GCI TECH NOTES©
Volume 9, Number 2 A Gossman Consulting, Inc. Publication April 2004
by
David Constans,
Gossman Consulting, Inc.
In Section VIII
D of the Proposed Standards for Hazardous Air Pollutants of Hazardous
Waste
Combustors (Phase I Final Replacement Standards and Phase II) the EPA
is
proposing the new standards to limit emissions of semi-volatile metals
(SVM). Section VIII E then proposes the
new
standards to limit emissions of low-volatile metals (LVM).
See Federal Register for Tuesday, April 20,
2004, page 21248.
These two
sections propose to limit SVM and LVM input rates tied to the heat
content of
the hazardous waste fuel. What impact will this rule change have on
cement
kilns? The incinerators, solid fuel
fired boilers and hydrochloric acid production furnaces do not have
such a
requirement. Why not?
GCI has a
waste fuel input calculator that will calculate the maximum allowable
concentration of the SVM or LVM for existing and new facilities based
on the
heat content of the fuel and the facility’s system removal efficiency. Go to this page to access the
calculator. If you would like a copy of this
calculator as an Excel
spreadsheet give us a call or send an e-mail to dgossman@gcisolutions.com. The table illustrates the impact of the
proposed regulation.
Assuming a
SVM SRE of 99.0% and a LVM SRE of 99.9% the maximum allowable
concentration of
the metals in the HWF is shown in the following table.
Note how the allowable concentration
decreases with heat content.
|
|
Maximum Allowable Concentration in HWF,
expressed as ppm by weight |
|
|
Heat Content BTU/lb. |
SVM |
LVM |
|
5000 |
200 |
70 |
|
7000 |
280 |
98 |
|
9000 |
360 |
126 |
|
10000 |
400 |
140 |
Certainly,
these SRE’s are lower than many of the kilns have established. However, some kilns have not been rigorous
in the establishment of SRE values and have relied on maximum metal
input rates
established during trial burns to set metal feed rate limits not SRE’s. Remember the facility will have a total and
liquid HWF feed rate limit as before.
Metals
concentrations do not generally decrease with decreasing heat content. Waste minimization requirements cause
generators to reduce volatile organic components in their wastes, which
increase the solids concentrations in the waste and consequently the
metals
concentration in the waste. It is not a
hard and fast rule but certainly a concept well known and well
understood by
the industry and the EPA. This is less
of a problem for liquid wastes than for solid wastes.
The way this rule is written cement kilns that feed low heat
content solids may have to restrict their generator base to ensure
having the
correct metal/heat content ratio in the fuel they burn.
If this is an important criterion in
hazardous waste fuels emissions control why are incinerators and solid
fuel
boilers exempted from this requirement?
In the past,
under BIF and the current HWF, if the waste fuel in the facility had a
high
concentration of a particular metals such that the facility could not
feed at
its maximum allowable rates it could feed at a lower rate.
Under the proposed rule, the facility will
have to blend this high metal concentration fuel with other fuels to
achieve
the proper metals/heat content ratio.
The question that immediately comes to mind is, why? This is not required of incinerators. It is not an emissions control scheme that
is superior to the current requirements.
There are already state permits issued based on the current
control
scheme in the HWC MACT requirements.
Will these permits be voided?
What about kilns that utilize non-hazardous wastes and
substitute raw
materials that have significant quantities of regulated metals? How will the states and the EPA address
those kiln’s permit requirements?
GCI sees
three events resulting from EPA’s proposed changes in the regulation:
1.
Some
wastes will be sent to incinerators instead of cement kilns,
lightweight
aggregate kilns or liquid fired boilers because the correct metals/heat
content
ratio can not be met economically and these devices will not be allowed
to burn
these wastes even at a very low feed rate.
This is bad for the cement kilns economically and bad for the
environment. Any waste burned in an
incinerator without a heat recovery system versus an industrial furnace
means
that more fossil fuel must be consumed and more carbon dioxide
generated in the
US each year (a concept EPA never discusses).
2.
The
price differential for having waste burned in a commercial incinerator
versus
an approved and permitted industrial furnace can be substantial. This proposed regulation would discourage
waste minimization efforts by generators.
The industrial furnaces mindful of the metals/heat content ratio
will
charge more for high concentration/low heat content wastes. The generator seeing his disposal costs
increasing as he minimizes his waste generation will certainly think
twice
about any further waste minimization efforts.
3.
This
change in the EPA’s approach to metals emissions control for industrial
furnaces will result in considerable expense and time.
Not only in lost customers, but in redesign
of control and monitoring schemes, as well as fixing the permits to
reflect the
new regulations. None of this will
improve the environment! Indeed the end
result is likely to be increased carbon dioxide emissions.
