[Federal Register: December 8, 2006 (Volume 71, Number 236)]
[Notices]
[Page 71206-71208]
[DOCID:fr08de06-142]

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SECURITIES AND EXCHANGE COMMISSION

[Release No. 34-54855; File No. SR-DTC-2006-15]

Self-Regulatory Organizations; The Depository Trust Company;
Notice of Filing of a Proposed Rule Change Relating to the Canadian
Link Service

December 1, 2006.
    Pursuant to Section 19(b)(1) of the Securities Exchange Act of 1934
(``Act'') \1\ and Rule 19b-4 thereunder,\2\ notice is hereby given that
on October 10, 2006, The Depository Trust Company (``DTC'') filed with
the Securities and Exchange Commission (``Commission'') the proposed
rule change as described in Items I, II, and III, below, which Items
have been prepared by DTC. The Commission is publishing this notice to
solicit comments on the proposed rule change from interested persons.
---------------------------------------------------------------------------

    \1\ 15 U.S.C. 78s(b)(1).
    \2\ 17 CFR 240.19b-4.
---------------------------------------------------------------------------

I. Self-Regulatory Organization's Statement of the Terms of Substance
of the Proposed Rule Change

    The proposed rule change would amend DTC's Rule 30, Canadian-Link
Service, to allow certain Canadian-Link transactions to settle in U.S.
dollars.

II. Self-Regulatory Organization's Statement of the Purpose of, and
Statutory Basis for, the Proposed Rule Change

    In its filing with the Commission, DTC included statements
concerning the purpose of and basis for the proposed rule change and
discussed any comments it received on the proposed rule change. The
text of these statements may be examined at the places specified in
Item IV below. DTC has prepared summaries, set forth in sections A, B,
and C below, of the most significant aspects of such statements.

A. Self-Regulatory Organization's Statement of the Purpose of, and
Statutory Basis for, the Proposed Rule Change

    DTC's Canadian-Link Service currently allows participants of DTC
(``DTC Participants'') to clear and settle two categories of securities
transactions in Canadian dollars: (1) Transactions with participants of
The Canadian Depository for Securities Limited (``CDS Participants'')
and (2) transactions with other DTC Participants. The Canadian-Link
Service also allows DTC Participants to transfer Canadian dollar funds
to CDS Participants through the

