02/07/2022 document.xls CYCLONE DESIGN AND ANALYSIS by Esco Engineering 179 Lansdowne Avenue, Kingsville, Ontario N9Y 3J2 Canada Revisions ph 519 733 3122 ### Corrected error in cell D14 on efficiency sheets fax 519 733 6094 ### Added diagram Contact: Neil Stone, Chief Engineer 3-Apr-99 Corrected cell O7, Efficiency 1 - thanks to Laercio Frare for pointing out this error e-mail [email protected]2-Dec-99 Added metric option, NV sketch Website www.mnsi.net/~pas/esco.htm ### Corrected error in density calc (size!E9, Efficiency 1! and 2!E19) Copyright 1997 by John Neil Stone. All rights reserved. May be redistributed free of charge, but may not be sold without the author's explicit permission. Provided "as is" without warranty of any kind. HOW TO USE THIS SPREADSHEET NOTE: This spreadsheet is for the use of knowledgeable professionals, capable of evaluating the accuracy of the results. The author is not responsible for the use to which these results are put. 1 The 'Cyclone size' sheet calculates dimensions for various standard cyclones. Enter the flow rate, design inlet velocity and gas density in the colored squares and the sheet will give dimensions for five standard cyclones - two high efficiency, and three low efficiency. The table also gives the predicted pressure drop, but be aware that this is a very uncertain calculation (see original references). See 'Diagram' sheet for nomenclature. On the 'Cyclone size' sheet you specify the units you want to use - metric or US Customary (Imperial) THIS UNITS SELECTION APPLIES TO ALL SHEETS 2 Two methods are provided for calculating cyclone efficiency. You can calculate both, and compare the results on the chart. Both sheets are set up with the same layout, so data can be copied between sheets easily. 3 The efficiency calculation requires particle size data, cyclone dimensions, and physical property data for the gas and the solids. The calculation assumes that the size distribution of the particles is log normally distributed. The sheet is set up so that you can enter either the mean and standard deviation of the log normal distribution, or the particle size data, from which these data are then calculated. 4 Procedure for efficiency calculations: a) Enter the cyclone dimensions in cells D4 to D11. If you have calculated these using this spreadsheet, the values in cells 13 to 20 for the selected cyclone design can be directly copied b) Enter the gas property data in cells D18 to D21. c) Enter the particulate data in cells D26 to D29. If you enter the mean and standard deviation, and select 'N' for cell D28, then the overall efficiency is immediately given in cell H15, and the inlet and outlet size distributions are given in cells O21 to O41 and R21 to R41. d) If you want to use the size distribution method, enter 'Y' in cell D28, and then the range limits starting in cell N50 and the corresponding % in range starting in O50. If you want to use more than nine ranges, you can extend these columns to as many rows as you want - just remember to copy the formulae in columns M and P through T into any rows that you add. After entering the size distribution data, You have to run the regression tool. Choose the 'Tools' menu then 'Data Analysis' then 'Regression'. For the 'X' value pick all the values in column Q, starting in Q50; for the 'Y' values, pick all the values in column T, starting in T50. For the 'Output range' enter V48. You will get a message saying results will overwrite cells - pick OK. Once the regression is done, the results are available, as described in c) above. 5 The chart sheet graphs the penetration (col P = 1 - fractional efficiency) against particle size for the two efficiency from the same data if you want to compare the two efficiency calculations! 6 The spreadsheet is protected in order to prevent accidental overwriting of the formulae. However, there is no password needed to unprotect it, so you can freely adapt it to suit your purposes. into D4 to D11. NOTE: Paste special the values - do not just copy the cells. calculation methods. CAUTION: The two efficiency sheets are not linked, so make sure they are both calculating
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04/07/2023 document.xls
CYCLONE DESIGN AND ANALYSISby Esco Engineering
179 Lansdowne Avenue,Kingsville, Ontario N9Y 3J2 Canada Revisionsph 519 733 3122 ### Corrected error in cell D14 on efficiency sheetsfax 519 733 6094 18-Jan-99 Added diagramContact: Neil Stone, Chief Engineer 3-Apr-99 Corrected cell O7, Efficiency 1 - thanks to Laercio Frare for pointing out this errore-mail [email protected] 2-Dec-99 Added metric option, NV sketchWebsite www.mnsi.net/~pas/esco.htm ### Corrected error in density calc (size!E9, Efficiency 1! and 2!E19)
Copyright 1997 by John Neil Stone. All rights reserved.May be redistributed free of charge, but may not be sold without the author's explicit permission.Provided "as is" without warranty of any kind.
HOW TO USE THIS SPREADSHEET
NOTE: This spreadsheet is for the use of knowledgeable professionals, capable of evaluating the accuracy of the results. The author is not responsible for the use to which these results are put.
