Parndon Wood Crematorium - Emissions Report 2016 · 2019-08-09 · EMISSIONS MONITORING TEST REPORT...
Transcript of Parndon Wood Crematorium - Emissions Report 2016 · 2019-08-09 · EMISSIONS MONITORING TEST REPORT...
EMISSIONS MONITORING TEST REPORT
PARNDON WOOD CREMATORIUM Harlow Essex
CM19 4SF
15th March 2016
Report Authorised by Date 15.th April 2016 Mr J L Boyce Emissions Monitoring Team Leader
MCertS level 2 + TE1,2,3,4 MM 06 707 JB/DEMD0909/15.03.16
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CONTENTS 1. INTRODUCTION 2. PROCEDURES
2.1 Total Particulate Matter 2.2 Hydrogen Chloride 2.3 Mercury 2.4 Carbon monoxide 2.5 Total Organic Compounds 2.6 Oxygen 2.7 Moisture 2.8 Temperature 2.9 Velocity and Volumetric Flow
3. RESULTS TABLE 1 – Parndon Wood Cremators 1 & 2 & Abatement System –
Total Particulate Matter and Hydrogen Chloride Results TABLE 2 – Parndon Wood Cremators 1 & 2 & Abatement System –
Mercury Results TABLE 3 – Parndon Wood Cremators 1 & 2 & Abatement System –
Comparison of Test Results with Site Instrumentation 4. COMMENTS 5. QUALITY CONTROL APPENDIX 1 Data Logs and Calculations APPENDIX 2 Analysis Reports
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1. INTRODUCTION The two cremators and associated flue gas abatement system at Parndon Wood Crematorium, Harlow Essex, CM19 4SF were monitored on the 15th March 2016 to the requirements given in Process Guidance Note PG5/2 (2012) for emission releases to atmosphere. The work was carried out on site by the following staff of Davies & Co (Engineering) Limited: Mr J L Boyce EA MCertS Level 2 + TE1,2,3,4 MM 06 707 Davies & Co does not hold company UKAS / MCertS accreditation at this time, as the company specialises in cremator and incinerator testing that are Part B processes. Air Quality Guidance Note AQ12 (04) states that UKAS / MCertS accreditation is not a mandatory requirement for the testing of Part B processes. Davies & Co are members of the Source Testing Association, and have extensive knowledge of crematoria testing. All analysis was conducted using UKAS approved laboratories, methods and calibrated equipment. The work on site involved monitoring the flue gas components after the flue gas abatement system fitted to the cremator with the plant operating normally. The plant being tested comprises two cremators, No 1 of model type FTIII with a wider hearth and No 2 of model type FTII, both fitted with two nozzle mix burners utilising natural gas as the support fuel. The waste gases from both cremators combine and are ducted to a flue gas treatment plant. The treatment plant comprises of a shell and tube boiler to cool the flue gases, a reagent feeder station that introduces a blend of activated carbon/sodium bicarbonate to react with the cooled gases, and a bag filter to clean the treated gases. The waste heat from the boilers in the form of warm water is dissipated to atmosphere via a finned tube air blast cooler situated outside the crematory. The plant operates under full microprocessor based automatic control that requires little manual intervention. The cremators and flue gas abatement system were manufactured, installed and commissioned by Facultatieve Technologies Limited to meet the requirements of the Environmental Permitting (England & Wales) Regulations 2010 (EPR 2010) as relevant to new crematoria installations, summarised in Process Guidance Note PG5/2 (2012). The flue ducting and test points were in accordance with the requirements of EA TGN M1. Measurements were undertaken to enable comparisons to be made of the operation of the cremators and associated abatement system with the requirements of the Guidance Note in terms of emission releases to air.
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This report details the monitoring procedures used and the results obtained from this test work along with comparisons with the requirements and comments where appropriate. Relevant procedures were followed to enable quality control to be maintained throughout the test preparation, site test work, laboratory analysis, calculations and reporting.
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2. PROCEDURES 2.1 Total Particulate Matter A flue gas sample was extracted and filtered to collect total particulate matter. A Whatman QM-A filter paper was used with a particle retention of not less than 99.5% at a particle size of 0.3 micron. The flue gas extraction employed techniques given in BS EN 13284 Part 1. The method employed was BS EN 13284 Part 1.
The sampling was conducted using apparatus in accordance with the requirements of BS EN 13284 Part 1. This consisted of a heated known dimension Pyrex glass nozzle, heated Pyrex glass probe liner, heated Pyrex glass filter housing with Titanium frit containing quartz microfibre filter (all heaters set to 160°C), PTFE sample line, dreschel absorption bottles, gas dryer (silica gel), sample line to pump, pump, gas meter, rotameter, pitot and impulse lines, electronic manometer, type K thermocouple, balance (for gravimetric moisture) and datalogger. Settings tables were pre-prepared to enable isokinetic flow to be maintained (based on online measurements of flue gas velocity and temperature to set nozzle flow / pump rate (l/min)). Particulate matter analysis was carried out by weighing the filter and probe rinse collection on a calibrated balance, with the media being dried and weighed prior to and following the test. Standard BS EN 13284 Part 1 was deviated from only in so far as a consequence of conducting tests in accordance with the requirements of PG5/2(12) that requires total particulate matter to be sampled for one hour of cremation. This therefore implies that only one sampling line can be used for each test run as sampling on 2 lines would require a stop half way through the test to move the probe out of one port and into another thus losing a period within the allotted one hour needed to obtain an hourly average as required by PG5/2(12). This is contrary to BS EN 13284 Part 1 that requires 2 sample lines to be used during an isokinetic test i.e. four point sampling (2 points x 2 lines) for a duct of this diameter.
The effect on uncertainty of using only one sample line is not considered to be significant and assumed to be within the calculated uncertainties stated in this report. These assumptions are on the basis that the preliminary pitot traverses confirmed the gas velocity profiles were well within required limits, and the duct diameter was relatively small (350 mm diameter) considering the scope of BS EN 13284 Part 1. The duct was compliant with the requirements of the Standard in terms of duct diameter and length measurements as well as meeting all requirements of Environment Agency Technical Guidance Note M1. In accordance with the Standard flue gas was sampled at 2 representative points along the sample line and as such there is no reason to suspect that the gas sampled from only one sampling line is not representative of the duct as a whole. This recommended deviation is a reflection that cremation is a batch process, and that changing sampling ports part-way through a cremation could introduce more errors due to fact that a period of each cremation would not be sampled during the changeover process. The tests reported herein were conducted to prove the performance of the cremators relative to PG5/2(2012).
