6.CS_Imp123456789101112131415161723Pipe Thickness [mm],
according ASME B36.10M45ASME B36.10M SCHEDULE /
IDENTIFICATIONApplicationDn
=10in6Sizedext5102030406080100120140160STDXSXXS(with input
validation)SCH
=XXS-71/221.31.652.11-2.412.77-3.73-0-4.782.773.737.47di
=Pipe_Imp_CS_Dint_dn_schN/Amm83/426.71.652.11-2.412.87-3.91-0-5.562.873.917.82de
=Pipe_Imp_CS_Dext_dn406.4mm9133.41.652.77-2.93.38-4.55-0-6.353.384.559.09s
=Pipe_Imp_CS_Thickness_dn_schN/Amm101
1/442.21.652.772.973.564.856.353.564.859.7111
1/248.31.652.77-3.183.68-5.08-0-7.143.685.0810.1512260.31.652.77-3.183.91-5.54-0-8.743.915.5411.07ApplicationDn
=16in132
1/2732.113.054.785.167.019.535.167.0114.0214388.92.113.05-4.785.49-7.62-0-11.135.497.6215.24(without
input validation)SCH =81153
1/2101.62.113.054.785.748.085.748.08164114.32.113.05-4.786.02-8.56-11.13-13.496.028.5617.12di
=Pipe_Imp_CS_Dint_dn_schN/Amm175141.32.773.4--6.55-9.53-12.7-15.886.559.5319.05de
=Pipe_Imp_CS_Dext_dn559mm186168.32.773.4--7.11-10.97-14.27-18.267.1110.9721.95s
=Pipe_Imp_CS_Thickness_dn_schN/Amm198219.12.773.766.357.048.1810.3112.715.0918.2620.6223.018.1812.722.23The
shedule entered is
wrong20102733.44.196.357.89.2712.715.0918.2621.4425.428.589.2712.725.42112323.83.964.576.358.3810.3114.2717.4821.4425.428.5833.329.5312.725.42214355.63.966.357.929.5311.1315.0919.0523.8327.7931.7535.719.5312.7-2316406.44.196.357.929.5312.716.6621.4426.1930.9636.5340.499.5312.7-24184574.196.357.9211.1314.2719.0523.8329.3634.9339.6745.249.5312.7-25205084.786.359.5312.715.0920.6226.1932.5438.144.4550.019.5312.7-26225594.786.359.5312.7-22.2328.5834.9341.2847.6353.989.5312.7-27246105.546.359.5314.2717.4824.6130.9638.8946.0252.3759.549.5312.7-2826660-7.9212.715.88-------9.5312.7-2928711-7.9212.7--------9.5312.7-30307626.357.9212.715.88-------9.5312.7-3132813-7.9212.715.8817.48------9.5312.7-3234864-7.9212.715.8817.48------9.5312.7-3336914-7.9212.715.8819.05------9.5312.7-3438965-----------9.5312.7-35401016-----------9.5312.7-36421067-----------9.5312.7-441118-----------9.5312.7-461168-----------9.5312.7-39481219-----------9.5312.7-Carbon
steel pipesdnSc -in1/253/4101201
1/2302403604805100612081401016012STD14XS16XXS18202224262830323436384042444648
7.SS_ImpNOMINAL SIZENOMINAL O.D5S10S40S80Smmdi [mm]di [mm]di
[mm]di [mm]Stainless Steel Pipe Schedule ANSI B36.10dndeInternal
diameter [mm]ApplicationDn =4in1/810.29-7.816.835.47(with input
validation)SCH =40S1/413.72-10.429.247.68di
=Pipe_Imp_SS_Dint_Dn_SCHmm3/817.15-13.8512.5310.75de
=Pipe_Imp_SS_Dext_Dnmm1/221.3418.0417.1215.8013.88s
=Pipe_Imp_SS_Thickness_Dn_SCHmm3/426.6723.3722.4520.9318.85133.4030.1027.8626.6424.301
1/442.1638.8636.6235.0432.46ApplicationDn =1.5in1
1/248.2644.9642.7240.9038.10(without input validation)SCH
=5S260.3357.0354.7952.5149.25di =Pipe_Imp_SS_Dint_Dn_SCHmm2
1/273.0368.8166.9362.7159.01de
=Pipe_Imp_SS_Dext_Dnmm388.9084.6882.8077.9273.66s
=Pipe_Imp_SS_Thickness_Dn_SCHmm3 1/2101.6097.3895.5090.1285.44The
nominal diameter entered is
wrong4114.30110.08108.20102.2697.185141.30135.76134.50128.20122.246168.28162.74161.48154.06146.34208219.08213.54211.56202.72193.685S10273.05266.25264.67254.51247.6512323.85315.93314.71304.79298.4514355.60347.68346.04--16406.40398.02396.84--18457.20448.82447.64--20508.00498.44496.91--22558.80549.24547.72--24609.60598.52596.90--30762.00749.30746.16--dnSchin-1/85S1/410S3/840S1/280S3/411