1 The 'Cyclone size' sheet calculates dimensions for various standard cyclones.Enter the flow rate, design inlet velocity and gas density in the colored squaresand the sheet will give dimensions for five standard cyclones - two high efficiency, andthree low efficiency. The table also gives the predicted pressure drop, but be aware that this is avery uncertain calculation (see original references). See 'Diagram' sheet for nomenclature.On the 'Cyclone size' sheet you specify the units you want to use - metric or US Customary (Imperial)THIS UNITS SELECTION APPLIES TO ALL SHEETS
2 Two methods are provided for calculating cyclone efficiency. You can calculate both, andcompare the results on the chart. Both sheets are set up with the same layout, so data can be copied between sheets easily.
3 The efficiency calculation requires particle size data, cyclone dimensions, and physical propertydata for the gas and the solids. The calculation assumes that the size distribution of the particlesis log normally distributed. The sheet is set up so that you can enter either the mean and standarddeviation of the log normal distribution, or the particle size data, from which these data are then calculated.
4 Procedure for efficiency calculations:a) Enter the cyclone dimensions in cells D4 to D11. If you have calculated these using this
spreadsheet, the values in cells 13 to 20 for the selected cyclone design can be directly copied
b) Enter the gas property data in cells D18 to D21.c) Enter the particulate data in cells D26 to D29. If you enter the mean and standard deviation, and
select 'N' for cell D28, then the overall efficiency is immediately given in cell H15, and the inlet andoutlet size distributions are given in cells O21 to O41 and R21 to R41.
d) If you want to use the size distribution method, enter 'Y' in cell D28, and then the range limits starting in cell N50 and the corresponding % in range starting in O50. If you want to use more than nine ranges, youcan extend these columns to as many rows as you want - just remember to copy the formulaein columns M and P through T into any rows that you add.After entering the size distribution data, You have to run the regression tool. Choose the 'Tools' menuthen 'Data Analysis' then 'Regression'. For the 'X' value pick all the values in column Q, starting in Q50;for the 'Y' values, pick all the values in column T, starting in T50. For the 'Output range' enter V48. You willget a message saying results will overwrite cells - pick OK.Once the regression is done, the results are available, as described in c) above.
5 The chart sheet graphs the penetration (col P = 1 - fractional efficiency) against particle size for the two efficiency
from the same data if you want to compare the two efficiency calculations!
6 The spreadsheet is protected in order to prevent accidental overwriting of the formulae.However, there is no password needed to unprotect it, so you can freely adapt it to suit your purposes.
into D4 to D11. NOTE: Paste special the values - do not just copy the cells.
calculation methods. CAUTION: The two efficiency sheets are not linked, so make sure they are both calculating
04/07/2023 document.xls
DEFINITION OF CYCLONE DIMENSIONS
D
b De
a Sh
H
NV = Neutral vaneExtension of innerside if inlet to centerlineof cyclone
B ELEVATION PLAN
Cyclone size
Page 3
CALCULATE DIMENSIONS FOR CYCLONE NOTES Sheet 1 is for sizingSheets 2/3 are for efficiency (alternates)Sheet 4 are charts of results of sheets 2/3
SPECIFY UNITS (U = US CUSTOMARY[IMPERIAL], M = METRIC) U This setting applies to the whole spreadsheetInput Working
Flow rate Q cfm 2000 2000 cfmDesign inlet vel vi fps 50 50 fpsGas density rg pcf 0.0740 0.074 pcfInlet area 0.67 sfPD parameter 0.56 in water
Dimensions Type of cycloneStairmand Swift Lapple Swift Peterson/Whitby
HE HE LE LE LE
Dia D ft 2.58 2.69 2.31 2.31 2.34Inlet ht a in 15.49 14.18 13.86 13.86 16.40Inlet width b in 6.20 6.77 6.93 6.93 5.85Outlet length S ft 1.29 1.34 1.44 1.39 1.37Outlet dia De in 15.49 12.89 13.86 13.86 14.07Cylinder ht h ft 3.87 3.76 4.62 4.04 3.13Overall ht H ft 10.33 10.48 9.24 8.66 7.43Dust outlet dia B in 11.62 12.89 6.93 11.09 14.07# vel hds Nh 5.14 4.87 4.49 4.69 4.77Press drop, no NV in water 2.85 2.70 2.49 2.60 2.65Press drop, with NV in water 1.34 1.27 1.17 1.22 1.24
Cyclone data from "New design approach boosts cyclone efficiency", W.H.Koch and W.Licht, Chem Eng Nov 7 1977, 80Pressure drop vel head correlation from "A better way to calculate cyclone pressure drop" J.Casal and J.M. Martinez-Benet, Chem Eng, Jan 24, 1983, 99
Cyclone size
Page 4
Sheets 2/3 are for efficiency (alternates)Sheet 4 are charts of results of sheets 2/3
This setting applies to the whole spreadsheet
Copy one col of outlinedata (copy values only)to efficiency sheet.
