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Incinerators
AeroPulse has many collectors on incinerators. We’ve listed
these jobs below.
In addition, we’ve met the European code on toxin and
dioxin of 0.1 ng/M3. Our results were 0.006 ng/M3,
a success rate of sixteen times the European code. The data
is included. In addition, we’ve enclosed our results on the elimination
of the affluent from burning of PCB’s at Norlite Corporation in Cohoes,
New York. Again, we’ve enclosed our results. We met the codes on everything
but mercury. We were not asked to remove mercury. Had we been we would
have introduced carbon to the system and this has shown to meet the
codes of mercury by a factor of 4 to 12.
We’ve also included pictures on our portable units which
have been furnished for mobile incineration systems.

Kings College Hospital
England
Measurement of Emissions of
Polychlorinated Dibenzo-p-dioxins
and Polychlorinated Dibenzofurans
From the Clinical Waste Incinerator at Kings College Hospital
29 September 1994
| |
Contents |
Page |
| 1 |
Summary and Introduction |
1 |
| 2 |
Plant Description |
1 |
| 3 |
Measurement Technique |
1 |
| 4 |
Results |
3 |
| |
Appendix: Analytical Report |
1 Summary and Introduction
1.1 Clinical Waste Limited operate a clinical
waste incinerator at Kings College Hospital. TBV Science measured concentrations
of polychlorinated dibenzo-p- dioxins (PCDDs) and polychlorinated dibenzofurans
(PCDFs) emitted from the incinerator on 29 September 1994. The result
of this measurement is reported at the referenced conditions of 273K.
101.3 kPa, dry gas and 11% oxygen. The mass emission rate has also been
reported.
2 Plant Description
2.1 The incinerator is used to burn clinical
waste generated on the hospital site. Combustion may be aided by the
burning of natural gas. Exhaust gases leave the incinerator at a temperature
of about 1100° C and pass through a steam-raising boiler and then
a wet scrubber. The cleaned gases are then discharged through a separate
flue in a multi-flue stack.
2.2 During the period of this site visit, the
plant was reported to be running normally.
3 Measurement Technique
3.1 Sampling was carried out via a standard
4 inch BSP port installed on a horizontal section of flue downstream
of the wet scrubber.
3.2 The method used for sampling is described
in an in-house technical procedure note and conforms to the main procedural
requirements of US EPA Method 23. Gas was extracted from the stack at
a rate of 15 1 min-1 over a period of four hours. PCDDs and
PCDFs contained in particulate matter were collected on a glass fibre
filter and those in the vapour phase were trapped in a glass column
containing XAD-2 absorbent resin maintained at <20° C.
The filter and column had been supplied precleaned by Scientific Analysis
Laboratories, Ltd. and were returned to them for analysis for PCDDs
and PCDFs.
4 Results
4.1 Analysis for PCDDs and PCDFs was carried
out on a combined toluene extract of the filter and the XAD-2
resin. A standard analytical procedure was followed, and the result
quoted is the sum of the concentrations of the PCDDs and PCDFs, weighed
according to their relative toxicities using the so-called toxic equivalent
factors derived by the US EPA, NATO/CCMS and the EC.
4.2 The total concentration of PCDDs and PCDFs
in the emitted gas under Normal conditions of dry gas, temperature 273K
and pressure 101.3 kPa was <0.003 ng/Nm3 at the measured
oxygen concentration of 16.0% which is equivalent to <0.006
ng Nm-3 at 11% oxygen. This corresponds to an emission
rate of <9 x 10-3 ng 5-1.
EXECUTIVE SUMMARY
NORLITE CORPORATION
Cohoes, New York
Norlite Corporation, located in Cohoes, New York, operates
two thermal treatment processes (rotary kilns) to manufacture lightweight
aggregate for the construction industry. The rotary kiln process utilizes
certain Low Grade Fuels (LGF) as substitutes for fossil fuels. This
form of beneficial recycling is known as energy recovery. Both New York
State and Federal regulations require that industrial furnaces which
utilize hazardous waste fuels for energy recovery must conduct comprehensive
emissions tests to establish safe operating limits. These test results
identify operating limits and become part of the facility permit. These
emissions tests must quantify the following critical parameters:
- Destruction and Removal Efficiency (DRE) for Principal Organic Hazardous
Constitutes (POHCs).
- Emission Rates of Acid Gases formed as byproducts of the combustion
process, and removed by the Air Pollution Control System (APCS). Acid
gases principally include hydrogen chloride, sulfur dioxide and oxides
of nitrogen.
- Emission Rates of Particulate Matter, also removed by the APCS.
- Emission rates of 14 regulated metals, contained in the raw aggregate
feed materials and LGF and removed by the APCS.
