1 (Mechanical Yard Area Plan) Attachment 2.1 is a copy of the outside Mechanical Yard Area Plan for GenMark Diagnostics, Inc. indicating proposed outside Mechanical yard Area Plan Control Area within 2210 Faraday Avenue, Suite 120, Carlsbad, CA 92008. Diesel Generator Air Cooled Chiller 3000 Gallon DI Water Skid 316 Gallon Liquid Nitrogen DI WaterjS~kijd Co 316] (LN2)Tank (3000] 1J L I '\\(/ L •'\( ______ ________________________________ LJ l ii T' --j I I / I I lilil [iITO,H 8' Foot high Chain Link Equipment Enclosure with 42" Steel Pipe Guardrail & Swinging Gate U. L..1 GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 33 Attachment 2.2 (Hazardous Materials Facility Site Map Symbols) Attachment 2.2 is a copy of the Facility Hazardous Materials Site Map Symbols Legend for GenMark Diagnostics, Inc. located at 2210 Faraday Avenue, Suite 120, Carlsbad, CA 92008. Hazardous Materials Facility Site Map SYMBOLS Y he DapwtrTwssl _________ p4rnJsjer yfites1 ffl Cømp(esed Gs- lffl1V CaNnct IMSDSl SfttyDotoEcct Fs Gas Frnssjency trnfq,nolau. In Cylinders i IBEP 1 flui.sfi Plus. Chnücs'J ltsvesslay 6 Maps Outside Hazardous HWS I iws lsssoe Hrd05js CiD Pressuazea Tank IOI Warti)streagn 10HMs1 outwe H2Ol0OUfl I IHMS Ins-Ae H23dOU It€4lalS5tOra)e Storage Insida Hazardous ''° '° IOHMHI Hazardous Tank in l.rrIl ttatena!s Handling I IHMH I Meteflals Handling .upioslves a Und IgIOdTdilr blasbngAgents () No.FLmablGas Insijiatea tank Flanasatle Uquirit Mir H5itfl 2ñtd Corrosive $> cnc () F,ro Hydrant . - Alrerelwe Bmnr. X rest Ujflltl qd Re Dmad Tract 0y3en <6> tMuutdPoVatC'3t -•-- Rands.liSp UnstatIa Raoalva Indicate by Name aable .o4lø Wales Ilescive PiIIIIIiIIlIIIIi Indleete tOw€St to p,T1ns Hazardous Materials Cattier <9> 11omn Gas <> -larisnable Ca. Iaznrduu [J Flammable Storage Cabinet I I F1or Draln unrsri Gas Shut Sewer Connection Storm Drain GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 34 Attachment 3 (Curriculum Vitae) Curriculum Vitae for Ricky R. Francis Sr., AS, CCFCI EDUCATION Associate Science Degree, Environmental Health and Safety Management (EHSM), Cuyamaca College, San Diego, California 2009. PROFESSIONAL TRAINING National Code Services 2014 California Fire Code Inspector Recertification Exam, 2014 National Code Services 2013 California Fire Code Training, 2013 California Fire Prevention Officers 2009 lFC High-Piled Combustible Storage Training, 2012 Confined Space Entry Certification Training Certificate OSHA 29CFR (1910.146) 2004 OSHA 40-Hour HAZWOPER Training, 2004 with Eight Hour HAZWOPER Refresher Training, 2013. US Navy Hazardous Materials Control and Management (HMC&M) Technician, Naval Occupational Safety and Health and Environmental Training, 1995 PROFESSIONAL HISTORY Occupational Services, Inc. (2001 to Present) Hazardous Materials Specialist: Conducts chemical inventories, hazardous materials technical reports and Combustible, Explosive and Dangerous Materials (CEDMAT) inspection preparation, providing accurate Chemical Health Hazard, Physical Hazard and Chemical Hazard Classification limits per building control area in accordance with the 2013 California Fire Code and Building Code. Prepares Combustible, Explosive and Dangerous Materials (CEDMAT) reports, state and local Hazardous • Materials Business Plans (HMBP). Updates and maintains a Microsoft Access Database Chemical Classification Program of over 200,000 chemicals, and chemical compounds. Accomplishments: Compiles required physical chemical inventories of over 150,000 hazardous/non-hazardous chemicals and chemical compounds. Provides necessary chemical safety Material Safety Data Sheet (MSDS) and/or Safety Data Sheet (SDS) training. Drafted and implemented over 50 Occupational Safety Injury Illness and Prevention Programs (IIPP), Hazardous Material Business Plans (HMBP), California Accidental Release Programs (CalArp), Industrial User Wastewater Discharge Permits, and Hazardous Material/Toxic Chemical and Controlled Substance Management Reports in accordance with federal, state and local regulations. Naval Air Station North Island, Coronado CA (1994-2001) Aviation Maintenance Department Quality Assurance Chief Petty Officer, and Egress System AM (E) Supervisor. Manages 10 First Class Petty Officers Supervises Maintenance Safety Program for over 750 Squadron personnel during launching, recovering, inspecting, maintenance and servicing of over 20 C-2 Greyhound, and E-2 Hawkeye aircraft. Responsible safety of flight aircraft inspections, investigating accident/mishaps, analyzing material damage, personal injury accidents and cases of occupational illnesses and injuries. Generate and Submits Aircraft (HMR) Hazardous Material Reports for defective and ineffective C-2/E-2 Aircraft Systems and Subsystems. Conducts quarterly audits and monitors all aircraft organizational level maintenance programs. Compiles statistical data and prepares charts, tables and hazard reports to prevent the occurrence of accidents and defects. Performs risk assessment of hazardous process/conditions identified. Advises the Aircraft Maintenance Officer of methods of control and/or elimination of identified hazards, including various available alternative measures. Aircraft Mechanic performing depot and organizational level maintenance on C-2/E-2 aircraft Propulsion, Air-conditioning, Pressurization, Structural, Flight Control, Hydraulics, and Emergency Systems. 0 I GenMark Diagnostics, Inc. September 29, 2015 Technical Report I Hazardous Materials Summary (Rev.2) Page 35 Attachment 4 (NCSA Certificate Number CFC0306.13) NCSA Certificate Number CFC0306.13 Ricky R. Francis Sr., AS, CCFCI: Certified California Fire Code Inspector NATIONAL CODE SERVICES ASSOCIATION, INC. Ricky Renard Francis Sr. Certified California Fire Code Inspector The National Code Ser*es Association attests that the individual named on this cenilkate has sails facriwiiy demonstrated knowkdgc of the California Fire Code by successfully completing the prescribed written examination, based on the 2013 edition. Witnessed by our hand Certificate No. CFC0306.13 Issued:- August 3, 2014 NCSA For the National Code Sences Association \ ~—~ 9