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-(Srz02I 00 I c13 I here by certify that this plan, specification, ', /,f�i_ '(� or report was prepared by me or under my direct supervision and that I am NICET Certified Brent Kotula Dat—e7711 NICET Certification No. 113889 Water-Based Systems Layout - Level IV Certification Expires: June 1, 2023 • Up01101 RECEIVED AquaSAFETM Fire Safety System NOV 9 2021 OfFJCZ C CITY OF TIGARD BUILDING DIVISION Uponor 5925 148th Street West Apple Valley, MN 55124 800-321-4739 Job Name : RIVER TERRACE MULTIPLEXES -Two Head Calculation (H.1 & H.5) Drawing : RESIDENTIAL Location : 2 STORY TRIPLEX ADU-2 TIGARD OR Remote Area : 1 Contract : 39400F 001 Data File : River Terrace Multiplexes 39400F 001 2 Story Triplex, ADU-2. Date/Time : 07/02/2021 -06:43 AM Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Uponor Page 1 RIVER TERRACE MULTIPLEXES -Two Head Calculation (H.1 & H.5) Date 7/2/2021 HYDRAULIC DESIGN INFORMATION SHEET Name - RIVER TERRACE MULTIPLEXES Date - 07/02/2021 Location - TIGARD OR Building - RESIDENTIAL System No. - 1 Contractor - ALLIANCE PLUMBING Contract No. - 39400F 001 Calculated By - TIM McDONALD Drawing No. - F100 Construction: (X) Combustible ( ) Non-Combustible Ceiling Height VARIES OCCUPANCY - RESIDENTIAL S Type of Calculation: ( )NFPA 13 Residential ( )NFPA 13R (X)NFPA 13D Y Number of Sprinklers Flowing: ( ) 1 (X)2 ( ) 4 ( ) S ( )Other T ( )Specific Ruling Made by Date E _ M Listed Flow at Start Point - 13 Gpm System Type Listed Pres. at Start Point - 7.04 Psi (X) Wet ( ) Dry D MAXIMUM LISTED SPACING 16 x 16 ( ) Deluge ( ) PreAction E Domestic Flow Added - 5 Gpm Sprinkler or Nozzle S Additional Flow Added - Gpm Make SENJU Model RC-RES I Elevation at Highest Outlet - 119 Feet Size 7/16 K-Factor 4.9 G Note: Temperature Rating 162 N Calculation Gpm Required 26.0061 Psi Required 83.23 At Ref Pt STR Summary C-Factor Used: Overhead 150 Underground 150 W Water Flow Test: Pump Data: Tank or Reservoir: A Date of Test - x Rated Cap. Cap. T Time of Test - x @ Psi Elev. E Static (Psi) - 105 Elev. R Residual (Psi) - 100 Other Well Flow (Gpm) - 300 Proof Flow Gpm S Elevation - 95 P Location: STREET P L Source of Information: CONTRACTOR Y Computer Programs by Hydratec Inc. Route 111 Windham N.H. USA 03087 Water Supply Curve Uponor Page 1 Date City Water Supply: Demand: C1 - Static Pressure : 105 D1 - Elevation : 10.394 C2 - Residual Pressure: 100 D2 - System Flow : 26.006 C2 - Residual Flow : 300 D2 - System Pressure : 87.515 Hose ( Demand ) : 10 D3 - System Demand : 36.006 Safety Margin : 17.386 150 140 130 p120 R 110 . Cl C2 E 100 . - S 90 ® D2 S 80 D3 U 70 R 60 ' E 50 40 30 20 10 q D1 ....... .... ....I.... . . . . . . . . . . . . . , . . . 