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The tests reported herein were conducted to prove the performance of the cremators relative to PG5/2(2012). 2.2 Hydrogen Chloride A flue gas sample was extracted and filtered. A Whatman QM-A filter paper was used with a particle retention of not less than 99.5% at a particle size of 0.3 micron. The flue gas extraction employed techniques given in BS EN 13284 Part 1. The sampling was conducted using apparatus in accordance with the requirements of BS EN 13284 Part 1. The method employed was BS EN 1911 Parts 1-3. Laboratory analysis for hydrogen chloride was carried out on the absorption medium using Ion Chromatography (IC). 2.3 Mercury A flue gas sample was extracted and filtered to collect solid phase mercury. A Whatman QM-A filter paper was used with a particle retention of not less than 99.5% at a particle size of 0.3 micron. The flue gas extraction employed techniques given in BS EN 13284 Part 1. The gas sample was then passed through an absorption medium of acidified potassium dichromate to collect vapour phase mercury. The method employed was BS EN 13211. Laboratory analysis for solid and vapour phase mercury was carried out on the filter and absorption medium using Inductively Cold Vapour Atomic Fluorescence Spectroscopy (CVAFS). 2.4 Carbon Monoxide A flue gas sample was continuously extracted, filtered and dried before being passed through a pre-calibrated Siemens Ultramat 23 infrared analyser for the on-line measurement of carbon monoxide. The method employed was BS EN 15058. The analyser has a fixed range of 0-1250 mg/Nm3 and was zeroed with air and calibrated with a nominal 800 ppmv carbon monoxide in balance nitrogen gas. The analyser output was continuously recorded using a Grant 'Squirrel' data logger.
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For these tests a relatively high range analyser was used due to the typical pattern of carbon monoxide concentration emissions from cremators being very low (often indicated as zero) for most of the cycle, but with occasional, high, short duration spikes of CO being emitted. The convention since non-continuous emissions monitoring became a mandatory requirement for cremators during 1990, has been to attempt to monitor the magnitude of spikes, as these are often the main contributor to total CO emissions. If, for example, a mean one minute emission of CO was say 100 mg/Nm³, it would be expected that the peak concentration during that one minute averaging period would be considerably higher than this. It follows that utilising a lower range analyser would frequently understate CO emissions, despite increasing sensitivity at low CO concentrations. 2.5 Total Organic Compounds A flue gas sample was continuously extracted and filtered before being passed via a heated line through a pre-calibrated Signal 3030PM Flame Ionisation Detection (FID) analyser for the on-line measurement of volatile organic compounds. The analyser was ranged 0-100 ppmv total hydrocarbons and was zeroed with air passed through a catalytic converter and calibrated with a nominal 50 ppmv propane in balance air gas. The method employed was BS EN 12619. The analyser output was continuously recorded using a Grant 'Squirrel' data logger. Similar comments apply to TOC’s as CO, in that the analyser scaling is set to quantify the peaks that are the nature of the emission. 2.6 Oxygen A flue gas sample was continuously extracted from the same position in the flue as the hydrogen chloride extraction, filtered and dried before being passed through a pre-calibrated Siemens Ultramat 23 electrochemical cell analyser for the on-line measurement of flue oxygen. The method employed was BS EN 14789. The analyser was calibrated using a standard reference gas in the laboratory before and after the site visit, and with nitrogen “zero” gas and air at the start and end of each day’s testing on site. It was assumed that calibration linearity was maintained during sampling, and the post checks indicated that this was the case. The output of the analyser was continuously recorded using a Grant 'Squirrel' data logger. 2.7 Moisture A flue gas sample was extracted and filtered. The gas sample was then passed through an absorption medium to collect any water vapour. The method employed was BS EN 14790.
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Flue gas moisture was determined gravimetrically by weighing the absorption medium and final gas drier prior to and following the test. This was carried out alongside testing for hydrogen chloride. 2.8 Temperature Flue gas temperature was measured by the use of a calibrated Type K thermocouple. The method employed was BS EN 13284 Part 1. The flue gas temperature was continuously recorded using a Grant 'Squirrel' data logger. 2.9 Velocity and Volumetric Flow Flue gas velocity was found from inserting a calibrated s-type pitot tube into the flue. The pitot head pressure was then measured using a calibrated electronic manometer. The method employed was BS EN 13284 Part 1. The electronic manometer output was continuously recorded using a Grant 'Squirrel' data logger. Flue gas velocity was then calculated from Bernoulli's equation as the density of the flue gas was known (from measurements of flue gas moisture and temperature). Flue gas volumetric flow rate was found from the measurement of the flue duct size and hence its area and corrected to normalised conditions (again from measurements of flue gas moisture and temperature).
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3. RESULTS The results are summarised in Tables 1 - 3. Total Particulate Matter and Hydrogen Chloride determinations are given in Table 1. Mercury determination is given in Table 2. Comparisons of the test results with the site instrumentation are given in Table 3. Carbon Monoxide, Total Organic Compounds, Oxygen, Temperature and Velocity and Volumetric Flow were continuously monitored. All values in the tables are corrected to the reference conditions of 273K, 101.3kPa, 11%v/v oxygen and dry gas as given in PG5/2(12) where required. All data logs and calculations can be seen in Appendix 1. All analysis reports can be seen in Appendix 2.
