| Gossman Consulting, Inc |
GCI TECH NOTES©
What follows is a step by step guide to performing a trace metals mass balance. With appropriate modifications, this guide can be used to determine the mass balance of non-metal constituents.
GUIDE FOR PERFORMING A TRACE METALS MASS BALANCE ON A COMBUSTION DEVICE
1. Scope
1.1 The
purpose
of this guide is to provide a procedure to be used to perform a mass
balance
calculation of trace metals entering and leaving a combustion device.
Such
a combustion device may be an incinerator, an industrial furnace or
steam
generation boiler or a heat transfer media heater (such as a direct
fired
hot oil heater). A mass balance calculation aids in determining the
quality
of the analyses of the input and output streams of a combustion device.
Due to analytical imprecision, it may not be possible to demonstrate
that
the input mass of a specific trace metal is equal to the output mass of
this metal. To demonstrate "closure" in a mass balance it must
be shown that the mass input plus or minus the analytical imprecision
overlaps
the range of values of the mass output plus or minus the analytical
imprecision.
By utilizing the appropriate sampling and analytical methods, this
guide
could also be used to determine the mass balance of non-metallic
elements.
1.2 The
units
may be expressed in any format provided they are used consistently for
both the input and output values. Input and output values may be
expressed
as mass per unit time, however the units must be consistent for both
input
and output values; e.g., grams per second or grams per hour, the units
of time must be the same for both input and output values.
1.3
This
guide does not purport to address all of the safety concerns, if any,
associated
with its use. It is the responsibility of the user of this guide to
establish
appropriate safety and health practices and determine the applicability
of regulatory limitations prior to use.
2. Reference
Documents
2.1
These
are covered in Section 7, Test Methods.
3. Terminology
3.1
Description
of terms specific to this guide:
3.1.1
Trace
metals -- any metal consti-tuent that is less than 1% by weight in any
one of the device input or output streams.
3.1.2
Combustion
device -- any device that is intended to convert organic based fuels
into
energy by oxidation. Generally for the purpose of this guide, this is
limited
to combustion devices such as incinerators, industrial furnaces, direct
fired steam generation units or direct fired heat transfer media
heaters.
3.1.3
Mass
balance -- the sum of the inputs into a process (in this case the
combustion
device) of a specific metal are compared with the sum of the outputs
from
the device of that same metal.
3.1.4
Closure
-- when the total mass input of a metal plus or minus the analytical
imprecision
overlaps the ranges of values of the total mass output of that same
metal
plus or minus the analytical imprecision.
3.1.5
Analytical
imprecision -- each analytical method has a determinable level of
imprecision.
Generally this is stated as a percentage of the measured analytical
value.
As an example, SW-846 Method 0060 typically has a QA/QC data quality
goal
of +/-25% of the measured value. The achievement of this goal is
demonstrated
by the QA procedures during the execution of the analytical method.
4. Summary of
Practice
4.1 The
person
wishing to perform a trace metals mass balance on a combustion device
selects
the appropriate sampling and analytical methods which will measure the
targeted trace metals in all of the combustion device inputs and all of
the combustion device outputs. A careful accounting of the mass in each
of the device inputs and outputs must be made over a selected time
period.
This is accomplished by selecting the appropriate sampling point for
each
input and output stream and an appropriate sampling frequency based on
the knowledge of the process, and by measuring the mass input and
output
of each of these streams during the sampling period. The analytical
data
and the mass input and mass output data are used to calculate a range
of
total mass input and total mass output for each of the targeted metals.
A comparison of the range of input versus the range of output values
for
each metal will determine whether a balance has been achieved.
5. Significance of
Use
5.1 A
demonstration
of closure in a mass balance would be indicative of a set of analyses
and
input and output stream rate measurements that adequately characterize
the concentration of the targeted trace metals present in each of the
combustion
device's input and output streams. A failure to demonstrate closure
would
be indicative of a failure to characterize the metal concentration in
one
of the input or output streams or the failure to adequately measure the
rate of an input or output stream or, possibly, the omission or
misidentification
of a stream. Lack of closure can also occur if a metal is retained and
"builds up" within the system and the testing did not allow sufficient
time for the system to reach equilibrium. (For certain cement kiln
designs and some metals, equilibrium may never be reached. Under those
circumstances a different approach is required to determine the lonng
term emission rate and metal balance.)