50 100 150 200 250 300 350 400 450 FLOW ( NA1.85 ) Computer Programs by Hydratec Inc. Revision: 50.54.4 Fittings Used Summary Uponor Page 2 Date Fitting Legend Abbrev. Name % ' 1 1% 1% 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 G NFPA 13 Gate Valve 1 1 1 1 1 1 1 1 1 2 2 3 4 5 6 7 8 10 11 13 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 Ucp* Aquapex Coupling 1 2 2 2 2 3 0 0 0 0 0 0 0 0 0 0 0 0 0 0 Uel* Aquapex 90 Elbow 11 11 12 11 13 18 0 0 0 0 0 0 0 0 0 0 0 0 0 0 Utb* Aquapex Tee-Branch 2 17 14 9 12 17 0 0 0 0 0 0 0 0 0 0 0 0 0 0 Utr* Aquapex Tee-Run 1 2 2 4 2 1 0 0 0 0 0 0 0 0 0 0 0 0 0 0 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. Revision: 50.54.4 Flow Summary - NFPA Uponor Page 3 Date SUPPLY ANALYSIS Node at Static Residual Available Source Pressure Pressure Flow Pressure Total Demand Required Pressure STR 105.0 100 300.0 104.901 36.01 87.515 i NODE ANALYSIS Pressure Discharge Node Tag Elevation Node Type at Node at Node Notes H.1 119.0 4.9 7.04 13.0 0.05 256 T.22 119.0 11.95 T.21 119.0 13.24 T.38 109.0 17.86 T.39 109.0 19.09 H.14 109.0 19.22 T.42 109.0 19.77 H.17 109.0 20.02 T.37 109.0 20.92 H.13 109.0 21.09 H.16 109.0 21.55 T.44 109.0 23.13 T.48 109.0 23.26 T.51 109.0 23.87 T.52 109.0 24.15 S.1 109.0 26.81 PRV 95.0 40.13 SMTR 95.0 54.4 TEE 95.0 61.8 10.0 MTR 95.0 73.94 CRB 95.0 83.21 STR 95.0 87.51 H.5 119.0 4.9 7.04 13.0 0.05 256 H.8 119.0 9.9 T.30 119.0 11.33 T.31 119.0 12.83 T.49 109.0 17.51 T.50 109.0 19.18 H.18 109.0 19.66 T.47 109.0 20.52 T.46 109.0 20.82 T.45 109.0 21.21 H.9 119.0 12.75 H.10 119.0 14.3 T.34 119.0 15.08 T.33 119.0 18.14 T.23 119.0 12.45 H.2 119.0 13.21 T.26 119.0 14.47 H.6 119.0 14.77 H.7 119.0 14.84 T.32 119.0 15.06 Computer Programs by Hydratec Inc. Revision: 50.54.4 Flow Summary - NFPA Uponor Page 4 _ Date NODE ANALYSIS(cont.) Pressure Discharge Node Tag Elevation Node Type at Node at Node Notes H.4 119.0 15.15 T.28 119.0 15.21 T.29 119.0 17.67 H.3 119.0 14.69 T.27 119.0 14.91 H.15 109.0 19.13 H.19 109.0 19.15 H.11 119.0 15.06 H.12 119.0 15.07 H.20 109.0 20.67 Computer Programs by Hydratec Inc. Revision: 50.54.4 Final Calculations : Hazen-Williams Uponor Page 5 Date Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftngs Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqiv Len Total Pf/Ft Pf *REMOTE HEAD TO SUPPLY H.1 119 4.90 12.69 0.75 Utr 2.0 13.000 