facilities of CDS and to other DTC Participants through Canadian
settlement banks acting for DTC and such DTC Participants. The proposed
rule change would add an additional functionality to the Canadian-Link
Service to allow DTC Participants to settle certain securities
transactions with CDS Participants in U.S. dollars (``cross-border U.S.
dollar securities transactions''). Set forth below is a description of
the current Canadian-Link Service and a description of the proposed
change.
Current Functionality of the Canadian-Link Service
    The Canadian-Link Service allows DTC Participants to clear and
settle valued securities transactions in Canadian dollars with CDS
Participants through the link between DTC and CDS. The securities that
may be the subject of these transactions are securities that are
eligible for book-entry transfer through the facilities of CDS and DTC
(``Full-Service Canadian-Link Securities'') and securities that are
eligible for book-entry transfer through the facilities of CDS but not
through DTC (``Limited Service Canadian-Link Securities''). The
securities are delivered to and from CDS Participants through the
facilities of CDS. Money settlement between DTC and CDS is included in
Canadian dollar money settlement at CDS. Money settlement between DTC
and DTC Participants takes place between Canadian settlement banks
acting for DTC and such DTC Participants.
    The Canadian-Link Service allows DTC Participants to clear and
settle valued transactions in Canadian dollars with other DTC
Participants through the facilities of DTC. The securities that may be
the subject of these transactions are Full-Service Canadian-Link
Securities. The securities are delivered to and from DTC Participants
through the facilities of DTC. Money settlement between DTC and DTC
Participants takes place through Canadian settlement banks acting for
DTC and such DTC Participants.
    The Canadian-Link Service allows DTC Participants to transfer
Canadian dollar funds without any corresponding delivery or receipt of
securities to CDS Participants or other DTC Participants. Transactions
between DTC Participants and CDS Participants are processed through the
facilities of CDS. Transactions between DTC Participants and other DTC
Participants are processed through Canadian settlement banks acting for
such DTC Participants.
    The proposed rule change would not change any of the existing
components of the Canadian-Link Service and except for cross-border
U.S. dollar securities transactions, as set forth below, would not
change how securities transactions are currently processed through the
Canadian-Link Service.
Proposed Enhancement of the Canadian-Link Service
    The proposed rule change would enhance the Canadian-Link Service to
allow DTC Participants to clear and settle certain valued securities
transactions in U.S. dollars with CDS Participants through the link
between DTC and CDS.\3\ The securities that would be the subject of the
enhancement are Limited-Service Canadian-Link Securities, i.e.,
securities that are eligible for book-entry transfer through the
facilities of CDS but not DTC. The securities would be delivered to and
from CDS Participants through the facilities of CDS. Money settlement
between DTC and CDS would be included in U.S. dollar money settlement
at DTC. Money settlement between DTC and DTC Participants would also be
included in U.S. dollar money settlement at DTC together with the
settlement of DTC Participants' other transactions at DTC. As the
foregoing indicates, these cross-border U.S. dollar securities
transactions would be processed in substantially the same way that
transactions are now processed except that these transactions would
settle in U.S. dollars rather than in Canadian dollars and the place of
money settlement will be at DTC rather than at CDS or through Canadian
settlement banks.
---------------------------------------------------------------------------

    \3\ DTC has represented to the Commission that some transactions
executed in Canadian markets, either on a stock exchange or over-
the-counter, are settled in U.S. dollars. Transactions that settle
in U.S. dollars would be reported to DTC in U.S. dollar amounts. DTC
would not convert settlement amounts from Canadian to U.S. dollars.
---------------------------------------------------------------------------

    The proposed rule change would also add new definitions to DTC Rule
30 to distinguish between transactions between DTC Participants and CDS
Participants (``Cross-Border Securities Transactions'') and
transactions between only DTC Participants (``Intra-DTC Securities
Transactions''). The proposed rule change would also add new
definitions to distinguish between transactions that settle in U.S.
dollars and transactions that settle in Canadian dollars (for example,
``Cross-Border CAD Securities Transactions'' and ``Intra-DTC USD
Securities Transactions'').
Risk Management Controls
    Set forth below is a description of DTC's risk management controls
with respect to the Canadian-Link Service and how these risk management
controls would be affected as a result of the proposed rule change.
    1. Canadian-Link Required Participants Fund Deposit. A DTC
Participant that uses the Canadian-Link Service is currently required
to make an additional required deposit to the DTC participants fund
that is determined in accordance with a formula that takes into account
the volume of cross-border Canadian dollar securities transactions
processed by DTC for such DTC Participant. Under the proposed rule
change, such formula would also take into account the volume of cross-
border U.S. dollar securities transactions processed by DTC for such
DTC Participant.
    2. Security for Canadian-Link Transactions. A DTC Participant that
uses the Canadian-Link Service is currently required to pledge to DTC
its interest in the securities subject to cross-border Canadian dollar
securities transactions that are held by DTC for such DTC Participant
at CDS. Under the proposed rule change, such DTC Participant will also
be required to pledge to DTC its interest in the securities subject to
cross-border U.S. dollar securities transactions that are held by DTC
for such DTC Participant at CDS.
    3. Canadian-Link Service Net Debit Caps. A DTC Participant that
uses the Canadian-Link Service is currently subject to a net debit cap
on the negative Canadian dollar balance that may, from time to time, be
incurred by such DTC Participant with respect to its use of the
Canadian-Link Service. Under the proposed rule change, a DTC
Participant would also be subject to a net debit cap on the negative
U.S. dollar balance that may from time to time be incurred by such DTC
Participant with respect to its cross-border U.S. dollar securities
transactions. The proposed rule change would add new definitions to DTC
Rule 30 to take into account that there would be separate Net Debit
Caps for U.S. and for Canadian dollar transactions.
    4. Collateral Monitor of Canadian-Link Participants. A DTC
Participant that uses the Canadian-Link Service is currently subject to
the DTC collateral monitor with respect to its use of the Canadian-Link
Service. Under the proposed rule change, a DTC Participant would also
be subject to the DTC collateral monitor with respect to its cross-
border U.S. dollar securities transactions.
    As the foregoing indicates, cross-border U.S. dollar securities
transactions will be subject to essentially the same robust risk
management controls that are already