1/41 1/222 1/233 1/24568101214161820222430
Note 1
1.CS610.31.732.41----1.73-2.41----813.72.243.02----2.24-3.02----ApplicationDn
=900mm1017.12.313.2----2.31-3.2----(with input validation)SCH
=401521.32.773.737.47---2.77-3.73---4.78di =Pipe_CS_Dint_dn_sch
=mm2026.72.873.917.82---2.87-3.91---5.56de =Pipe_CS_Dext_dn
=mm2533.43.384.559.09---3.38-4.55---6.35s =Pipe_CS_Thickness_dn_sch
=mm3242.23.564.859.7---3.56-4.85---6.354048.33.685.0810.15---3.68-5.08---7.145060.33.915.5411.07---3.91-5.54---8.7465735.167.0114.02---5.16-7.01---9.53ApplicationDn
=350mm8088.95.497.6215.24---5.49-7.62---11.13(without input
validation)SCH =4090101.65.748.08----5.74-8.08----di
=Pipe_CS_Dint_dn_sch
=333.34mm100114.36.028.5617.12---6.02-8.56-11.13-13.49de
=Pipe_CS_Dext_dn
=355.6mm125141.36.559.5319.05---6.55-9.53-12.7-15.88s
=Pipe_CS_Thickness_dn_sch
=11.13mm150168.37.1110.9721.95---7.11-10.97-14.27-18.26The shedule
entered is
wrong200219.18.1812.722.23-6.357.048.1810.3112.715.0918.2620.6223.01250273.19.2712.725.4-6.357.89.2712.715.0918.2621.4425.428.58300323.99.5312.725.4-6.358.3810.3114.2717.4821.4425.428.5833.32350355.69.5312.7-6.357.929.5311.1315.0919.0523.8327.7931.7535.71400406.49.5312.7-6.357.929.5312.716.6621.4426.1930.9636.5340.494504579.5312.7-6.357.9211.1314.2719.0523.8329.3634.9339.6745.245005089.5312.7-6.359.5312.715.0920.6226.1932.5438.144.4550.015505599.5312.7-6.359.5312.7-22.2328.5834.9341.2847.6353.986006109.5312.7-6.359.5314.2717.4824.6130.9638.8946.0252.3759.546506609.5312.7-7.9212.7--------7007119.5312.7-7.9212.715.88-------7507629.5312.7-7.9212.715.88-------8008139.5312.7-7.9212.715.8817.48------8508649.5312.7-7.9212.715.8817.48------9009149.5312.7-7.9212.715.8819.05------105010679.5312.7-----------STDExStrXxStr102030406080100120140160AC6STD8ExStr10XxStr1510202025303240406050806510080120901401001601251502002503003504004505005506006507007508008509001050
ResumeRev. cjc. 30.01.2014Channel. 0.- Channels and pipes with
frictional and singular pressure drop1.- Pressure loss calculation
routine, for water2.- Pressure loss calculation routine, for
slurry3.- Weir method for slurry pump selection for A-type
fluids(Application of Warman's theory)4.- Circular Semicircular
& Rectangular channels. Array & single functions. Variable
Manning's coefficient.5.- Circular Semicircular & Rectangular
channels. Array & single functions. Variable Manning's
coefficient (Channel 5).6.- Pressure loss coefficients for Valves
and Fittings7.- Widening and narrowing fittingsRef.Note for fluids
type A (according to Weir)- In the standard method (sheet 2) the
pressure head is calculated using the same method as used for the
water (sheet 1), but utilizing the properties of the pulprather
than the properties of water.- The method of Weir (sheet 3)
calculates the pressure drop as if the fluid was water and adding a
pressure differential correction to account for the properties
ofthe slurry. Larger values of correction, correspond to cases
where the flow velocity is close to the limit deposition
velocity.In this case, the flow and pressure head will have their
lowest values, and therefore the power requirement is the
minimumWeir and standrd methodThe comparison of the two methods for