150 7.040 to 2.000 0.0 T.22 119 12.69 0.671 15.000 0.3271 4.907 Vel = 11.51 T.22 119 -7.58 0.75 Utb 17.0 2.260 150 11.947 to Ucp 2.0 19.000 0.0 T.21 119 5.11 0.671 21.260 0.0609 1.294 Vel = 4.64 T.21 119 0.0 1 15.842 150 13.241 to 4.331 T.38 109 5.11 0.862 15.842 0.0179 0.284 Vel = 2.81 T.38 109 0.0 0.75 Utb 17.0 1.273 150 17.856 to Ucp 2.0 19.000 0.0 T.39 109 5.11 0.671 20.273 0.0609 1.234 Vel = 4.64 T.39 109 -0.90 0.75 Utr 2.0 1.000 150 19.090 to 2.000 0.0 H.14 109 4.21 0.671 3.000 0.0423 0.127 Vel = 3.82 H.14 109 0.0 0.75 Utr 2.0 11.000 150 19.217 to 2.000 0.0 T.42 109 4.21 0.671 13.000 0.0425 0.552 Vel = 3.82 T.42 109 0.0 0.75 6.000 150 19.769 to 0.0 H.17 109 4.21 0.671 6.000 0.0425 0.255 Vel = 3.82 H.17 109 0.0 0.75 Utr 2.0 19.000 150 20.024 to 2.000 0.0 T.37 109 4.21 0.671 21.000 0.0425 0.893 Vel = 3.82 T.37 109 0.0 0.75 Utr 2.0 2.000 150 20.917 to 2.000 0.0 H.13 109 4.21 0.671 4.000 0.0425 0.170 Vel = 3.82 H.13 109 0.0 0.75 Utr 2.0 9.000 150 21.087 to 2.000 0.0 H.16 109 4.21 0.671 11.000 0.0425 0.467 Vel = 3.82 H.16 109 0.0 0.75 Utb 17.0 20.000 150 21.554 to 17.000 0.0 T.44 109 4.21 0.671 37.000 0.0425 1.572 Vel = 3.82 T.44 109 6.54 1.25 Utr 4.0 1.000 150 23.126 to 4.000 0.0 T.48 109 10.75 1.054 5.000 0.0266 0.133 Vel = 3.95 T.48 109 7.11 1.25 Utr 4.0 5.000 150 23.259 to 4.000 0.0 T.51 109 17.86 1.054 9.000 0.0683 0.615 Vel = 6.57 T.51 109 8.15 1.25 2.000 150 23.874 to 0.0 T.52 109 26.01 1.054 2.000 0.1365 0.273 Vel = 9.56 T.52 109 0.0 1.25 Uel 11.0 6.000 150 24.147 to T 2.44 13.440 0.0 S.1 109 26.01 1.054 19.440 0.1368 2.659 Vel = 9.56 S.1 109 0.0 1.25 E 1.22 8.000 150 26.806 to 1.220 12.063 ** Fixed Loss =6 PRV 95 26.01 1.054 9.220 0.1369 1.262 Vel = 9.56 Computer Programs by Hydratec Inc. Revision: 50.54.4 4 Final Calculations : Hazen-Williams Uponor Page 6 Date Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftngs Pe ******* Notes *****" Node2 Elev2 Fact Qt Act Eqiv Len Total Pf/Ft Pf PRV 95 0.0 1.25 2.000 150 40.131 to 14.000 ** Fixed Loss = 14 SMTR 95 26.01 1.054 2.000 0.1365 0.273 Vel = 9.56 SMTR 95 0.0 1.25 E 1.22 50.000 150 54.404 to G 0.407 4.067 0.0 TEE 95 26.01 1.054 T 2.44 54.067 0.1368 7.396 Vel = 9.56 TEE 95 H10 10.00 1.5 T 3.443 50.000 150 61.800 to E 1.721 5.164 6.000 ** Fixed Loss =6 MTR 95 36.01 1.244 55.164 0.1114 6.145 Vel = 9.51 MTR 95 0.0 1 25.000 150 73.945 to 1.000 **Fixed Loss = 1 CRB 95 36.01 0.995 25.000 0.3306 8.264 Vel = 14.86 CRB 95 0.0 1 10.000 150 83.209 to 1.000 ** Fixed Loss = 1 STR 95 36.01 0.995 10.000 0.3306 3.306 Vel = 14.86 0.0 STR 36.01 87.515 K Factor= 