applicable to the other securities transactions currently processed
through the Canadian-Link Service.
Statutory Basis for the Proposed Rule Change
    Section 17A(a)(3)(F) of the Act requires that the rules of a
registered clearing agency be designed to promote the prompt and
accurate clearance and settlement of securities transactions and to
assure the safeguarding of securities and funds which are in its
possession or control or for which it is responsible. The proposed
enhancement to the Canadian-Link Service should promote the prompt and
accurate clearance and settlement of cross-border securities
transactions between DTC Participants and CDS Participants and between
DTC Participants and other DTC Participants in a secure, efficient, and
regulated environment.

B. Self-Regulatory Organization's Statement on Burden on Competition

    DTC does not believe that the proposed rule change will impose any
burden on competition.

C. Self-Regulatory Organization's Statement on Comments on the Proposed
Rule Change Received From Members, Participants, or Others

    No written comments relating to the proposed rule change have been
solicited or received by DTC from members, participants, or other
persons. DTC will notify the Commission of any written comments it
receives.

III. Date of Effectiveness of the Proposed Rule Change and Timing for
Commission Action

    Within thirty five days of the date of publication of this notice
in the Federal Register or within such longer period (i) as the
Commission may designate up to ninety days of such date if it finds
such longer period to be appropriate and publishes its reasons for so
finding or (ii) as to which the self-regulatory organization consents,
the Commission will:
    (a) By order approve the proposed rule change or,
    (b) Institute proceedings to determine whether the proposed rule
change should be disapproved.

IV. Solicitation of Comments

    Interested persons are invited to submit written data, views, and
arguments concerning the foregoing, including whether the proposed rule
change is consistent with the Act. Comments may be submitted by any of
the following methods:

Electronic Comments

     Use the Commission's Internet comment form (http://www.sec.gov/rules/sro.shtml.
); or     Send an e-mail to<EMAIL_ADDRESS>Please include

File Number SR-DTC-2006-15 on the subject line.

Paper Comments

     Send paper comments in triplicate to Nancy M. Morris,
Secretary, Securities and Exchange Commission, 100 F Street, NE.,
Washington, DC 20549-1090.

All submissions should refer to File Number SR-DTC-2006-15. This file
number should be included on the subject line if e-mail is used. To
help the Commission process and review your comments more efficiently,
please use only one method. The Commission will post all comments on
the Commission's Internet Web site (http://www.sec.gov/rules/sro.shtml
). Copies of the submission, all subsequent amendments, all

written statements with respect to the proposed rule change that are
filed with the Commission, and all written communications relating to
the proposed rule change between the Commission and any person, other
than those that may be withheld from the public in accordance with the
provisions of 5 U.S.C. 552, will be available for inspection and
copying in the Commission's Public Reference Room. Copies of the filing
also will be available for inspection and copying at the principal
office of DTC. All comments received will be posted without change; the
Commission does not edit personal identifying information from
submissions. You should submit only information that you wish to make
available publicly. All submissions should refer to File Number SR-DTC-
2006-15 and should be submitted on or before December 29, 2006.