5.2 A
failure
to characterize the concentration of metal in an input or output stream
may be indicative of an inadequate level of precision in the sampling
and/or
analytical methods. It may also be that the mass input or output rates
have not been adequately measured during the sample period. Either of
these
indications would require an examination of the sampling and analytical
method and their execution, sampling frequency and process input/output
measurements and controls. The successful demonstration of closure of
the
mass balance ultimately rests on the achievable accuracy of the
analyses
and input/output stream measurements. If input and output streams
cannot
be accurately metered, particularly if these streams exhibit wide
variability
in flow rate over the test period, closure of the mass balance is
unlikely.
Steady state operating conditions are generally required for the test
period.
This test period should not closely follow a period of non-steady state
operation. Processes with highly erratic feedrates, process cycling or
highly erratic trace metals concentrations in the input/outputs may
require
an elaborate sampling and analytical plan to achieve closure of the
mass
balance.
6. Procedure
6.1 A
person
knowledgeable of the process should examine each process input and
output
stream and determine the following:
6.1.1
The
accuracy of the measurement of the stream flow rate. The accuracy of this
measurement
should be as good as possible over the test period, but should at least
be no worse than +/-10% of actual.
6.1.2
The
expected variability of the trace metals concentration in the various
input
and outputs must be considered when selecting a sample frequency for
that
stream. More variability in the trace metals concentration will require
more frequent sampling. Alternately, if the stream is highly variable
in
its trace metals concentration and these variable concentrations can be
isolated to discreet volumes, it is possible to sample and analyze
these
volumes separately; either prior to the test if this is an input or
subsequent
to the test if it is an output.
6.1.3
If
very low levels of a trace metal are expected for a stream, there
should
be a consideration of collecting a larger sample than normal or
utilizing
an analytical procedure that achieves a lower detection limit. Either
of
these considerations may affect the sampling method or sampling
location.
6.1.4
Some
input or output streams should be sampled on an advanced or delayed
schedule.
In some cases the only safe sample point of a feed stream may result in
the feed stream entering the device several minutes or more subsequent
to sampling. Or, an output stream may represent the inputs fed to it an
hour or more previous to its sampling. Sampling times must be adjusted
to accommodate such time delays, otherwise the test period will not be
characterized by analyses.
6.1.5
Sample
point selection and sampling method must be considered as a part of the
overall quality of the performance of the mass balance. In addition to
the safety of the person performing the sampling consideration must be
given to how representative a sample from that location is of the
stream.
As an example; is the stream well mixed? Have two or more sub-streams
entered
the stream prior to the sample point? Is the sample likely to be
contaminated
during sample retrieval? This can occur due to the stream being very
hot
or very cold, or being at a location that is dusty. Sampling tools must
be appropriate for the location, but not introduce contaminants into
the
analysis. As an example, a stainless steel sample cup may be the
standard
sampling tool, but such a tool can contaminate the sample with chromium
and/or nickel.
6.2
After
examining all these considerations, a detailed plan is prepared to
specify
the sample points, the sampling method at each point, the schedule for
sample collection at each point, a sample storage and label designation
system and a plan to modify the sampling schedule in the event of test
delays or interruption.
6.3
Prior
to the test period the sample storage materials and sampling tools must
be strategically located. The persons performing the sampling must be
trained
and a sample coordinator designated. A clean, dry location must be
selected
for the cataloging and storage of the samples. Invariably, a stack
emissions
sampling and/or analytical firm must be selected. This firm must
understand
the QA/QC requirements that they are expected to meet and the
importance
of communication of run start and stop times and, in the event of an
interruption,
the start and stop times of any interruption of their sampling due to
any
cause.
6.4 On
the
day of the test, the sampling of the various streams is performed in
accordance
with the sampling plan determined above. Those streams that must be
sampled
prior to the test period must be sampled the appropriate time period in
advance of the start of the stack gas sampling. This requires
coordination
with the stack sampling firm. The sampling schedule is keyed to the
stack
sampling execution. If the stack sampling is interrupted, the
input/output
stream sampling schedule must be altered accordingly. At the end of the
test period after all of the input and output streams have been
collected,
the properly labeled samples are sent for analysis.
6.5 It
is
recommended that the analysis of the samples be periodically monitored.
This is usually done by the sample coordinator. The purpose of this
monitoring
is to ensure that the samples are analyzed prior to their expiration
date,
that the QA/QC checks have been performed as agreed and to spot check
the
data for obvious errors such as misdesignation of sample ID and
mathematical
errors.