3.85 *NEW PATH H.1 119 0.31 0.75 Utr 2.0 10.000 150 7.040 to 2.000 0.0 H.5 119 0.31 0.671 12.000 0.0003 0.004 Vel = 0.28 H.5 119 4.90 13.00 0.75 Utr 2.0 6.000 150 7.044 to 2.000 0.0 H.8 119 13.31 0.671 8.000 0.3575 2.860 Vel = 12.08 H.8 119 0.0 0.75 Utr 2.0 2.000 150 9.904 to 2.000 0.0 T.30 119 13.31 0.671 4.000 0.3572 1.429 Vel = 12.08 T.30 119 -7.67 0.75 Ucp 2.0 1.479 150 11.333 to Utb 17.0 19.000 0.0 T.31 119 5.64 0.671 20.479 0.0729 1.493 Vel = 5.12 T.31 119 0.0 1 16.158 150 12.826 to 4.331 T.49 109 5.64 0.862 16.158 0.0215 0.348 Vel = 3.10 T.49 109 0.0 0.75 Utb 17.0 3.979 150 17.505 to Ucp 2.0 19.000 0.0 T.50 109 5.64 0.671 22.979 0.0729 1.675 Vel = 5.12 T.50 109 0.90 0.75 5.000 150 19.180 to 0.0 H.18 109 6.54 0.671 5.000 0.0960 0.480 Vel = 5.93 H.18 109 0.0 0.75 Utr 2.0 7.000 150 19.660 to 2.000 0.0 T.47 109 6.54 0.671 9.000 0.0959 0.863 Vel = 5.93 T.47 109 -1.46 0.75 Utr 2.0 3.000 150 20.523 to 2.000 0.0 T.46 109 5.08 0.671 5.000 0.0602 0.301 Vel = 4.61 T.46 109 1.46 0.75 Utr 2.0 2.000 150 20.824 to 2.000 0.0 T.45 109 6.54 0.671 4.000 0.0958 0.383 Vel = 5.93 Computer Programs by Hydratec Inc. Revision: 50.54.4 Final Calculations : Hazen-Williams • Uponor Page 7 Date Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftngs Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqiv Len Total Pf/Ft Pf T.45 109 0.0 0.75 Utr 2.0 1.000 150 21.207 to Utb 17.0 19.000 0.0 T.44 109 6.54 0.671 20.000 0.0960 1.919 Vel = 5.93 0.0 T.44 6.54 23.126 K Factor= 1.36 *NEW PATH T.30 119 7.68 0.75 Utr 2.0 9.000 150 11.333 to 2.000 0.0 H.9 119 7.68 0.671 11.000 0.1291 1.420 Vel = 6.97 H.9 119 0.0 0.75 Utr 2.0 10.000 150 12.753 to 2.000 0.0 H.10 119 7.68 0.671 12.000 0.1291 1.549 Vel = 6.97 H.10 119 0.0 0.75 Utr 2.0 4.000 150 14.302 to 2.000 0.0 T.34 119 7.68 0.671 6.000 0.1290 0.774 Vel = 6.97 T.34 119 0.47 0.75 Utb 17.0 2.258 150 15.076 to Ucp 2.0 19.000 0.0 T.33 119 8.15 0.671 21.258 0.1440 3.062 Vel = 7.39 T.33 119 0.0 1 Utb 17.0 19.018 150 18.138 to 14.000 4.331 T.51 109 8.15 0.862 33.018 0.0426 1.405 Vel = 4.48 0.0 T.51 8.15 23.874 K Factor= 1.67 *NEW PATH T.22 119 7.58 0.75 Utr 2.0 2.000 150 11.947 to 2.000 0.0 T.23 119 7.58 0.671 4.000 0.1262 0.505 Vel = 6.88 T.23 119 0.0 0.75 Utr 2.0 4.000 150 12.452 to 2.000 0.0 H.2 119 7.58 0.671 6.000 0.1260 0.756 Vel = 6.88 H.2 119 0.0 0.75 Utr 2.0 8.000 150 13.208 to 2.000 0.0 T.26 119 7.58 0.671 10.000 0.1261 1.261 Vel = 6.88 T.26 119 -5.69 0.75 Utb 17.0 12.000 150 14.469 to Utr 2.0 19.000 0.0 H.6 119 1.89 0.671 31.000 0.0097 0.301 Vel = 1.71 H.6 119 0.0 0.75 Utr 2.0 