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� � � �STP I�on-levet Pressure Distributicrn . ' <br /> M171J1E!50Id�OEIU�IOtI �.TtiIVj:CtSzT�` . <br /> Cantrol Agency <br /> QE'Sl�n WOt`�CS�t@�� c�� ;��t�;tvFsc�-z:a <br /> Laterai 4 GPM=L�g#h of LaYersl X Galtona Per Minute Per Foot(Line 8) <br /> 30 ft X 0.30 GPMlFt= 9.0 GPM <br /> Number of Perforatiau=GPM/Ftow Rate far lateral a(Line 6.4) Lheck Tabte to ensure the maximum number of perforatio�as fs nat <br /> exteeded. <br /> 9.0 + 0.80 = 14 Perforations ��Type of Manifold Cunnection(End ar Center): <br /> Spadng={Length of Laterat)!(Number o€Perforatians-1) 0 E"d �rxrne� <br /> {t�l ) � d y� Perforations-1} _ 2.9 fE = 34.9 ind�es <br /> lateral5 GPM=�Length of Latera(X Gallons Per Minuke Per Foot(line 8} <br /> �� ft?( 0.3fl GPMlFt= 4.Q GPM <br /> N�anber of Perforallons g GPM/Fiow Rate for t.aterai 5(Line b.5) ���Tabie to enswe the maxsmum number of perforations is not <br /> exceeded. <br /> 9.0 4 0.80 = 11 Perforatiotts �(�7ype of Ma�ifotd tonnectior�(Ersd ar Ge�ter): <br /> Spacing=(Length of Laterat)/(Nt�rnber ot Perforations-1) <br /> C7 era ❑cencer <br /> { 3D ) � ( 11 PerForations-9) = 2.g it = 34.9 ���� <br /> Laterat 5 GPM=Length af Lateral X Ga11o�Per Minute Per Foat{tirie 8) <br /> 3U ft X fl.3�D GPM/Ft= 9A GPM <br /> Number of Perforattons=GPMIFIow ftate for laterat 6(Lir�S.b} ��7able ta ensure the maximum nnmber of�erforations is aot <br /> exteedeti. <br /> 9.0 . 0.80 = 14 Perforations ��t Type af Manifotd Connectian(End or Genter): <br /> Spacir�m{Length�f Lateral)/(Num4er of Perfprations-1) �E"� �� <br /> ! 30 ? _ ( 11 Perforations-7) = 2.4 1t = 34.4 i�� <br /> 10. Latculate 7otat GPM fpr system-Lhe t4i.�!GPM need from 4he pump. <br /> Laterai 1 fiow+taterat 2 Fiow+Laterai 3 Ftow+Laterai 4 Ftow+�.yterat 5 Flow�•l.ateral 6 Ftow <br /> 9A + 9.Q + 9.0 + 9.0 + 9.0 + 9.0 .. �A•2 Total GPM <br /> i 1. 5ummary <br /> Entef the minimum ptpe size that atiows for even d9stributiore a�the vdune of tiquid in the pipe from `lotume o€Lic�uid in <br /> the table. '�'►� <br /> Total Voiixne Pipe L.iquid <br /> Pipe Vot�xne Pipe Length to FiFI Pipe Perforatia� Diam�ter Aer Faot. <br /> pipe S9ze{irsl (gaVit) ift) t8�al) Size(in) Spaci (ft) (�ncfies) (Gallons) <br /> ft 9n 1 0.045 <br /> Caterat 1 1.5 0.110 30 3.3 7/32 2.0 24,0 itighest 1•75 a•O7$ <br /> I.aaterat 2 1.5 0.110 30 3.3 7/32 2.0 24A �•� q•��� <br /> 2 O.f70 <br /> taterat3 �,5 0.11U 3A 3.3 7J32 2.0 2g,0 3 a,380 <br /> iaterat4 1.5 0.11U 30 3.3 7I32 2.9 34.9 g 0,661 <br /> �aterat 5 1.5 0.110 30 3.3 7J32 2.9 34.9 <br /> taterat s 1.5 0.t 10 30 3.3 7/32 2.9 34.9 �owest <br /> Totat Yatur�vf Distribution Qiping m 19.8 <br /> Min.Detivered Dase Votum�=Fo�X the Tota{Yoiume of PipSng� 79.Z <br /> Commentsl5peciat Design Considerations: <br /> instal!gate vatve and squirt height test in each Mound unit for fine tc�ing distribution and future adJ+tstments if eve�needed. <br />