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TABLE 1Parndon Wood Cremators 1 & 2 & Abatement SystemEmissions Monitoring 15th March 2016Total Particulate Matter & Hydrogen Chloride Sampling
Average Requirement toPG5/2 (2012)
Total Particulate Matter - mg/Nm3c. 1.43 ± 2.22 1.41 ± 2.82 1.15 ± 2.68 1.33 <20
Hydrogen Chloride - mg/Nm3c. 14.16 ± 0.73 10.25 ± 0.60 12.56 ± 0.68 12.32 <30
Carbon Monoxide - mg/Nm3c. 4.68 ± 0.23 4.37 ± 0.22 1.28 ± 0.06 3.44 <100
Carbon Monoxide First 30 mins - mg/Nm3c. 0.91 ± 0.05 0.00 ± 0.00 0.04 ± 0.00 0.32 <100
Carbon Monoxide Second 30 mins- mg/Nm3c. 8.57 ± 0.01 8.88 ± 0.01 2.56 ± 0.13 6.67 <100
Organic Compounds - mg/Nm3c. 0.54 ± 0.01 0.79 ± 0.04 0.04 ± 0.01 0.46 <20
Flue Oxygen - %v/v dry 14.60 ± 0.10 15.42 ± 0.10 15.00 ± 0.10 15.00Flue Moisture - %v/v 9.2 ± 0.9 9.4 ± 0.9 11.2 ± 1.1 9.9
- %w/w 6.0 ± 0.6 6.1 ± 0.6 7.3 ± 0.7 6.4Flue Temperature - Deg C 137 ± 2 141 ± 2 138 ± 2 139Volumetric Flow - Nm
3/h dry 3075 ± 61 2617 ± 52 2527 ± 51 2740
Note 1: All emissions as concentration levels are given as mg/Nm3 corrected to 11%v/v oxygen and dry gas
Note 2: All uncertainties (±) are calculated to a 95% confidence interval
Uncertainties estimated using the procedure suggested in the STA Quality Guidance Note QGN001-01
Test 1 Test 2 Test 3
15 March 2016 15 March 2016 15 March 2016
11:08-12:08 12:36-13:36 14:02-15:02
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TABLE 2Parndon Wood Cremators 1 & 2 & Abatement System OutletEmissions Monitoring 15th March 2016Mercury Sampling
Requirement toPG5/2 (2012)
Mercury - µg/Nm3c. 17.56 ± 0.89 <50
Flue Oxygen - %v/v dry 13.30 ± 0.10
Flue Moisture - %v/v 11.4 ± 1.1
- %w/w 7.4 ± 0.7
Flue Temperature - Deg C 134 ± 2
Volumetric Flow - Nm3/h dry 3387 ± 68
Note 1: All emissions as concentration levels are given as µg/Nm3 or mg/Nm3 corrected to 11%v/v oxygen and dry gas
Note 2: All uncertainties (±) are calculated to a 95% confidence interval
Uncertainties estimated using the procedure suggested in the STA Quality Guidance Note QGN001-01
Hg Test
15 March 2016
08:14-10:49
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TABLE 3
Cremators Abatement System Outlet
Emissions Monitoring Parndon Wood 2016
Comparison of Test Results with Site Instrumentation
Cermator Test Date Averaging
Plant Period (mins) Davies & Co Site
Cremator FGT Out 1 March 15, 2016 0 - 30 1 5
Cremator FGT Out 1 March 15, 2016 30 - 60 9 8
Cremator FGT Out 2 March 15, 2016 0 - 30 0 6
Cremator FGT Out 2 March 15, 2016 30 - 60 9 6
Note 1: All emission concentration levels are given as mg/Nm3 corrected to 11% oxygen, 273K & dry gas
Note 2: Results as emitted from Flue Gas Treatment (FGT) Plant with 2 cremators abated by 1 FGT
Carbon Monoxide mg/Nm³
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4. COMMENTS The results obtained from this monitoring test work show compliance with the requirements given in Process Guidance Note PG5/2 (2012) for the cremators and abatement system. The cremators and flue gas clean up system operated satisfactorily during testing without any failure or alarm events. No unusual charges were cremated during these tests. They were of all standard materials. No visible chimney emissions, other than the expected steam plume during pre-heat, were observed throughout the test work. PG5/2 (2012) states that the continuous emission monitors (CEMs) should be periodically checked (calibrated) to ensure that the readings being reported are correct. The CEM’s on site are regularly maintained, checked and calibrated in accordance with the manufacturers recommendations, and were functional at the time of the tests. The PCME particulate monitor primarily functions as a filter leak detector rather than being calibrated to give qualitative results. This instrument is more than capable of satisfying this function. Limited similarity of carbon monoxide emissions was evident although levels were low throughout these tests therefore supplying insufficient data for an effective comparison. 5. QUALITY CONTROL All the tests performed were carried out to the methods given in the appropriate listed Standards using calibrated equipment. The gas analyser was calibrated prior to use using suitable calibration gases. Analysis of the absorber solutions was carried out at an external UKAS laboratory following UKAS approved analysis methods. For this test work the following external laboratory was used for the given determination: Scientific Analysis Laboratories (SAL) } Hydrogen Chloride Mercury
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APPENDIX 1
Data Logs and Calculations
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Explanation of Data Logs
Data is taken from a Grant Squirrel data logger. Time is from logger clock. Flue Gas Temp is direct from test flue thermocouple. Meter Temp is direct from gas meter. (The stated meter temperature is that of the sampled gas at the meter, and is not the room ambient temperature. The temperature always increases during a test due to the heat gain from the sample pump that is contained in an enclosed box along with the gas meter, and this is quite normal). Flue O2 is from the Siemens Ultramat 23 analyser. CO is from the Siemens Ultramat 23 analyser. TOC is from the Signal 3030PM FID analyser expressed as carbon equivalent. Sample Point Pa is from the pitot tube to a Furness Controls FCO12 electronic manometer. The room temperature was typically 20°C, and there were no issues with the analysers overheating. Functional and calibration checks at the start and end of each test confirmed correct operation of the analysers. All values in the tables are corrected to the reference conditions of 273K, 101.3kPa, 11%v/v oxygen and dry gas as given in PG5/2(12) where required.