5.000 150 14.770 to 2.000 0.0 H.7 119 1.89 0.671 7.000 0.0096 0.067 Vel = 1.71 H.7 119 0.0 0.75 Utb 17.0 6.000 150 14.837 to 17.000 0.0 T.32 119 1.89 0.671 23.000 0.0097 0.223 Vel = 1.71 T.32 119 -0.47 0.75 Utr 2.0 14.000 150 15.060 to 2.000 0.0 H.4 119 1.42 0.671 16.000 0.0058 0.092 Vel = 1.29 H.4 119 0.0 0.75 Utr 2.0 8.000 150 15.152 to 2.000 0.0 T.28 119 1.42 0.671 10.000 0.0057 0.057 Vel = 1.29 Computer Programs by Hydratec Inc. Revision: 50.54.4 Final Calculations : Hazen-Williams Uponor Page 8 _ Date Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftngs Pe ******* Notes ***"** Node2 EIev2 Fact Qt Act Eqiv Len Total Pf/Ft Pf T.28 119 5.69 0.75 Ucp 2.0 2.990 150 15.209 to Utb 17.0 19.000 0.0 T.29 119 7.11 0.671 21.990 0.1120 2.463 Vel = 6.45 T.29 119 0.0 1 Utb 17.0 24.000 150 17.672 to 14.000 4.331 T.48 109 7.11 0.862 38.000 0.0331 1.256 Vel = 3.91 0.0 T.48 7.11 23.259 K Factor= 1.47 *NEW PATH T.26 119 5.69 0.75 Utr 2.0 1.000 150 14.469 to 2.000 0.0 H.3 119 5.69 0.671 3.000 0.0740 0.222 Vel = 5.16 H.3 119 0.0 0.75 Utr 2.0 1.000 150 14.691 to 2.000 0.0 T.27 119 5.69 0.671 3.000 0.0740 0.222 Vel = 5.16 T.27 119 0.0 0.75 Utr 2.0 2.000 150 14.913 to 2.000 0.0 T.28 119 5.69 0.671 4.000 0.0740 0.296 Vel = 5.16 0.0 T.28 5.69 15.209 K Factor= 1.46 *NEW PATH T.39 109 0.90 0.75 Utr 2.0 13.000 150 19.090 to 2.000 0.0 H.15 109 0.9 0.671 15.000 0.0024 0.036 Vel = 0.82 H.15 109 0.0 0.75 Utr 2.0 9.000 150 19.126 to 2.000 0.0 H.19 109 0.9 0.671 11.000 0.0025 0.028 Vel = 0.82 H.19 109 0.0 0.75 Utr 2.0 9.000 150 19.154 to 2.000 0.0 T.50 109 0.9 0.671 11.000 0.0024 0.026 Vel = 0.82 0.0 T.50 0.90 19.180 K Factor= 0.21 *NEW PATH T.32 119 0.47 0.75 Utr 2.0 3.000 150 15.060 to 2.000 0.0 H.11 119 0.47 0.671 5.000 0.0008 0.004 Vel = 0.43 H.11 119 0.0 0.75 Utr 2.0 10.000 150 15.064 to 2.000 0.0 H.12 119 0.47 0.671 12.000 0.0007 0.009 Vel = 0.43 H.12 119 0.0 0.75 4.000 150 15.073 to 0.0 T.34 119 0.47 0.671 4.000 0.0008 0.003 Vel = 0.43 0.0 T.34 0.47 15.076 K Factor= 0.12 *NEW PATH T.47 109 1.46 0.75 Utb 17.0 7.000 150 20.523 to 17.000 0.0 H.20 109 1.46 0.671 24.000 0.0060 0.145 Vel = 1.32 Computer Programs by Hydratec Inc. Revision: 50.54.4 Final Calculations : Hazen-Williams Uponor Page 9 Date Node1 Elev1 K Qa Nom Fitting Pipe CFact Pt to or Ftngs Pe ******* Notes ****** Node2 Elev2 Fact Qt Act Eqiv Len Total Pf/Ft Pf H.20 109 0.0 0.75 Utb 17.0 7.000 150 20.668 to Utr 2.0 19.000 0.0 T.46 109 1.46 0.671 26.000 0.0060 0.156 Vet = 1.32 _ 0.0 T.46 1.46 20.824 K Factor= 0.32 , Computer Programs by Hydratec Inc. Revision: 50.54.4