Cyclone data from "New design approach boosts cyclone efficiency", W.H.Koch and W.Licht, Chem Eng Nov 7 1977, 80Pressure drop vel head correlation from "A better way to calculate cyclone pressure drop" J.Casal and J.M. Martinez-Benet, Chem Eng, Jan 24, 1983, 99
Efficiency 1
Page 5
CALCULATE EFFICIENCY FOR CYCLONE (method 1)CALCULATIONS ARE IN US CUSTOMARY [IMPERIAL] UNITSGeometry Input Working Limits/warningsDia D ft 2.58 2.58Inlet ht a in 15.49 15.49Inlet width b in 6.20 6.20Outlet length S ft 1.29 1.29Oulet dia De in 15.49 15.49Cylinder ht h ft 3.87 3.87Overall ht H ft 10.33 10.33Dust outlet dia B in 11.62 11.62Natural length L ft 6.40 6.40# vel hds Nh 5.14Press drop, no NV in water 2.85Press drop, with NV in water 1.34 Overall efficiency
Gas dataFlow rate Q acfm 2000 2000.00 33.33333 cfsDensity rg pcf 0.0740 0.0740 0.076 air @ 1 atm, spec'd tempViscosity u cP 0.010 0.010 6.72E-06 lb/f-sTemperature T °F 60 60Salt. temp fact fT 1.00 1Salt dens. fact fp 1.00 1
Particle data Value usedLog mean dia dp µm 12 11.905565Log SD sd µm 3 3.1077764Use distribution? (Y/N) y If yes, run regression - adjust input ranges (cols Q,T) to suit dataSpecific gravity 0.8 49.92 pcf
ReferencesEfficiency from "New design approach boosts cyclone efficiency",
W.H.Koch and W.Licht, Chem Eng Nov 7 1977, 80Pressure drop vel head correlation from "A better way to calculate cyclone pressure
drop" J.Casal and J.M. Martinez-Benet, Chem Eng, Jan 24, 1983, 99
MS F Significance F14.59118 27837.76 7.33E-140.000524
t Stat P-value Lower 95%Upper 95%Lower 95.000%Upper 95.000%319.6806 7.74E-16 2.458684 2.495328 2.458684 2.495328166.8465 7.33E-14 1.117837 1.149978 1.117837 1.149978
Efficiency 2
Page 12
CALCULATE EFFICIENCY FOR CYCLONE (method 2)CALCULATIONS ARE IN US CUSTOMARY [IMPERIAL] UNITSGeometry Input Working Limits/warningsDia D ft 3.33 3.33Inlet ht a in 20.00 20.00Inlet width b in 8.00 8.00Outlet length S ft 1.67 1.67Oulet dia De in 20.00 20.00Cylinder ht h ft 5.00 5.00Overall ht H ft 13.33 13.33Dust outlet dia B in 15.00 15.00Natural length L ft 8.26 8.26# vel hds Nh 5.14Press drop, no NV in water 1.03Press drop, with NV in water 0.48 Overall efficiency
Gas dataFlow rate Q acfm 2000 2000.00 33.33333 cfsDensity rg pcf 0.0740 0.0740 0.076 air @ 1 atm, spec'd tempViscosity u cP 0.010 0.010 6.72E-06 lb/f-sTemperature T °F 60 60Salt. temp fact fT 1.00 1Salt dens. fact fp 1.00 1
Particle data Value usedLog mean dia dp um 24 11.905565Log SD sd um 3 3.1077764Use distribution? (Y/N) y If yes, run regression - adjust input ranges (cols Q,T) to suit dataSpecific gravity 5 312 pcfRe-entrainment coeff alpha 0 default = 0 (see original paper for definition)
ReferencesEfficiency from "A new collection theory of cyclone separators",
L.Enliang & W Yingmin, AIChEJ Vol 35, #4 April 1989, 666Pressure drop vel head correlation from "A better way to calculate cyclone pressure
drop" J.Casal and J.M. Martinez-Benet, Chem Eng, Jan 24, 1983, 99
2.101083 1.226669 -1.226669 Multiple R 0.9998741.740188 0.77197 -0.77197 R Square 0.999749
1.28139 0.150652 -0.150652 Adjusted R 0.9997131.489069 0.43948 0.43948 Standard E 0.0228941.794123 0.841457 0.841457 Observatio 91.947881 1.036431 1.0364312.145966 1.281729 1.281729 ANOVA2.648229 1.881213 1.881213 df SS MS F