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Parndon Wood Cremators 1 & 2 & Abatement System
Data Log
Test 1
Time Flue Gas Meter Flue O2 CO TOC Sample PointoC
oC %v/v dry mg/Nm
3 c. mg/Nm
3 c. Pa
11:08 132 34.0 14.47 0.00 0.00 96.6
11:09 132 34.1 15.47 0.00 0.00 86.5
11:10 132 34.3 15.47 0.00 0.00 96.6
11:11 132 34.4 15.07 0.00 0.00 85.7
11:12 132 34.6 15.07 3.72 0.00 84.0
11:13 133 34.7 15.07 1.86 0.00 110.9
11:14 133 34.8 14.27 0.00 0.00 105.0
11:15 133 35.0 13.37 0.00 0.00 117.6
11:16 134 35.1 13.37 0.79 0.00 123.5
11:17 135 35.3 13.27 0.00 0.00 129.4
11:18 135 35.4 13.67 1.37 0.00 119.3
11:19 136 35.5 13.57 0.81 0.00 117.6
11:20 136 35.7 13.57 3.10 0.00 116.8
11:21 137 35.8 13.37 12.86 0.00 121.8
11:22 138 36.0 13.67 3.69 0.00 127.7
11:23 138 36.1 13.97 0.00 0.00 109.2
11:24 138 36.2 13.77 0.00 0.00 107.5
11:25 139 36.4 14.17 0.00 0.00 107.5
11:26 138 36.5 14.27 0.00 0.00 98.3
11:27 138 36.7 14.17 0.00 0.00 94.1
11:28 139 36.8 14.27 0.00 0.00 95.8
11:29 139 36.9 14.37 0.00 0.00 91.6
11:30 139 37.1 14.37 0.00 0.00 86.5
11:31 138 37.0 14.47 0.00 0.00 79.0
11:32 139 37.1 14.47 0.00 0.00 83.2
11:33 139 37.2 14.47 0.00 0.00 86.5
11:34 139 37.2 14.57 0.00 0.00 91.6
11:35 139 37.3 14.77 0.00 0.00 95.8
11:36 139 37.3 14.97 0.00 0.00 100.0
11:37 140 37.4 15.17 0.00 0.00 98.3
11:38 140 37.4 15.47 0.00 0.00 102.5
11:39 139 37.5 15.77 0.00 0.00 84.8
11:40 139 37.5 16.67 0.00 0.00 73.1
11:41 138 37.6 16.67 0.00 0.00 63.0
11:42 137 37.6 16.37 0.00 0.00 53.8
11:43 138 37.7 16.67 223.64 29.98 99.1
11:44 139 37.7 14.87 26.51 2.82 94.9
11:45 138 37.8 14.37 0.91 0.00 80.6
11:46 137 37.8 15.17 0.00 0.00 61.3
11:47 137 37.9 15.57 0.00 0.00 58.8
11:48 137 37.9 15.97 0.00 0.00 59.6
11:49 137 38.0 16.27 0.00 0.00 68.0
11:50 137 38.0 15.07 0.00 0.00 69.7
11:51 137 38.0 16.17 0.00 0.00 77.3
11:52 137 38.1 14.37 0.00 0.00 76.4
11:53 137 38.1 15.57 1.11 0.00 93.2
11:54 137 38.2 13.17 0.77 0.00 94.9
11:55 137 38.2 15.47 1.09 0.00 78.1
11:56 138 38.3 14.37 0.91 0.00 107.5
11:57 137 38.3 14.07 0.00 0.00 76.4
11:58 138 38.4 15.67 2.07 0.00 91.6
11:59 138 38.4 13.37 0.00 0.00 103.3
12:00 138 38.5 13.67 0.00 0.00 84.0
12:01 138 38.5 13.57 0.00 0.00 84.8
12:02 138 38.6 13.67 0.00 0.00 83.2
12:03 138 38.6 13.87 0.00 0.00 81.5
12:04 138 38.7 13.97 0.00 0.00 79.0
12:05 138 38.7 13.87 0.00 0.00 76.4
12:06 138 38.8 13.87 0.00 0.00 71.4
12:07 138 38.8 14.07 0.00 0.00 68.9
12:08 138 38.9 13.67 0.00 0.00 75.6
Average 137 37.1 14.60 4.68 0.54 90.8
0.91
8.57
Carbon Monoxide First 30 mins
Carbon Monoxide Second 30 mins
15 March 2016
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Parndon Wood Cremators 1 & 2 & Abatement System
Data Log
Test 2
Time Flue Gas Meter Flue O2 CO TOC Sample PointoC
oC %v/v dry mg/Nm
3 c. mg/Nm
3 c. Pa
12:36 138 33.5 15.55 0.00 0.00 78.1
12:37 139 33.6 15.55 0.00 0.00 83.2
12:38 139 33.6 15.65 0.00 0.00 84.8
12:39 139 33.7 15.55 0.00 0.00 85.7
12:40 140 33.8 15.35 0.00 0.00 104.2
12:41 140 33.8 14.65 0.00 0.00 96.6
12:42 140 33.9 14.75 0.00 0.00 89.9
12:43 141 33.9 13.95 0.00 0.00 104.2
12:44 141 34.0 13.95 0.00 0.00 106.7
12:45 142 34.1 14.05 0.00 0.00 110.0
12:46 143 34.1 14.05 0.00 0.00 118.4
12:47 144 34.2 14.65 0.00 0.00 104.2
12:48 144 34.2 14.95 0.00 0.00 95.8
12:49 144 34.3 14.95 0.00 0.00 82.3
12:50 144 34.4 14.75 0.00 0.00 75.6
12:51 144 34.4 14.75 0.00 0.00 76.4
12:52 145 34.5 14.75 0.00 0.00 76.4
12:53 144 34.5 14.85 0.00 0.00 68.0
12:54 144 34.6 14.65 0.00 0.00 64.7
12:55 144 34.7 14.95 0.00 0.00 60.5
12:56 144 34.7 15.05 0.00 0.00 59.6
12:57 144 34.8 15.15 0.00 0.00 62.2
12:58 144 34.8 14.95 0.00 0.00 60.5
12:59 143 34.9 14.95 0.00 0.00 51.2
13:00 143 35.0 15.05 0.00 0.00 47.0
13:01 143 35.0 15.05 0.00 0.00 51.2
13:02 143 35.1 15.15 0.00 0.00 53.8
13:03 143 35.1 15.35 0.00 0.00 55.4
13:04 142 35.2 15.55 0.00 0.00 51.2
13:05 142 35.3 15.75 0.00 0.00 48.7
13:06 142 35.3 15.95 0.00 0.00 47.9
13:07 142 35.4 16.15 0.00 0.00 47.9
13:08 142 35.4 16.35 0.00 0.00 49.6
