*See Pipe Specific Tables on pages 4, 5, and 6. As the schedule number increases, the wall thickness increases, and the actual bore is reduced.

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The pump and the tube size or diameter are the 2 elements that typically can be changed.

Sample size for one sample and two samples. We begin with some results that we shall use when making friction loss calculations for steady, fully developed, incompressible, Newtonian flow through a straight circular pipe. endstream endobj startxref endstream endobj 317 0 obj<> endobj 318 0 obj<> endobj 319 0 obj<>/ProcSet[/PDF/Text]/ExtGState<>>> endobj 320 0 obj<> endobj 321 0 obj<> endobj 322 0 obj<> endobj 323 0 obj<> endobj 324 0 obj<> endobj 325 0 obj<> endobj 326 0 obj<>stream h�b```f``�c`b`��f`@ 0�hfh��|����'K�Es�t���J �">�5������A �-8::J�F0N��Y��lh\$?C��ӆE�-\$0\�����e`�NҌ@��L�L>�4@� .X �kP�������4F+Uop3Q����L�L��Ǝ��ƚ%1����1 32 SAMPLE SIZE n = number per group (two samples) 0 50 100 150 0 25 50 75 n = number in group (one sample) 2.0 0.9 0.7 0.5 0.4 0.9 0.6 0.5 0.4 0.95 0.9 0.8 0.7 0.6 0.5 Power: PSfrag replacements j j jˆj Fig. There are eleven Schedules ranging from the lowest at 5 through 10, 20, 30, 40, 60, 80, 100, 120, 140 to schedule No. L�� H��WMo#7���QSt���c�4�-Z @\��ۃ7�M\\$�a;mw}II�? *See Pipe Specific Tables on pages 4, 5, and 6. The bigger the pipe the easier it is to increase the flow rate within reason. Report DMCA, Standards and wall thickness There are a number of piping standards in existence around the world, but arguably the most global are those derived by the American Petroleum Institute (API), where pipes are categorised in schedule numbers. 316 14 316 0 obj <> endobj piping Much more than documents. Pipe Flow Calculations . 51 0 obj <>/Filter/FlateDecode/ID[<17B5E1A64B1E178ED97884CB98F388DD>]/Index[44 18]/Info 43 0 R/Length 57/Prev 108844/Root 45 0 R/Size 62/Type/XRef/W[1 2 1]>>stream From this point, read left and stop at the first pipe size selection line. "�@�X[�'-�QR)|���n��a3�h�ӻɅ�ju3�cr�!����.�7����j�/�7-+���g?��C\�N+ �th# d�͢i�X�dډ���~��� ����b����o�1'�/GW��v����]�,�Ċ[�_6��9���⁜,3��k̤Ԇ٥����\�9*GW2�j'�lZ���c�����|�������}��h�ĨNܽ��Qb��U1��u2���/�g\��h�l)%Jl_���O����D�j�LI&�}��Ef��,��kE_��E�LNKmԴ�����ծ���E�4e����x��6xC.�Sm�dD��! Regardless of schedule number, pipes of a particular size all have the same outside diameter (not withstanding manufacturing tolerances).

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0000001612 00000 n Formula, Units, Designation Formula Designation SI - Unit B Operating point - D Impeller diameter mm DN or d Nominal width of the pipe or pump port mm g Acceleration of the fall = 9.81 m/s2 m/s2 H Flow head m H A Flow head of the system m H geo Geodetic flow head m H s,geo Geodetic suction head m H d,geo Geodetic pressure head m H Pipe ID = [Pipe O.D. GAS PIPE LINE CALCULATION SIZING USING CPC PIPE SIZING TABLE (NATURAL GAS) This handout will guide you thru the basic, most common method for sizing a natural gas m Part 2 – Pipe (cont.) 0000001350 00000 n In larger and more complex buildings, or with supply pipes that are very long, it is neces-sary to use a recognized method of calculation such as that shown in sections 5.1 and 5.2.

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