Programa Isocal Taller (1)
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Transcript of Programa Isocal Taller (1)
Stationary Source Information
Plant Name Ladrillera El Rubí, Tunja
Fuel Type Carbon
Sampling Location Chimenea Horno
Operator Universidad de la SalleDate 15 de Octubre de 2009
Project #
Base Run Number R
# of Ports Available 4
# of Ports Used 4
Port Inside Diameter 0.1
Circular Stack? 1
Rectangular Stack? 1
Test Equipment Information
Meter Box Number Apex 572Meter Calibration Factor (Y) 0.994Orifice Meter Coefficient (DH@) 48.960 mm H2O
Pitot Identification
Pitot Tube Coefficient (Cp) 0.850Orsat Identification
Nozzle Number 30Nozzle Diameter (Dn) 6.200 mm
Probe Number
Probe Length 1.83 m
Liner Material Ac. Inox.Sample Case / Oven Number
Impinger Case Number
Acetone Lot Number
Testing Company Information
Company Name Universidad de la SalleAddress Calle 10 concarrera 2City State Zip Country BogotáPhone Number 3 68 85 96 /97 /98Fax Number 91-2 44 83 80
METHOD 1 - SAMPLE AND VELOCITY TRAVERSES FOR STATIONARY SOURCES
Plant Name Ladrillera El Rubí, Tunja Date 15 de octubre de 2009
Sampling Location Chimenea Horno Project #
Operator Universidad de la Salle # of Ports Available 4
Stack Type Circular # of Ports Used 2
Stack Size Large Port Inside Diameter 0.1
Circular Stack or Duct Diameter
Distance to Far Wall of Stack (Lfw) 2.87 m
Distance to Near Wall of Stack (Lnw) 0.39 m
Diameter of Stack (=Lfw - Lnw) (D) 2.48 m
Area of Stack (=3.14(D/2/Cunits)2) (As) 4.831 m2
Distance from Port to Disturbances
Distance Upstream (A) 8.00 m
Diameters Upstream (=B/D) (A/D) diameters
Distance Downstream (B) 14.00 m
Diameters Downstream (=A/D) (B/D) diameters
Number of Traverse Points Required
Diameters to Minimum Number of1
Flow Disturbance Traverse Points
Up Down Particulate Velocity
Stream Stream Points Points2.00-4.99 0.50-1.24 24 165.00-5.99 1.25-1.49 20 166.00-6.99 1.50-1.74 16 127.00-7.99 1.75-1.99 12 12>= 8.00 >=2.00 8 or 122 8 or 122
Upstream Spec
Downstream Spec
Traverse Pts Required
and Downstream conditions, then use the larger Number. Number of Traverse Points Used
2 Ports by 12 Across
12 for Circular Stacks over 24 inches 24 Pts Used 16 Required0 Particulate 0 Velocity
Traverse Point Locations
Fraction Distance Distance
Traverse of from Including
Point Stack Inside Nipple
Number Diameter Wall Length
m m123456789
101112
1 Check the Minimum Number of Points for the Upstream
2 8 for Circular Stacks 12 to 24 inches
METHOD 1 - SAMPLE AND VELOCITY TRAVERSES FOR STATIONARY SOURCES
15 de octubre de 2009
METHOD 2 - DETERMINATION OF STACK GAS VELOCITY AND VOLUMETRIC FLOW RATE
Plant Name Ladrillera El Rubí, Tunja Date 15 de OCTUBRE de 2009
Sampling Location Chimenea Horno Project #
Operator # of Ports Used 2
Stack Type Circular Pitot Identification
Pitot Leak Check 1 PreTest 0 PostTest Pitot Coefficient (Cp) 0.85
Stack Dimensions Velocity Traverse Data
Diameter or Length of Stack (D) 2.48 m Run Number R-1Width of Stack (W) m Run Time