13:09 141 35.5 17.85 0.00 0.00 26.9
13:10 140 35.6 16.85 0.00 0.00 29.4
13:11 139 35.6 17.15 0.00 0.00 47.0
13:12 139 35.7 18.85 0.00 0.00 48.7
13:13 139 35.7 19.05 0.00 0.00 19.3
13:14 140 35.8 17.75 238.49 46.09 66.4
13:15 141 35.9 15.35 25.94 1.88 63.8
13:16 140 35.9 15.05 0.00 0.00 51.2
13:17 139 36.0 15.75 0.00 0.00 63.8
13:18 139 36.0 15.75 0.00 0.00 63.0
13:19 139 36.1 14.25 0.00 0.00 62.2
13:20 139 36.2 15.15 0.00 0.00 58.0
13:21 140 36.2 14.65 0.16 0.00 60.5
13:22 139 36.3 14.15 0.15 0.00 59.6
13:23 139 36.3 16.15 1.24 0.00 63.0
13:24 140 36.4 13.75 0.00 0.00 65.5
13:25 139 36.5 15.75 0.19 0.00 65.5
13:26 140 36.5 15.75 0.19 0.00 73.1
13:27 141 36.6 14.75 0.00 0.00 58.0
13:28 140 36.6 16.35 0.00 0.00 58.0
13:29 140 36.7 16.45 0.00 0.00 65.5
13:30 139 36.8 15.65 0.00 0.00 62.2
13:31 139 36.8 15.95 0.00 0.00 65.5
13:32 138 36.9 15.75 0.00 0.00 62.2
13:33 138 36.9 15.35 0.00 0.00 66.4
13:34 138 37.0 14.45 0.00 0.00 63.0
13:35 137 37.1 14.85 0.00 0.00 62.2
13:36 137 37.1 15.25 0.00 0.00 60.5
Average 141 35.3 15.42 4.37 0.79 66.6
Carbon Monoxide First 30 mins 0.00
Carbon Monoxide Second 30 mins 8.88
15 March 2016
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Parndon Wood Cremators 1 & 2 & Abatement System
Data Log
Test 3
Time Flue Gas Meter Flue O2 CO TOC Sample PointoC
oC %v/v dry mg/Nm
3 c. mg/Nm
3 c. Pa
14:02 134 34.7 14.28 1.04 0.00 60.5
14:03 135 34.8 14.68 0.00 0.00 69.7
14:04 135 34.8 15.78 0.00 0.00 53.8
14:05 135 34.9 14.88 0.16 0.00 69.7
14:06 136 34.9 13.98 0.14 0.00 74.8
14:07 136 35.0 14.28 0.00 0.00 68.0
14:08 137 35.0 13.88 0.00 0.00 70.6
14:09 138 35.1 13.98 0.00 0.00 73.1
14:10 138 35.1 14.48 0.00 0.00 73.1
14:11 138 35.2 14.78 0.00 0.00 79.8
14:12 138 35.2 15.28 0.00 0.00 73.1
14:13 139 35.2 15.58 0.00 0.00 77.3
14:14 139 35.3 15.78 0.00 0.00 75.6
14:15 139 35.3 14.98 0.00 0.00 75.6
14:16 139 35.4 15.28 0.00 0.00 73.1
14:17 139 35.4 15.28 0.00 0.00 71.4
14:18 138 35.5 15.38 0.00 0.00 70.6
14:19 138 35.5 15.48 0.00 0.00 70.6
14:20 138 35.6 15.68 0.00 0.00 63.0
14:21 138 35.6 15.78 0.00 0.00 59.6
14:22 138 35.7 15.88 0.00 0.00 58.0
14:23 138 35.7 15.98 0.00 0.00 57.1
14:24 138 35.8 15.98 0.00 0.00 62.2
14:25 138 35.8 16.18 0.00 0.00 58.7
14:26 138 35.9 16.38 0.00 0.00 58.3
14:27 138 35.9 16.48 0.00 0.00 57.9
14:28 137 35.9 17.38 0.00 0.00 57.5
14:29 136 36.0 18.38 0.00 0.00 57.0
14:30 135 36.0 18.28 0.00 0.00 56.6
14:31 135 36.1 17.88 0.00 0.00 56.2
14:32 135 36.1 17.28 0.00 0.00 55.8
14:33 136 36.2 18.38 30.97 0.00 51.2
14:34 137 36.2 17.18 44.87 2.58 74.8
14:35 137 36.3 11.78 0.00 0.00 45.4
14:36 136 36.3 14.58 0.00 0.00 26.9
14:37 136 36.3 13.58 0.00 0.00 36.1
14:38 136 36.6 15.58 0.00 0.00 42.8
14:39 136 36.6 14.28 0.00 0.00 47.0
14:40 136 36.5 15.28 0.00 0.00 51.2
14:41 136 36.5 13.88 0.00 0.00 44.5
14:42 136 36.5 14.88 0.00 0.00 48.7
14:43 137 36.6 14.98 0.00 0.00 44.5
14:44 137 36.7 14.48 0.00 0.00 70.6
14:45 139 36.7 13.28 0.00 0.00 82.3
14:46 139 36.8 15.08 0.00 0.00 86.5
14:47 140 36.9 12.88 0.00 0.00 90.7
14:48 140 36.9 13.88 0.00 0.00 74.8
14:49 140 37.0 14.58 0.78 0.00 52.1
14:50 141 37.0 14.28 0.15 0.00 79.8
14:51 141 36.9 13.38 0.00 0.00 78.1
14:52 142 36.9 13.68 0.00 0.00 77.3
14:53 142 37.0 13.68 0.00 0.00 76.4
14:54 143 37.0 13.88 0.00 0.00 71.4
14:55 143 37.1 13.88 0.00 0.00 70.6
14:56 143 37.2 13.78 0.00 0.00 68.5
14:57 143 37.3 13.78 0.00 0.00 66.4
14:58 143 37.3 13.98 0.00 0.00 64.3
14:59 143 37.4 13.78 0.00 0.00 62.2
15:00 143 37.5 13.98 0.00 0.00 60.1
15:01 142 37.6 14.28 0.00 0.00 58.0
15:02 142 37.7 14.28 0.00 0.00 55.9
Average 138 36.1 15.00 1.28 0.04 63.9
Carbon Monoxide First 30 mins 0.04
Carbon Monoxide Second 30 mins 2.56
15 March 2016
JB/DEM0909/15.03.15 /Page19
Parndon Wood Cremators 1 & 2 & Abatement System
Total Particulate Matter and Hydrogen Chloride
Contract Parndon Wood Crematorium DEM0909
Date 15th March 2016
Location Cremators 1 & 2 & Abatement System Outlet
Engineer(s) JBAbsorbent H2O
Test Log Test 1 Test 2 Test 3