For cement
kilns, the EPA assumes that since these industrial furnaces do not do
anything
specific (i.e., carbon absorption or chemical scrubbing) to capture and
reduce
mercury emissions, that the SRE for mercury is proclaimed by EPA to be
zero. The EPA is going to have to have
a talk with the state of Texas. They
issued an adjudicated permit to TXI that recognizes a significant
mercury SRE.
In Section
VIII B in the proposed regulation, it states: “Given that no cement
kilns
burning hazardous waste use a control device which captures mercury
from the
flue gas streams, for purposes of this analysis, we assumed all sources
achieved a SRE of zero. The effect of
that assumption is that the sources with the lowest mercury
concentrations in
the hazardous waste were identified as the best performing sources”. This is a serious design flaw in the
EPA’s regulation.
By EPA’s own
text, this statement is refuted on the same page, 2 paragraphs down. “We did not use the stack emissions data
of preheater/ precalciner kilns in the floor analysis because we
believe the
mercury emissions are biased low when the in-line raw mill is
on-line
and biased high when the in-line raw mill is off-line”. (Emphasis
added)
The EPA does
not offer a reason for its ascribing this data as biased and
hence all of it being discounted. Could
an explanation for this phenomenon be that when the raw
mill is on-line the raw feed “captures mercury from the flue gas
stream”? The fact that the mercury is
subsequently
scrubbed from the recycled raw feed material when the raw mill is
off-line was
clearly the reason the EPA wanted the kilns tested in both the raw mill
on-line
and raw mill off-line modes. Now the
EPA discounts the data as biased.
Clearly, the raw feed is removing the mercury from the flue gas
stream. This fact does not support
EPA’s purpose, however, so the data is ascribed to be biased and so
discounted.
Since the
cement kilns had no reason to ensure that the mercury was not scrubbed
from the
recycled dust during the raw mill off-line period, they did not do so. They met the emissions limit using the
prescribed method. If however, the
cement kilns had had a need to reduce their mercury emissions to meet
the
standard, they could have removed recycled dust from the system to
reduce the
mercury in the raw feed fed to the kiln during periods when the raw
mill was
off. In which case, the mercury
emissions during the raw mill off-line period would not have been
“biased high”
as EPA ascribes those values to be.
Clearly, this is a case where the regulated community is being
punished
for complying with the regulations.
As noted
previously, TXI has a state permit that recognizes a substantial SRE
for mercury. Technically cement kilns do
not “use a
control device which captures” any metal “from the flue gas stream”. So why has EPA focused on this concept for
mercury only? Indeed mercury is not
generally captured well by the usual cement production process, but
some kilns
have or could possibly do so if need be.
By proclaiming that an SRE for mercury will be zero the EPA
closes off
any efforts by cement facilities to even attempt to reduce mercury
emissions by
making adjustments in its process operations.
In addition, by proclaiming an SRE of zero for cement kilns, the
reported emissions will be increased when in actual fact they have not. This will give the environmental groups more
reason to attack waste burning cement kilns.
GCI sees
three events resulting from this mercury emissions control regulation:
1.
Cement
kilns will have to restrict the amount of waste containing mercury even
though they could achieve the
emission standard if
they
were allowed to
utilize
a documented SRE greater than EPA’s proclaimed zero SRE. These wastes could possibly be disposed of
at incinerators or solid waste fuel boilers.
(Though this later option is highly unlikely as the maximum
allowable
metals emission rate for solid waste fuel boilers is less than 1/6 of
that for
cement kilns.) Disposal at incinerators
for these wastes as noted before is likely to increase carbon dioxide
emissions
in the US.
2.
As
noted above some cement kilns have already been issued permits that
document a
significant SRE for mercury and allow mercury feed rates that would be
greater
than that allowed by the proposed regulation.
The efforts to reconcile these permits with the proposed
regulation will
entail a significant cost to both the states and the cement facilities
for no
discernable improvement in mercury emissions control.
A cost that incinerators will not be subject to.
3.
Incinerators
are allowed twice the emissions rate per dscm for mercury versus cement
kilns. This regulation will shift more
mercury to those devices. Has the EPA
examined the effect of this increase in mercury feed rates at these
incinerators?
Clearly these
proposed regulations favor incinerators at the expense of industrial
furnaces
and the environment as a whole. There
is no other justification for how these regulations are written. The EPA is calling for comments on these
proposed regulations. This proposed
regulation was published April 20, 2004.
The EPA must receive comments by July 6, 2004.
GCI is
offering its services to help your company respond to this request for
comments. GCI will be glad to assist
you in addressing these issues or other issues more specific to your
facility. Please contact us at
847-683-4188 or by e-mail to dgossman@gcisolutions.com.
onsulting, Inc. 45W962 Plank Road ● Hampshire, IL 60140 ●
(847) 683-4188 ● Fax: (847) 683-4212 http://gcisolutions.com GCI Tech Notes is edited by David Gossman. This issue was
authored by David Constans, constans@gcisolutions.com