6.6 A
sample
trace metals mass balance report is attached.
7. Test Method
7.1
Process
Stream Sampling and Analytical Methods - Process streams such as kiln
feed,
cement dust or incineration fly ash, clinker or bottom ash and fuels
are
sampled utilizing a "grab" sample method and subjected to an
analysis for trace metals utilizing the ASTM E926 Method A.
7.2
Stack
Emissions Sampling and Analytical Methods - Stack emission samples are
collected and analyzed utilizing EPA SW-846 Method 0060.
8. Report
8.1
Once
all of the analytical data is compiled, as well as the input/output
stream
flow rate data, a spreadsheet is constructed. This spreadsheet
calculates
the mass or each targeted trace metal for each input and output stream.
8.1.1
Each
analysis has a stated or determined precision. Generally this is
expressed
as +/-XX%. For each metal in each stream, a minimum and maximum rate is
calculated by multiplying the analytically determined concentration
times
the mass input or output rate according to the following method.
8.1.2
If
the analysis is below the detection limit of the analytical procedure,
the minimum metal mass rate is 0 (zero). The maximum value is the
detection
limit concentration times the mass rate of the stream.
8.1.3
If
the analysis is above the detection limit but below the quantitation
limit,
the minimum metal mass rate is the detection limit times the mass rate
of the stream. The maximum metal mass rate is the quantitation limit
times
the mass rate of the stream.
8.1.4
If
the analysis is above the quantitation limit, the minimum metal mass
rate
is the declared imprecision percent-age subtracted from 100% and the
resultant
times the concentration and that value times the mass rate of the
stream.
(e.g. 75% x conc. x mass rate) The maximum metal mass rate is the
declared
imprecision percentage added to 100% with the resultant multiplied with
the concentration and that value times the mass rate of the stream.
(e.g.
125% x conc x mass rate)
8.1.5
This
is repeated across the various metals and the streams to result in a
minimum
and maximum metal mass for each metal in each input and output stream.
8.1.6
At
this point, it is now possible to create a minimum and maximum input
value
for each targeted metal by summing the minimum values for each metal in
the input streams and the maximum values for each metal in the input
streams.
Perform a similar summing of the minimum and maximum values for the
output
streams.
8.2 For
each
targeted trace metal, there are now two ranges of values, the mass
input
ranging from minimum to maximum and the mass output ranging from
minimum
to maximum. If these ranges overlap when compared, meaning a value of
each
is within the range of values of the other, closure of the mass balance
for that trace metal has been demonstrated.
9. Appendices
9.1
Appendix
"A" - Sample Mass Balance Report
Appendix A Sample Mass Balance Report
| Metals and Chlorine Balance - Test Day 1 | ||||||||||||
| Kiln Feed | Coal | Liquid HWF | Solid HWF | Spike | Total Input | |||||||
| lb/hr | lb/hr | lb/hr | lb/hr | lb/hr | lb/hr | |||||||
| min | max | min | max | min | max | min | max | min | max | min | max | |
| Silver | 0.009109 | 0.086736 | 0.001909 | 0.003181 | 0.106571 | 0.177619 | 7.77E-05 | 0.00013 | 0.117667 | 0.267666 | ||