Barometric Pressure(kPa) 101.0 101.0 101.0
Gas Meter Temperature(Deg C) 37.1 35.3 36.1
Oxygen Concentration(%v/v dry) 14.60 15.42 15.00
Flue Gas Volumetric Flow(Nm3/h dry) 3075 2617 2527
Start End Start End Start End
Time 11:08 12:08 12:36 13:36 14:02 15:02
Gas Meter Reading(Am3 dry) 82.692 83.249 83.482 83.983 84.076 84.567
Absorber Weight(g) 3321.5 3361.5 3521.8 3558.7 3351.6 3395.4
Filter Reference PW150316F1 PW150316F2 PW150316F3
Filter Weight(g) 0.55133 0.55142 0.54840 0.54847 0.53893 0.53899
Probe Rinse Reference PW150316R1 PW150316R1 PW150316R1
Probe Rinse Weight(g) 76.88558 76.88594 76.88594 76.88621 76.88621 76.88645
Sample Reference HCl PW270116H1 PW270116H2 PW270116H3A+B
Absorbent Volume(ml) 500 250 250
Absorbent(mg/l as HCl) 5.1 13 0.06
Blank(mg/l as HCl) 0.06 0.06
Calculation: General
Barometric Pressure(kPa) 101.0 101.0 101.0
Gas Meter temperature(Deg C) 37.1 35.3 36.1
Gas Volume Sampled(Am3 dry) 0.557 0.501 0.491
Gas Volume Sampled(Nm3 dry) 0.4890 0.4423 0.4323
Mass of Dry Gas(g @ 1292.8 g/Nm3) 632.16 571.82 558.92
Change in Absorber Weight(g) 40.0 36.9 43.8
Water Vapour Volume(Nm3 @ 803.9 g/Nm
3) 0.0498 0.0459 0.0545
Gas Volume(Nm3 wet) 0.5387 0.4882 0.4868
Mass of Wet Gas(g) 672.16 608.72 602.72
Moisture Concentration(%v/v) 9.2 9.4 11.2
Moisture Concentration(%w/w) 6.0 6.1 7.3
500
8.9
0.06 0.06
JB/DEM0909/15.03.15 /Page20
Calculation: Particulate
Increase In Filter Weights(g) 0.00045 0.00035 0.00030
Particulate Emission(mg/Nm3 dry) 0.91 0.78 0.69
Oxygen Concentration(%v/v dry) 14.60 15.42 15.00
Particulate Emission 1.43 1.41 1.15
(mg/Nm3 @ 11 %v/v Oxygen dry)
Flue Gas Volumetric Flow(Nm3/h dry) 3075 2617 2527
Particulate Emission(g/h) 2.80 2.05 1.74
Required Sample Velocity(Nm/s) 8.88 7.56 7.29
Nozzle Used(mm) 4.5 4.5 4.5
Area of Nozzle(m2) 0.00001590 0.00001590 0.00001590
Test Duration(mins) 60 60 60
Actual Sample Velocity(Nm/s) 8.54 7.73 7.55
Isokinetic Closure(%) 96 102 104
Start Leak Check(%) 1.2 1.2 1.2
@10 l/min @10 l/min @10 l/min
End Leak Check(%) 1.2 1.2 1.2
@10 l/min @10 l/min @10 l/min
Calculation: HCl
Absorbent(mg/l as HCl) 8.9 5.1 13.06
Blank(mg/l as HCl) 0.06 0.06 0.06
Chloride Absorbed(mg/l as HCl) 8.84 5.04 13
Chloride Absorbed(mg as HCl) 4.42 2.52 3.25
HCl(mg) 4.42 2.52 3.25
HCl Emission(mg/Nm3 dry) 9.04 5.70 7.52
Oxygen Concentration(%v/v dry) 14.60 15.42 15.00
HCl Emission 14.16 10.25 12.56
(mg/Nm3 @ 11 %v/v Oxygen dry)
Flue Gas Volumetric Flow(Nm3/h dry) 3075 2617 2527
HCl Emission(g/h) 27.79 14.91 18.99
101
JB/DEM0909/15.03.15 /Page21
Parndon Wood Cremators 1 & 2 & Abatement System
Flue Gas Volumetric Flow
Contract Parndon Wood Crematorium DEM0909
Date 15th March 2016
Location Cremators 1 & 2 & Abatement System Outlet
Engineer(s) JB
Test Log Test 1 Test 2 Test 3
Flue Gas Temperature(Deg C) 137 141 138
Flue Gas Pitot Head Sample Points(Pa) 90.8 66.6 63.9
Flue Gas Moisture(%v/v) 9.2 9.4 11.2
Flue Gas Moisture(%w/w) 6.0 6.1 7.3
Flue Gas Duct Dimensions(mm)
Flue Gas Duct Area(m2)
Calculation
Flue Gas Density(kg/m3) 0.8414 0.8331 0.8346
Flue Gas Velocity(Am/s) 14.69 12.64 12.37
Flue Gas Volumetric Flowrate(Am3/h) 5088 4380 4286
Flue Gas Volumetric Flowrate(Am3/h dry) 4618 3968 3806
Flue Gas Volumetric Flowrate(Nm3/h dry) 3075 2617 2527
350mm Diameter Circular Duct
0.0962
JB/DEM0909/15.03.15 /Page22
Parndon Wood Cremators 1 & 2 & Abatement System Outlet
Data Log 15/03/16
Hg Test
Time Flue Gas Meter Flue O2 Pitot HeadoC
oC %v/v dry Pa
08:14 101 13.6 16.35 76.4
08:15 102 13.6 13.65 95.8
08:16 104 13.7 15.15 100.0
08:17 104 13.9 13.25 92.4
08:18 105 14.1 12.45 86.5
08:19 105 14.4 12.85 85.7
08:20 106 14.5 12.65 102.5
08:21 107 14.6 12.35 97.4
08:22 108 14.8 12.25 101.6
08:23 108 14.9 12.25 96.6
08:24 109 19.5 11.95 109.2
08:25 110 19.4 12.85 100.8
08:26 111 15.4 12.25 118.4
08:27 111 15.6 12.55 96.6
08:28 111 15.8 12.15 89.9
08:29 112 15.9 11.75 110.9
08:30 113 16.1 12.15 112.6
08:31 115 16.2 11.95 150.4
08:32 117 16.4 12.05 152.9