The results are as follows:
| Table ES-1 |
| Summary
of Key Trial Burn Results |
| Parameter |
Average
Result |
Current
Permit Standard |
Factor
Better Than
(or over) Standard |
| POHC
DRE(1), % for |
|
|
|
| Carbon
tetrachloride |
99.999 |
>99.9900 |
10 |
| -Chlorobenzene |
99.999 |
>99.9900 |
10 |
| -Perchlorethylene |
99.998 |
>99.9900 |
10 |
| -1,1,1
Trichloroethane |
100 |
>99.9900 |
>100 |
| PARTICULATES, |
|
|
|
|
Emission Rate, gr/dscf |
0.0097 |
0.08 |
8.2 |
| ACID
GASES, |
|
|
|
| Emission
Rate, lbs/hour |
|
|
|
| -Hydrogen
Chloride |
1.89 |
4.0 |
2.1 |
| -Sulfur
Dioxide |
12.9 |
30 |
2.3 |
| -Nitrogen
Oxides |
25.7 |
61 |
2.4 |
| REGULATED
METALS
Emission Rates, lbs/hr |
|
|
|
| -
Antimony |
0.00043 |
0.00187 |
4.4 |
| -
Arsenic |
0.000087 |
0.000419 |
4.8 |
| -
Barium |
0.000135 |
0.0135 |
100 |
| -
Beryllium |
<0.000013 |
0.0000655 |
5.0 |
| -
Cadmium |
0.000260 |
0.000289 |
1.1 |
| -
Chromium (V1) |
0.0000205 |
0.0000750 |
3.7 |
| -
Copper |
0.000306 |
0.0375 |
122 |
| -
Lead |
0.000116 |
0.0214 |
185 |
| -
Mercury |
0.0281 |
0.00168 |
(16.7) |
| -
Nickel |
0.00305 |
0.0271 |
8.9 |
| -
Selenium |
0.000149 |
0.000939 |
6.3 |
| -
Silver |
<0.000046 |
0.000769 |
17 |
| -Thallium |
0.0000296 |
0.000769 |
26 |
| -
Zinc |
0.00275 |
0.0390 |
14 |
| (1)
DRE-Destruction and Removal Efficiency |
| Table 2.1-39 |
| Calculation
of Air Pollution Control System Removal Efficiencies |
| |
CONDITION
B |
CONDITION
D |
| Constituent |
Kiln
Feed
Rate,
LBS/Hr |
Emission
Rate,
LBS/Hr |
APCS
Removal
Efficiency,
% |
Kiln
Feed
Rate,
LBS/Hr |
Emission
Rate,
LBS/Hr |
APCS
Removal
Efficiency
% |
| Chlorine |
428.11 |
2.23 |
99.47911 |
438.01 |
2.67 |
99.39042 |
| METALS |
|
|
|
|
|
|
| Antimony |
0.3553 |
0.000189 |
99.94681 |
0.3652 |
0.000567 |
99.84474 |
| Arsenic |
0.3926 |
1.88E-05 |
99.99521 |
0.3926 |
5.88E-05 |
99.98502 |
| Beryllium |
0.0451 |
1.25E-05 |
99.97228 |
0.0418 |
1.28E-05 |
99.96038 |
| Barium |
4.651 |
0.000102 |
99.99781 |
4.2756 |
0.000116 |
99.99729 |
| Cadmium |
0.348 |
0.000289 |
99.91695 |
0.3564 |
0.000168 |
99.95286 |
| Chromium (V1) |
5.5722 |
1.1E-05 |
99.9998 |
5.4038 |
1.05E-05 |
99.99981 |
| Copper |
7.6641 |
0.000281 |
99.99633 |
7.9814 |
0.000101 |
99.99873 |
| Lead |
3.6187 |
0.000149 |
99.99588 |
3.7983 |
0.000101 |
99.99734 |
| Mercury |
0.1297 |
0.0328 |
74.71087 |
0.1337 |
0.0289 |
78.38444 |
| Nickel |
4.9896 |
0.00376 |
99.92464 |
5.0713 |
0.00344 |
99.93217 |
| Selenium |
0.1633 |
0.000511 |
99.68708 |
0.1701 |
2.56E-05 |
99.98495 |
| Silver |
0.1658 |
4.67E-05 |
99.97183 |
0.1754 |
4.49E-05 |
99.9744 |
| Thallium |
0.2992 |
2.04E-05 |
99.99318 |
0.3831 |
3.21E-05 |
99.99162 |
| Zinc |
8.9969 |
0.00212 |
99.976-44 |
12.438 |
0.00148 |
99.9881 |
| Average
(exc. Hg) |
99.95187 |
|
|
99.97049 |
NOTE;
APCS REMOVAL EFFICIENCY - (KILN FEED RATE FOR CONSTITUENT - EMISSION
RATE)
x 100 / KILN FEED RATE |
| PARTIAL
INCINERATOR LIST |
|
ACFM |
Description |
| 18,000 |
|
Collects
hazardous waste particulate, followed with wet scrubber that gets
the acid from the gas. |
| 10,560 |
|
This
is a system with our baghouse being used for dry lime injection |
| 8,100 |
|
System
with our unit only for dry lime. No wet scrubber included. |
| 4,300 |
|
Hospital
waste - Dry injection system without scrubber backup. |
| 62,000 |
|
Hazardous
waste from burning hazardous liquid with high HCL in kiln. |
| 15,000 |
|
Collects
effluent from a medical waste incinerator |
| 15,000 |
|
Collects
effluent from a medical waste incinerator |
| 13,000 |
|
Medical
Waste Incinerator. Unit includes Ca(OH)2 injection system
and silo |
| 5,000 |
|
Medical
Waste Incinerator - Unit includes Ca(OH)2 injection system
and silo. |
| 9,000 |
|
Incinerator
Effluent - Collector Only |
| 3,000 |
|
Medical
Waste Incinerator - Unit includes Ca(OH)2 injection system
and silo. |
| 5,000 |
|
Medical
Waste Incinerator - Unit includes Ca(OH)2 injection system
and silo |
| 100,000 |
|
Two
portable baghouses combined into a single system to decontaminate
soil. |
| 62,000 |
|
Hazardous
waste from burning hazardous liquid with high HCL in kiln. |
| 12,500 |
|
Portable
baghouse system decontaminating soil with high hydrocarbon levels.
Followed by an afterburner. |
| 16,000 |
|
Portable
baghouse system cleaning sand with hydrocarbons and trace chlorides.
Followed by an afterburner |
| 12,500 |
|
Portable
baghouse system - soil remediation. |
| 18,000 |
|
Baghouse
only in London meeting the new European Codes |
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