| Arsenic | 0.164754 | 1.298855 | 0.060931 | 0.101552 | 0.004401 | 0.03488 | 5.07E-05 | 8.45E-05 | 6.185026 | 7.559476 | 6.415163 | 8.994848 |
| Barium | 33.0162 | 55.02701 | 0.726859 | 1.211431 | 13.34337 | 22.23895 | 0.012336 | 0.02056 | 47.09877 | 78.49795 | ||
| Beryllium | 0.39881 | 0.664683 | 0.031382 | 0.052304 | 0.00033 | 0.003488 | 1E-05 | 1.67E-05 | 0.928675 | 1.135047 | 1.359207 | 1.855538 |
| Cadmium | 0.269033 | 0.448388 | 0.005123 | 0.008538 | 0.060923 | 0.101538 | 9.92E-05 | 0.000165 | 6.118846 | 7.478589 | 6.454023 | 8.037219 |
| Chromium | 12.06236 | 20.10393 | 0.207058 | 0.345096 | 1.545022 | 2.575037 | 0.002706 | 0.00451 | 61.67727 | 75.38333 | 75.49441 | 98.4119 |
| Nickel | 4.903397 | 8.172328 | 0.482056 | 0.803427 | 1.060447 | 1.767411 | 0.00512 | 0.008534 | 6.45102 | 10.7517 | ||
| Lead | 1.641003 | 2.735006 | 0.235097 | 0.391828 | 8.971661 | 14.95277 | 0.003661 | 0.006102 | 71.80199 | 87.75798 | 82.65341 | 105.8437 |
| Antimony | 0.161158 | 0.268597 | 0.010892 | 0.018153 | 0.416102 | 0.693504 | 0.000875 | 0.001459 | 0.589028 | 0.981714 | ||
| Selenium | 0 | 0.130212 | 0 | 0.002139 | 0.018259 | 0.030432 | 3.74E-05 | 6.23E-05 | 0.018297 | 0.162846 | ||
| Thallium | 0.111471 | 0.185784 | 0.00646 | 0.010766 | 0 | 0.000304 | 3.68E-07 | 3.51E-06 | 0.117931 | 0.196858 | ||
| Mercury | 0.000955 | 0.012901 | 0.000778 | 0.001296 | 0.004459 | 0.007432 | 1.15E-05 | 1.92E-05 | 0.006203 | 0.021649 | ||
| Chlorine | 18.58496 | 0 | 0.000998 | 5.392125 | 636.7363 | 955.1045 | 0.153375 | 0.230063 | 655.4756 | 960.7266 | ||
| Kiln Dust | Clinker | Stack | System Removal | Total Output | ||||||||
| lb/hr | lb/hr | lb/hr | Efficiency (%) | lb/hr | ||||||||
| min | max | min | max | min | max | min | max | min | max | |||
| Silver | 0.185007 | 0.308345 | 0.044967 | 0.074946 | 0.000872 | 0.001308 | 98.88839 | 99.67422 | 0.230846 | 0.384599 | ||
| Arsenic | 0.68973 | 1.14955 | 3.825957 | 6.376595 | 0.000511 | 0.000766 | 99.98806 | 99.99432 | 4.516198 | 7.526911 | ||
| Barium | 5.229 | 8.715 | 44.09788 | 73.49647 | 0.005557 | 0.008336 | 99.9823 | 99.99292 | 49.33244 | 82.2198 | ||
| Beryllium | 0.104829 | 0.174715 | 0.941583 | 1.569305 | 0 | 5.07E-05 | 99.99627 | 100 | 1.046412 | 1.744071 | ||
| Cadmium | 5.229 | 8.715 | 0.572651 | 0.954419 | 0.01544 | 0.02316 | 99.64115 | 99.80789 | 5.817091 | 9.692579 | ||
| Chromium | 5.3286 | 8.881 | 41.36505 | 68.94176 | 0.003917 | 0.005876 | 99.99222 | 99.99602 | 46.69757 | 77.82863 | ||
| Nickel | 0.62748 | 1.0458 | 5.092995 | 8.488324 | 0.001197 | 0.001796 | 99.97216 | 99.98886 | 5.721672 | 9.53592 | ||
| Lead | 76.443 | 127.405 | 9.763643 | 16.27274 | 0.262133 | 0.3932 | 99.52428 | 99.75234 | 86.46878 | 144.0709 | ||
| Antimony | 0.108813 | 0.181355 | 0.773887 | 1.289811 | 7.23E-05 | 0.000311 | 99.94717 | 99.99264 | 0.882772 | 1.471477 | ||
| Selenium | 0.007935 | 0.066068 | 0 | 0.049481 | 0.013333 | 0.02 | 0 | 91.8123 | 0.021268 | 0.135549 | ||
| Thallium | 0.119769 | 0.199615 | 0.003462 | 0.03296 | 0.002992 | 0.004488 | 96.19437 | 98.48013 | 0.126223 | 0.237063 | ||
| Mercury | 0 | 0.001336 | 0 | 0.006087 | 0.006171 | 0.009256 | 0 | 71.49672 | 0.006171 | 0.016679 | ||
| Chlorine | 733.056 | 1099.584 | 1.603258 | 2.404887 | 21.83613 | 32.7542 | 756.4954 | 1134.743 | ||||
| HCl | 21.65333 | 32.48 | 95.04482 | 97.74615 | ||||||||
| Cl2 | 0.1828 | 0.2742 | 99.95817 | 99.98097 | ||||||||