08:33 118 16.6 11.85 157.1
08:34 119 16.7 11.85 131.9
08:35 119 16.9 11.75 123.5
08:36 120 17.1 11.85 125.2
08:37 121 17.2 12.05 156.2
08:38 124 17.4 11.85 173.0
08:39 125 17.5 11.95 173.0
08:40 127 17.7 12.15 171.4
08:41 128 17.9 12.25 164.6
08:42 130 18.0 12.35 146.2
08:43 131 18.2 12.35 187.3
08:44 131 18.4 12.55 166.3
08:45 132 18.5 12.55 157.1
08:46 132 18.7 12.75 155.4
08:47 134 18.9 11.95 125.2
08:48 135 19.0 11.95 154.6
08:49 136 19.2 12.75 182.3
08:50 137 19.3 12.35 67.2
08:51 138 19.5 12.85 58.0
08:52 139 19.7 12.95 59.6
08:53 140 19.8 13.05 82.3
08:54 140 20.0 12.95 136.9
08:55 141 20.2 12.95 179.8
08:56 141 20.3 13.25 157.1
08:57 140 20.5 13.65 132.7
08:58 140 20.6 13.35 128.5
08:59 140 20.8 13.25 149.5
09:00 141 21.0 13.45 154.6
09:01 141 21.1 13.45 147.0
09:02 141 21.3 13.45 139.4
09:03 141 21.5 13.45 131.0
09:04 141 21.6 13.55 135.2
09:05 141 21.8 13.45 136.9
09:06 141 21.9 13.55 137.8
09:07 140 22.1 13.55 136.1
09:08 140 22.3 13.55 138.6
09:09 140 22.4 13.55 133.6
09:10 140 22.6 13.65 133.6
09:11 140 22.8 13.75 129.4
09:12 140 22.9 13.85 123.5
09:13 140 23.1 13.75 121.0
09:14 139 23.2 13.95 110.9
09:15 139 23.4 14.05 110.9
09:16 139 23.6 14.15 108.4
09:17 139 23.7 14.15 110.0
09:18 138 23.9 14.35 109.2
09:19 138 24.1 14.55 109.2
09:20 138 24.2 14.75 114.2
JB/DEM0909/15.03.15 /Page23
09:21 138 24.4 14.85 117.6
09:22 138 24.6 15.05 116.8
09:23 137 24.7 15.25 116.8
09:24 137 24.9 15.45 113.4
09:25 137 25.0 15.55 112.6
09:26 137 25.2 15.85 94.9
09:27 136 25.4 16.85 87.4
09:28 135 25.5 17.05 73.9
09:29 134 25.7 15.15 63.0
09:30 134 29.9 15.85 92.4
09:31 136 29.6 16.45 151.2
09:32 135 29.6 12.95 116.8
09:33 134 31.8 14.35 86.5
09:34 134 30.5 15.05 93.2
09:35 134 31.3 13.55 107.5
09:36 134 31.6 13.55 110.0
09:37 134 32.0 14.05 110.9
09:38 134 32.3 13.95 112.6
09:39 134 32.7 13.35 116.8
09:40 135 33.0 13.05 136.1
09:41 135 34.8 13.45 128.5
09:42 135 32.3 13.05 133.6
09:43 136 33.2 13.25 140.3
09:44 136 55.8 13.05 153.7
09:45 137 32.0 13.05 151.2
09:46 138 32.2 12.95 157.1
09:47 138 32.5 13.55 141.1
09:48 138 32.7 13.65 128.5
09:49 138 33.8 12.95 140.3
09:50 140 33.2 12.55 164.6
09:51 141 33.1 13.05 142.8
09:52 140 32.4 13.65 132.7
09:53 140 33.3 13.85 126.8
09:54 140 33.4 14.25 100.0
09:55 140 33.3 13.35 117.6
09:56 141 33.6 12.95 145.3
09:57 142 33.9 13.85 130.2
09:58 143 33.6 14.85 178.1
09:59 145 34.4 13.55 185.6
10:00 145 33.8 11.45 163.8
10:01 145 34.4 11.95 157.9
10:02 146 34.7 12.25 161.3
10:03 146 34.0 12.15 147.0
10:04 145 34.1 12.55 126.0
10:05 146 34.4 12.05 137.8
10:06 146 34.3 11.85 152.9
10:07 147 34.1 11.85 147.0
10:08 146 32.9 12.45 122.6
10:09 146 34.2 11.85 129.4
10:10 146 33.6 12.35 127.7
10:11 146 34.5 12.05 121.8
10:12 146 34.4 12.05 115.9
10:13 145 34.7 12.25 106.7
10:14 145 35.8 11.95 105.0
10:15 145 34.9 12.05 106.7
10:16 145 34.0 12.15 97.4
10:17 145 35.1 12.05 95.8
10:18 145 35.1 12.15 94.9
10:19 144 35.2 12.15 95.8
10:20 144 33.7 12.25 80.6
10:21 143 35.3 12.25 77.3
10:22 143 35.3 12.45 81.5
10:23 143 35.4 12.85 88.2
10:24 142 35.6 13.15 84.8
10:25 142 35.5 13.55 81.5
10:26 142 35.5 13.35 69.7
10:27 141 35.4 13.85 66.4
10:28 141 35.1 13.55 68.0
10:29 140 35.4 14.45 60.5
10:30 140 35.6 13.65 68.9
10:31 140 34.9 14.55 55.4
10:32 140 35.8 13.95 66.4
10:33 139 35.7 13.45 50.4
10:34 139 36.0 14.75 72.2
10:35 139 42.1 12.75 77.3
10:36 138 35.7 13.15 65.5
JB/DEM0909/15.03.15 /Page24
10:37 137 36.7 14.65 50.4
10:38 138 37.5 13.75 73.1
10:39 137 35.8 13.25 58.8
10:40 137 36.0 13.65 55.4
10:41 137 36.1 13.75 58.0
10:42 136 35.2 13.85 55.4
10:43 136 36.1 14.05 52.9
10:44 136 36.2 14.05 54.6
10:45 136 36.0 14.25 65.5
10:46 136 36.2 14.05 68.0
10:47 136 36.9 14.05 77.3
10:48 135 36.2 14.55 78.1
10:49 135 36.1 14.55 79.0
Average 134 27.3 13.30 114.3
JB/DEM0909/15.03.15 /Page25
Parndon Wood Cremators 1 & 2 & Abatement System Outlet
Mercury
Contract Parndon Wood Crematorium, DEM0909
Date 15th March 2016
Location Cremators 1 & 2 Flue Gas Abatement System Outlet