the calculation of pulp line pressures, has been made based on a
particular case. This, therefore, does not allow general
conclusions .For the studied case , there is a good agreement
between the two results , being the Weir method some 3% higher than
the standard method . While recognizing theimpossibility of
obtaining a general conclusion, one might assume, that both methods
are applicable to other cases.However, the Weir method provides
information regarding its application range. Thus, if the Weir
method is accepted and it is considered that the standard
methodgives similar results, the same range of validity should be
applied to both methods. That is, the applicability of these
methods should be restricted to fluids of " type -A " .According
Weir, the method is valid for :0 % VmaxNotesNote 1. If the pipe
material is not carbon steel with dimensions according ASME B31.3,
the exterior diameter (Eq. 1) and the tickness (Eq. 2)shall be
entered manualy.Note 2. Input dimension of Width and Height for the
case of rectangular channels (Lined dimension).Note 3. For circular
channels "Dim" corresponds to the "diameter" . Thus the ratio
(HtoD)max is the maximum allowable ratio Height to Diameter.For
semicircular and rectangular channels, "Dim" corresponds to the
given channel heigt "Hchannel". Thus the ratio is the maximum
alowableratio H to the given channel height
"(HtoHchannel)max"Matrix functions included in the document
are:ChannelCircularNvar_Prop_HtoDmax_Qm3s_Dm_S_Rabsmm_temp_Cw_Ss_d50MicChanelRectangularNvar_Prop_HtoDmax_Qm3s_Dm_S_Rabsmm_tC_Cw_Ss_d50MicChannelSemiCircularNvar_Prop_HtoHchannelMax_Qm3s_Bm_HchannelM_S_Rabsmm_temp_Cw_Ss_d50MicThese
are a functions for circular, rectangular and semicircular
channels, with variable Manning's coefficient , calculated with Eq.
15In this applications, the property identifying parameter "Prop"
has been set to "Matrix".Thus, the outputs are a matrix and in this
case with "13 elements"Limit deposition velocity is calculated
according JRI [1], using the function shown with Eq. 16Viscosity
ratio is calculated according Thomas, equation (1965) [4], using
the function shown with Eq. 13.For rectangular channels, Max flow
"Qmax" is for the height corresponding to the maximum value of the
ratio Height to Hchannel "(HtoDim)max"In addition to the three
mentioned matrix functions, following single functions are
included:16 single functions for circular channel, with variable
Manning coefficient16 single functions for semicircular channel,
with variable Manning coefficient16 single functions for
rectangular channel, with variable Manning coefficient- For
constant Manning coefficient see: piping-tools.net,
document:Channel. 2.- Three channel types. Three_sizing_options.
Constant_Manning_coefficientChannel. 3.- Channels resume.
Constant_Manning_coefficient
cjc. 11.09.2013If the nominal diameter and/or the schedule are
not standard values for carbon steel pipes according ASME 21.3,
tabulated in sheet "6.CS_Imp", the message "N/A" will appear.
Values for "de" and "s" can be manualy input.cjc. 11.09.2013If
the nominal diameter and/or the schedule are not standard values
for carbon steel pipes according ASME 21.3, tabulated in sheet
"6.CS_Imp", the message "N/A" will appear.