Area of Stack (As) 4.831 m2 Traverse Velocity Stack Local
Point Head Temp Velocity
Pressures (Dp) (ts) (vs)l
Barometric Pressure (Pb) 542.00 mm Hg mm H2O °C m/sec
Static Pressure (Pstatic) 4.16 mm H2O 1A 1.00 74Absolute Stack Pressure (Ps) 542.31 mm Hg 2A 3.00 75
3A 4.50 75Stack Gas Composition 4A 4.00 77
Composition Data: Actual 1 Estimate 0 5A 5.00 77Carbon Dioxide Concentration (%CO2) % 6A 5.50 75Oxygen Concentration (%O2) % 7A 6.00 75Carbon Monoxide Concentration (%CO) % 8A 6.00 75Nitrogen Concentration (%N2) % 9A 4.00 75Stack Moisture Content (Bws) 10A 2.50 74Stack Dry Molecular Weight (Md) g/g-mole 11A 1.50 74Stack Wet Molecular Weight (Ms) g/g-mole 12A 1.00 74
1B 0.50 63Results 2B 0.50 64
Average Stack Gas Velocity (vs) m/sec 3B 1.00 62Dry Standard Volumetric Flow Rate (Qsd) dscm/hr 4B 1.50 68Dry Standard Volumetric Flow Rate (Qsd) dscm/min 5B 2.00 69
6B 2.50 70Stack Cross Section Schematic 7B 3.00 72
8B 3.50 719B 1.00 7210B 2.00 7211B 1.00 7212B 1.50 71
Average1
Dp, or, (Dp)1/2avg = 1/nS(Dp1/2)
Formulas Used
As = DW/Ku for Rectangular Stacks Ts(avg) = 1/nSts + Tu
As = (p(D/2)2)/Ku for Circular Stacks where Tu = 273 oK for metric units
where Ku = 1 for metric units where Tu = 460 oR for English units
where Ku = 144 (in2/ft2) for English units vs = KpCp(Dp)1/2avg (Ts(avg)/(PsMs))1/2
Ps = Pbar + Pstatic/13.6 where Kp = 34.97 for metric units
%N2 = 100 - %CO2 - %O2 - %CO where Kp = 85.49 for English units
Md = .44(%CO2) + .32(%O2 ) + .28(%N2 + %CO) Qsd = 3600(1 - Bws)vsAs(Tstd/Ts(avg))(Ps/Pstd)
Ms = Md(1 - Bws) + 18Bws where Tstd = 293 oK, Pstd = 760 mm Hg, for metric units
(Dp)1/2avg = 1/nS(Dp1/2) where Tstd = 528 oR, Pstd = 29.92 in Hg, for English units
1 Please report the average of the square roots of
METHOD 3 - GAS ANALYSIS FOR THE DETERMINATION OF DRY MOLECULAR WEIGHT
Plant Name Ladrillera El Rubí, Tunja Date 15 de octubre de 2009
Sampling Location Chimenea Horno Project #
Operator # of Ports Used 4
Fuel Type Carbon Minimum Fuel Factor Maximum Fuel Factor
Orsat Leak Check 1 PreTest 0 PostTest Orsat Identification
Gas Analysis Data
Run Number R-1 Run Start Time 15:35 Run Stop Time 18:00Sample Carbon Carbon Carbon Carbon Dry Molecular
Analysis Dioxide Oxygen Monoxide Dioxide Oxygen Monoxide Nitrogen Molecular Weight
Time Volume Volume Volume Concentra. Concentra. Concentra. Concentra. Weight Deviation
(VCO2) (VO2) (VCO) (%CO2) (%O2) (%CO) (%N2) (Md) (DMd)
hh:mm ml ml ml percent percent percent percent g/g-mole g/g-mole4.2 14.0 14.5 0.004.1 13.9 14.4 0.003.9 13.8 14.3 0.00
Results AveragesAverage Calculated Fuel Factor (Fo)avg Molecular Wt Deviation < 0.3? 1Average Excess Air (%EA)avg percent Fuel Factor in Handbook Range? 0
Gas Analysis Data
Run Number R-2 Run Start Time Run Stop Time
Sample Carbon Carbon Carbon Carbon Dry Molecular
Analysis Dioxide Oxygen Monoxide Dioxide Oxygen Monoxide Nitrogen Molecular Weight
Time Volume Volume Volume Concentra. Concentra. Concentra. Concentra. Weight Deviation