Engineer(s) JBAbsorbent 4% K2CR2O7 / 20% HNO3 in H2O
Test Log
Barometric Pressure(kPa)
Gas Meter Temperature(Deg C)
Oxygen Concentration(%v/v dry)
Flue Gas Volumetric Flow(Nm3/h dry)
Start End
Time 08:14 10:49
Gas Meter Reading(Am3 dry) 81.356 82.549
Absorber Weight(g) 3385.4 3498.1
Filter Reference
Filter Fraction Analysed
Filter(μg as Hg)
Filter Blank(μg as Hg)
Probe Rinse Reference
Probe Rinse Volume(ml)
Probe Rinse(μg/l as Hg)
Probe Rinse Blank(μg/l as Hg)
Absorbent Reference
Absorbent Volume(ml) 250 250
Absorbent(μg/l as Hg) 44 15
Absorbent Blank(μg/l as Hg) 0.5 0.5
Calculation: General
Barometric Pressure(kPa)
Gas Meter Temperature(Deg C)
Gas Volume Sampled(Am3 dry)
Gas Volume Sampled(Nm3 dry)
Mass of Dry Gas(g @ 1292.8 g/Nm3)
Change in Absorber Weight(g)
Water Vapour Volume(Nm3 @ 803.9 g/Nm
3)
Gas Volume(Nm3 wet)
Mass of Wet Gas(g)
Moisture Concentration(%v/v)
Moisture Concentration(%w/w)
0
0
0
1514.71
11.4
7.4
1.2247
1.193
1.0845
1402.01
112.7
1
0.01
0.1402
0.03
PW150316HgF
Washed into HgA
PW150316Hg A+B
101.3
27.3
Hg Test
101.3
27.3
13.30
3387
JB/DEM0909/15.03.15 /Page26
Calculation: Mercury
Filter(μg as Hg)
Probe Rinse(μg as Hg)
Absorbent(μg as Hg)
Total Mercury Sampled(μg)
Mercury Emission(μg/Nm3 dry)
Oxygen Concentration(%v/v dry)
Mercury Emission
(μg/Nm3 @ 11 %v/v Oxygen dry)
Flue Gas Volumetric Flowrate(Nm3/h dry)
Mercury Emission(g/h)
Required Sample Velocity(Nm/s)
Nozzle Used(mm) 4.0
Area of Nozzle(m2) 0.00001257
Test Duration(mins) 155
Actual Sample Velocity(Nm/s) 9.28
Isokinetic Closure(%) 95
9.78
3387
0.046
13.30
17.56
14.63
14.65
13.50
0.00
0.02
JB/DEM0909/15.03.15 /Page27
Parndon Wood Cremators 1 & 2 & Abatement System Outlet
Flue Gas Volumetric Flow
Contract Parndon Wood Crematorium, DEM0909
Date 15th March 2016
Location Cremators 1 & 2 Flue Gas Abatement System Outlet
Engineer(s) JB
Test Log Hg Test
Flue Gas Temperature(Deg C) 134
Flue Gas Pitot Head Sample Points(Pa) 114.3
Flue Gas Moisture(%v/v) 11.4
Flue Gas Moisture(%w/w) 7.4
Flue Gas Duct Dimensions(mm)
Flue Gas Duct Area(m2)
Calculation
Flue Gas Density(kg/m3) 0.8418
Flue Gas Velocity(Am/s) 16.48
Flue Gas Volumetric Flowrate(Am3/h) 5708
Flue Gas Volumetric Flowrate(Am3/h dry) 5055
Flue Gas Volumetric Flowrate(Nm3/h dry) 3387
350 mm Diameter Circular Flue
0.0962
JB/DEM0909/15.03.15 /Page28
Parndon Wood Cremators 1 & 2 & Abatement System
Emissions Monitoring March 2016
Test Instrumentation Calibration Data
Siemens Ultramat 23 Signal 3030PM
CO O₂ VOCDate of Check 15/03/2016 15/03/2016 15/03/2016Time of Check 07:50 07:50 10:55
Hg Test & Hg Test &Tests 1, 2 & 3 Tests 1, 2 & 3
Zero reading at analyser 0 mg/m³ 20.95% 0.1 ppmSpan reading at analyser 519 mg/m³ 0.01% 50.7 ppmZero check down line 0 mg/m³ 20.95% 0.1 ppmSpan check down line 518 mg/m³ 0.03% 50.7 ppmZero reading post test at analyser 0 mg/m³ 20.95% 0.1 ppm
Date of Check 15/03/2016 15/03/2016 15/03/2016Time of Check 15:30 15:30 15:45
Hg Test & Hg Test &Tests 1, 2 & 3 Tests 1, 2 & 3
Zero reading at analyser 0 mg/m³ 20.97% 0.1 ppmSpan reading at analyser 521 mg/m³ 0.01% 50.7 ppmZero check down line 0 mg/m³ 20.97% 0.1 ppmSpan check down line 518 mg/m³ 0.01% 50.7. ppmZero in air post test at analyser 0 mg/m³ 20.98% 0.1 ppm
Calibration Gases
Gas Supplier Cylinder No. Nominal Conc. Certified Conc. AnalyticalTolerance
± %Carbon monoxide in Nitrogen BOC M125970 400 ppm 415 ppm 2Propane in synthetic air BOC M126614 50 ppm 50.7 ppm 2Oxygen Fresh air - 20.95% - -
Tests 1, 2 & 3
Tests 1, 2 & 3Test Reference
Test Reference
JB/DEM0909/15.03.15 /Page29
JB/DEM0909/15.03.15 /Page30
APPENDIX 2
Analysis Reports
JB/DEM0909/15.03.15 /Page31
Particulate Weight Determination
Reference
PW150316FOB 4
PW150316F1 S20
PW150316F2 U1
PW150316F3 U2
PW150316ROB 77.65412 77.65417Rinses
76.88558 76.88645PW150316R1
Clean Dry Weight g Dirty Dry Weight g
0.55133 0.55142
0.5484
0.54018 0.54019
0.54847Filters
0.53893 0.53899
JB/DEM0909/15.03.15 /Page32
JB/DEM0909/15.03.15 /Page33