Values for "de" and "s" can be manualy input.Click on the plus
sign (+) to Unhide or in the minus sign (-) to Hide the Equations
and information
6.- Fittings and valvesRev. cjc. 30.01.2014Pressure loss
coefficients for Valves and FittingsNominal diameter in Imperial
UnitsNominal diameter in SI Units1.- Ball valvesK
=Pipe_Valve_Ball_Imp_K_dnK =Pipe_Valve_Ball_SI_K_dndn =6indn
=150mmK =0.05-K =0.05-2.- Butterfly valves Bray 2021K
=Pipe_Valve_Butterfly_Bray2021_Imp_K_dnK
=Pipe_Valve_Butterfly_Bray2021_SI_K_dndn =2indn =150mmK =0.27-K
=0.16-2.- Butterfly valves Bray 3031K
=Pipe_Valve_Butterfly_Bray3031_Imp_K_dnK
=Pipe_Valve_Butterfly_Bray3031_SI_K_dndn =6indn =150mmK =0.35-K
=0.35-3.- Knife valvesK =Pipe_Valve_Knife_Imp_K_dnK
=Pipe_Valve_Knife_SI_K_dndn =2indn =150mmK =41.25-K =0.68-4.- Globe
valvesk =Pipe_Valve_Globe_Imp_K_dnk =Pipe_Valve_Globe_SI_K_dnd
=2ind =150mmk =7.64k =7.535.- Pinch
valvesPipe_Valve_Pinch_Imp_K_dnk =Pipe_Valve_Pinch_SI_K_dnd =2ind
=150mmK =0.31K =0.286.- Diaphragm valvesK
=Pipe_Valve_Diaphragm_Weir_Imp_K_dnK
=Pipe_Valve_Diaphragm_Weir_SI_K_dnWeir typedn =6indn =150mmUnlinedK
=3.29K =3.296.- Diaphragm valvesK
=Pipe_Valve_Diaphragm_Weir_Lined_Imp_K_dnK
=Pipe_Valve_Diaphragm_Weir_Lined_SI_K_dnWeir typedn =6indn
=150mmLinedK =5.14K =5.146.- Diaphragm valvesK
=Pipe_Valve_Diaphragm_Straight_Thru_Imp_K_dnK
=Pipe_Valve_Diaphragm_Straight_Thru_SI_K_dnStraight_Thrudn =6indn
=150mmUnlinedK =0.43K =0.436.- Diaphragm valvesK
=Pipe_Valve_Diaphragm_Straight_Thru_Lined_Imp_K_dnK
=Pipe_Valve_Diaphragm_Straight_Thru_Lined_SI_K_dnStraight_Thrudn
=6indn =150mmLinedK =0.76K =0.767.- Round plug valveK
=Pipe_Valve_Plug_Round_Imp_K_dnK =dn =6indn =6mmK =0.30K =7.-
Rectangular plug valveK =Pipe_Valve_Plug_Rectg_Imp_K_dnK =dn =6indn
=150mmK =0.86K =8.- Check valvesK =Pipe_Valve_Check_Imp_K_dnK
=Pipe_Valve_Check_SI_K_dndn =2indn =50mmK =3.03-K =3.03-9.- Angle
valvesPipe_Valve_Angle_Imp_K_dndn =4inK =14.8410.- Cone valveK
=Pipe_Valve_Cone_Imp_K_dndn =6inK =0.09-11.- StrainersK
=Pipe_Y_strainer_Imp_K_dnK =Pipe_Y_strainer_SI_K_dndn =6indn
=150mmK =2.67-K =2.67-12.- Expansion/ReductionGradual expansion (q
= 30)Expansionb =0.7b =0.7K2_q = 30 =0.729K2_q = 30 =0.729Gradual
reduction (q = 30)Reductionb =0.7b =0.7K2_q = 30 =0.700K2_q = 30
=0.440Gradual expansion (q = 45)Expansionb =0.7b =0.7K2_q = 45
=1.08K2_q = 45 =1.083Gradual reduction (q = 45)Reductionb =0.7b
=0.7K2_q = 45 =0.65K2_q = 45 =0.650
7.- Widening and narrowingRev. cjc. 30.01.20147.- Widening and
narrowing fittings[9]Abrupt and gradual narrowingAbrupt and gradual
wideningIf q