(VCO2) (VO2) (VCO) (%CO2) (%O2) (%CO) (%N2) (Md) (DMd)
hh:mm ml ml ml percent percent percent percent g/g-mole g/g-mole
Results AveragesAverage Calculated Fuel Factor (Fo)avg Molecular Wt Deviation < 0.3? 0Average Excess Air (%EA)avg percent Fuel Factor in Handbook Range? 0
Gas Analysis Data
Run Number R-3 Run Start Time Run Stop Time
Sample Carbon Carbon Carbon Carbon Dry Molecular
Analysis Dioxide Oxygen Monoxide Dioxide Oxygen Monoxide Nitrogen Molecular Weight
Time Volume Volume Volume Concentra. Concentra. Concentra. Concentra. Weight Deviation
(VCO2) (VO2) (VCO) (%CO2) (%O2) (%CO) (%N2) (Md) (DMd)
hh:mm ml ml ml percent percent percent percent g/g-mole g/g-mole
Results AveragesAverage Calculated Fuel Factor (Fo)avg Molecular Wt Deviation < 0.3? 0Average Excess Air (%EA)avg percent Fuel Factor in Handbook Range? 0
Fuel Factor Fo Formulas Used
Fuel Type Minimum Maximum %CO2 = VCO2
Coal, Anthracite 1.016 1.130 %O2 = VO2 - VCO2
Coal, Lignite 1.016 1.130 %CO = VCO - VO2
Coal, Bituminous 1.083 1.230 %N2 = 100 - %CO2 - %O2 - %CO
Oil, Distillate 1.260 1.413 Md = .44(%CO2)+ .32(%O2 )+ .28(%N2 + %CO)
Oil, Residual 1.210 1.370 DMd = Md - MdavgGas, Natural 1.600 1.836 Fo = (20.9 - %O2 - .5%CO)/(%CO2 + %CO)
Gas, Propane 1.434 1.586 %EA=100(%O2-.5%CO)/(.264%NO2-(%O2-.5%CO))
Gas, Butane 1.405 1.553Wood 1.000 1.120Wood Bark 1.003 1.130
METHOD 4 - DETERMINATION OF MOISTURE CONTENT IN STACK GASES
Plant Name Date 15 de octubre de 2009
Sampling Location Chimenea Horno Project #
Operator # of Ports Used 2
Stack Type Circular Meter Box Number Apex 572
Train Leak Check 1 PreTest 0 PostTest Meter Cal Factor (Y) 1.01
Moisture Content Data
Run Number R-1 Run Start Time Run Stop Time
Total Meter Volume (Vm) 1.269 dcm Barometric Pressure (Pb) 542.00 mm Hg
Avg Meter Temp (tm)avg 23 Stack Static Pressure (Pstatic) 4.16 mm H2O
Avg Stack Temp (ts)avg 72 Avg Orifice Pressure (DH)avg 2.67 mm H2O
Impinger 1 Impinger 2 Impinger 3 Impinger 4 Impinger 5 Impinger 6 Impinger 7
ml ml ml g ml ml g
Contents
Final Value (Vf),(Wf) 113.00 107.00 0.00 107.62Initial Value (Vi),(Wi) 100.00 100.00 0.00 100.00Net Value (Vn),(Wn)
Results
Total Volume (Vt) ml Water Vol Condensed (Vwc(std)) scm
Total Weight (Wt) g Water Vol Weighed (Vwsg(std)) scm
Std Meter Volume (Vm(std)) dscm Sat. Moisture Content (Bws(svp)) %
Calc Moisture Content (Bws(calc)) % Final Moisture Content (Bws) %
Moisture Content Data
Run Number R-2 Run Start Time Run Stop Time
Total Meter Volume (Vm) dcm Barometric Pressure (Pb) 542.00 mm Hg
Avg Meter Temp (tm)avg Stack Static Pressure (Pstatic) 4.16 mm H2O
Avg Stack Temp (ts)avg Avg Orifice Pressure (DH)avg 2.67 mm H2O
Impinger 1 Impinger 2 Impinger 3 Impinger 4 Impinger 5 Impinger 6 Impinger 7
ml ml ml g ml ml ml
Contents
Final Value (Vf),(Wf)
Initial Value (Vi),(Wi)
Net Value (Vn),(Wn)
Results
Total Volume (Vt) 0.00 ml Water Vol Condensed (Vwc(std)) 0.000 scm
Total Weight (Wt) 0.00 g Water Vol Weighed (Vwsg(std)) 0.000 scm
Std Meter Volume (Vm(std)) dscm Sat. Moisture Content (Bws(svp)) %
Calc Moisture Content (Bws) % Final Moisture Content (Bws) %
Moisture Content Data
Run Number R-3 Run Start Time Run Stop Time
Total Meter Volume (Vm) dcm Barometric Pressure (Pb) 542.00 mm Hg
Avg Meter Temp (tm)avg Stack Static Pressure (Pstatic) 4.15 mm H2O
Avg Stack Temp (ts)avg Avg Orifice Pressure (DH)avg mm H2O
Impinger 1 Impinger 2 Impinger 3 Impinger 4 Impinger 5 Impinger 6 Impinger 7
ml ml ml g ml ml ml
Contents
Final Value (Vf),(Wf)
Initial Value (Vi),(Wi)
Net Value (Vn),(Wn)
Results
Total Volume (Vt) 0.00 ml Water Vol Condensed (Vwc(std)) 0.000 scm
Total Weight (Wt) 0.00 g Water Vol Weighed (Vwsg(std)) 0.000 scm
Std Meter Volume (Vm(std)) dscm Sat. Moisture Content (Bws(svp)) %
Calc Moisture Content (Bws) % Final Moisture Content (Bws) %
oC
oC
oC
oC
oC
oC
ISOKINETIC SAMPLING DATA
Plant Name Ladrillera El Rubí, Tunja
Sampling Location Chimenea Horno
Operator
# of Points Across 12
Slide Rule Set-Up
Pitot Tube Coefficient (Cp) 0.850Avg Stack Temp (ts) 72Avg Gas Meter Temp (tm) 24DH @ 0.75 SCFM (DH@) 49.78 mm H2O
Avg Pitot Tube Diff. Pressure (Dpavg) 9.62 mm H2O
Stack Moisture Content (Bws) 5.0 %
Stack Dry Molecular Weight (Mds) 28.94 g/g-mole
Estimated Orifice Flow Rate (Qm) 21.20 acmm
DP to DH Isokinetic Factor (K) 3.30
Pressures
Barometric Pressure (Pb) 542.00 mm Hg
Stack Static Pressure (Pstatic) 4.15 mm H2O
Absolute Stack Pressure (Ps) 542.31 mm Hg
Absolute Meter Pressure (Pm) 545.66 mm Hg
Dry Gas Desired Actual
Traverse Sampling Clock Meter Velocity Orifice Orifice
Point # Time Time Reading Head DH DH(Q) (Vm) (Dp) (DH) (DH)
min hr:min m3 mm H2O mm H2O mm H2O1B 0.0 15:35 21.662 5.50 18.15 18.002B 2.5 21.702 9.00 29.70 30.003B 5.0 21.749 11.50 37.95 38.004B 7.5 21.803 12.00 39.60 39.505B 10.0 21.861 13.00 42.90 43.006B 12.5 21.912 14.50 47.85 48.007B 15.0 21.978 15.00 49.50 49.508B 17.5 22.037 14.50 47.85 48.009B 20.0 22.099 13.00 42.90 43.00
10B 22.5 22.156 11.00 36.30 36.0011B 25.0 22.208 6.00 19.80 20.0012B 27.5 16:10 22.245 4.00 13.20 13.001A 30.0 17:25 22.280 5.00 16.50 16.502A 32.5 22.315 8.50 28.05 28.003A 35.0 22.361 11.00 36.30 36.004A 37.5 22.413 12.50 41.25 41.005A 40.0 22.472 14.50 47.85 48.006A 42.5 22.531 15.00 49.50 49.507A 45.0 22.595 16.00 52.80 53.008A 47.5 22.659 16.00 52.80 53.009A 50.0 22.720 16.00 52.80 53.00
10A 52.5 22.782 12.50 41.25 41.0011A 55.0 22.840 10.00 33.00 33.0012A 57.5 22.889 7.00 23.10 23.00
Ultimo 60.0 18:00 22.931
oC
oC
Final Values 60.0 18:00 22.931Average Values 11.38 37.54
ISOKINETIC SAMPLING DATA
Date 19 de enero de 1998
Project #
Run # R-1# of Ports Used 2
Sampling Equipment
Meter # Apex 572Meter Calibration Factor (Y) 1.010Nozzle # 30Actual Nozzle Diameter (Dna) 6.200 mm
Ideal Nozzle Diameter (Dni) 6.335 mm
Probe # / Length 1.83 m
Liner Material Ac. Inox.Sample Case / Oven #
Impinger Case #
DVm Leak Checks
Pre m3/min @ mm Hg
Post m3/min @ mm Hg
DVm < 0.00057 m3/min Yes?
Pitot OK? Orsat OK?
Meter Meter Impinger Square
Stack Inlet Outlet Filter Exit Pump Root
Temp Temp Temp Temp Temp Vacuum DP(ts) (tmi) (tmo) (Dp1/2)
mm Hg (mm H2O)1/268 24 24 150 12 1.2 2.3570 24 24 150 12 1.5 3.0073 24 24 150 12 2.0 3.3976 24 24 150 12 2.2 3.4676 24 24 152 12 2.2 3.6176 24 24 151 13 2.5 3.8177 24 24 152 13 2.5 3.8777 24 24 152 12 2.5 3.8177 24 24 152 12 2.5 3.6176 24 24 150 13 2.0 3.3275 24 24 151 13 1.5 2.4574 24 24 151 13 1.0 2.0072 24 24 151 13 1.0 2.2476 24 24 151 12 1.2 1.5078 24 24 152 12 2.0 2.0078 24 24 152 12 2.5 2.0078 24 24 151 12 2.5 2.5079 25 25 151 11 3.0 3.8780 25 25 152 11 3.0 4.0080 25 25 152 12 3.0 4.0079 25 25 151 12 3.0 4.0078 25 25 150 12 2.5 3.5478 25 25 150 13 2.0 3.1677 25 25 151 13 2.0 2.65
oC oC oC oC oC
Maximum Vacuum 3.0 Final Values
76 24 24 151 12 3.0924
Local Cumulative Cumulative
Stack Meter Percent
Velocity Volume IsoKinetic
(vs)l (Vm)std (I)
m/sec scm %10.37 0.029 104.113.31 0.062 99.615.11 0.101 99.015.50 0.142 100.216.14 0.179 97.417.04 0.226 99.317.36 0.268 98.517.06 0.312 98.816.16 0.353 98.714.84 0.390 98.610.95 0.417 98.28.92 0.442 98.79.95 0.466 98.5
13.05 0.499 98.514.88 0.536 98.415.87 0.579 98.817.09 0.621 98.617.41 0.667 98.818.00 0.712 98.918.00 0.756 98.617.98 0.800 98.515.87 0.841 98.614.19 0.876 98.511.86 0.906 98.5
Final Values 0.906 98.514.87
METHOD 5 - SAMPLE RECOVERY AND INTEGRITY DATA SHEET
Plant Name Ladrillera El Rubí, Tunja Date
Sampling Location Chimenea Horno Project #
Operator Acetone Lot Number
Run History Data
Run Number R-1 R-2 R-3Run Start Time 15:35 (hh:mm)
Run Stop Time 18:00 (hh:mm)
Train Prepared By rjrTrain Recovered By rjrRecovery Date 1/19/1998 (mm/dd/yy)
Relinquished By
Received By C.Q.Relinquished Date (mm/dd/yy)
Relinquished Time (hh:mm)
Equipment Identification Numbers
Filter 117Acetone Wash 10Silica Gel 10Impinger Case 12
Sample Box 1
Oven 1
Moisture Content Data
Impingers 1, 2, and 3 - Water Volume
Final Volume (Vf) 216.0 ml
Initial Volume (Vi) 200.0 ml
Net Volume (Vn) 16.0 ml
Comments
Impinger 4 - Silica Gel Weight
Final Weight (Wf) 206.7 g
Initial Weight (Wi) 200.0 g
Net Weight (Wn) 6.7 g
Comments
Total Water Collected
Total Volume (Vlc) 22.7 g
Formulas Used
Vn = Vf - Vi Wn = Wf - Wi Vlc = Vn + Wn/rw where rw = .9982 g/ml
METHOD 5 - SAMPLE RECOVERY AND INTEGRITY DATA SHEET
19 de enero de 1998
Acetone Lot Number
METHOD 5 - DETERMINATION OF PARTICULATE EMISSIONS - RESULTS
Plant Name Ladrillera El Rubí, Tunja Date
Sampling Location Chimenea Horno Project #
Operator Universidad de La Salle Stack Type
Historical Data
Run Number R-1 R-1 R-1
Run Start Time
Run Stop Time 18:00Meter Calibration Factor (Y) 1.010 1.010 1.010Pitot Tube Coefficient (Cp) 0.850 0.850 0.850Actual Nozzle Diameter (Dna) 6.200 6.200 6.200
Stack Test Data
Initial Meter Volume (Vm)i 21.662Final Meter Volume (Vm)f 22.931Total Meter Volume (Vm) 1.269Total Sampling Time (Q) 60.0
Average Meter Temperature (tm)avg 24.3
Average Stack Temperature (ts)avg 76.2Barometric Pressure (Pb) 542.00 542.00 542.00Stack Static Pressure (Pstatic) 4.15 4.15 4.15Absolute Stack Pressure (Ps) 542.31 542.31 542.31Average Orifice Pressure Drop (DH)avg 37.54Absolute Meter Pressure (Pm) 544.76Avg Square Root Pitot Pressure (Dp1/2)avg 3.09
Moisture Content Data
Impingers 1-3 Water Volume Gain (Vn) 16.0Impinger 4 Silica Gel Weight Gain (Wn) 6.7Total Water Volume Collected (Vlc) 22.7Standard Water Vapor Volume (Vw)std 0.030Standard Meter Volume (Vm)std 0.906Calculated Stack Moisture (Bws(calc)) 3.2Saturated Stack Moisture (Bws(svp)) 55.8Reported Stack Moisture Content (Bws) 3.2
Gas Analysis Data
Carbon Dioxide Percentage (%CO2) 3.9Oxygen Percentage (%O2) 9.9Carbon Monoxide Percentage (%CO) 0.4Nitrogen Percentage (%N2) 85.8Dry Gas Molecular Weight (Md) 29.02Wet Stack Gas Molecular Weight (Ms) 28.66Calculated Fuel Factor (Fo) 2.512Percent Excess Air (%EA) 74.9
Volumetric Flow Rate Data
Average Stack Gas Velocity (vs) 13.76Stack Cross-Sectional Area (As) 0.66 0.66 0.66Actual Stack Flow Rate (Qa) 549Dry Standard Stack Flow Rate (Qsd) 318Percent of Isokinetic Rate (I) 104.5
Emission Rate Data
Mass of Particulate on Filter (mf) 22.6
Mass of Particulate in Acetone (ma') 15.5Mass due to Acetone Blank (Wa) 0.0Total Mass of Particulates (mn) 38.1Stack Particulate Concentration (cs) 0.042Stack Particulate Concentration (cs) 0.649Particulate Emission Rate (E) 0.80
METHOD 5 - DETERMINATION OF PARTICULATE EMISSIONS - RESULTS
15 de Octubre de 2004
Circular
Historical Data
Average
hh:mm
hh:mm
mm
Stack Test Data
m3
m3
1.269 m3
60.0 min
24.3
76.2542.00 mm Hg
4.15 mm H2O
542.31 mm Hg
37.54 mm H2O
544.76 mm Hg
3.09 (mm H2O)1/2
Moisture Content Data
16.0 ml
6.7 g
22.7 ml
0.030 scm
0.906 dscm
3.2 %
55.8 %
3.2 %
Gas Analysis Data
3.9 %
9.9 %
0.4 %
85.8 %
29.02 g/g-mole
28.66 g/g-mole
2.51274.9 %
Volumetric Flow Rate Data
13.76 m/sec
m2
549 acmm
318 dscmm
104.5 %
Emission Rate Data
22.6 mg
oC
oC
15.5 mg
0.0 mg
38.1 mg
0.042 g/dscm
0.649 gr/dscm
0.80 kg/hr