    For the Commission, by the Division of Market Regulation,
pursuant to delegated authority.\4\
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    \4\ 17 CFR 200.30-3(a)(12).
---------------------------------------------------------------------------

Florence E. Harmon,
Deputy Secretary.
 [FR Doc. E6-20868 Filed 12-7-06; 8:45 am]

BILLING CODE 8011-01-P


316B RULE

 TELEPHONE LOG

Name of Caller: 	John Sunda, SAIC

Date: 	January 15, 2010

Company Name: 	SPX Cooling Technologies, Inc.

Street Address:	7401 W 129 Street

City/State/ZIP:	Overland Park, KS 66213

Person Contacted:	Kent A. Martens, P. E.

Title:	Chief Technical Advisor - Evaporative Cooling

Contact Info:	Tel:      913/664-7501

	Fax:     913/693-9522

	Cell:     913/302-7234

<EMAIL_ADDRESS>
Questions:  Inquired about plume and noise abatement cooling towers
including questions about operating problems cited by others with the
plume abated towers at Newington Energy Facility

The Newington plume abatement cooling tower is an obsolete cooling tower
design called “Clear Flow” that they no longer sell.  The dry
cooling portion of this design used corrugated PVC sheets with air and
water flowing between alternating sheets. He was not sure of the problem
but thinks it involved some leaking of cooling water in this part of the
system. This design of corrugated PVC sheets and alternating flow is
somewhat similar in design to their new Clear Skies technology but in
this case the alternating flow is ambient air and wet cooling exhaust.
This technology was originally designed as a water conservation
technology but has demonstrated an ability to function as plume
abatement as well.  He agreed that it may take some time for this
technology to acquire more public acceptance.  They have performed a
successful full scale demonstration in New Mexico.

Regardless, they do have plume abatement towers that use conventional
coils that are suitable for saltwater applications. He suggested they
would need to be constructed using high grade stainless steel or
titanium.

I asked about cycles of concentration for saltwater systems and he said
that typically they operate in the range of 1.3 to 1.7. I mentioned that
the Newington NPDES permit fact sheet indicated that the tower could
operate at a COC of 2.0 and he said that 2.0 was possible but it was
pushing the limit.

Regarding increased energy usage for plume abatement – although the
dry coils are higher than the wet tower spray nozzles, once the system
fills up with water the head loss is primarily due to friction losses
and the increase in pumping head will range from 5 to 10 ft with 8 ft
being a typical value.  There will also be a slight fan energy increase
on the order of about 5 to 10%.  This is due to the fact that the system
needs to account for some damper air leakage. Dampers are used to close
off the dry cooling coil portion in winter when it is not needed.   He
said that an increase in capital costs for a plume abated tower of 2.5
to 3.5 can be expected.

Regarding the ability to use plume abatement in back-to-back
configurations, it isn’t that it can’t be done but rather that since
the coils must be placed in a vertical configuration, it is difficult to
get full mixing of the dry cooling airflow coming in on one side with
the wet cooling airflow. So you don’t get sufficient dryer airflow
mixing towards the back side resulting in partial plume abatement (i.e.
only front half of plume is fully abated).

Regarding noise attenuation, he though that a 10% increase in capital
costs might be low especially if the noise abatement requirements are
aggressive. I suggested an aggressive design target of 50 dBA at 500 ft.
He did a quick calculation of an 18 cell back-to-back tower showing the
non-abated design producing 63.3 dBA at 500 ft and the same abated tower
producing 47 dBA at 500 ft using numerous additional features resulting
in nearly double the cost of the towers.  I requested that he provide me
with some design and cost estimates for comparable towers with different
features including aggressive noise abatement, moderate noise, and plume
abatement.

Some noise abatement points he made:

Noise abatement requires a sophisticated analysis by a specialist.

Some of the additional technologies may only be necessary on one side of
the tower limiting costs.

Low noise fans can cost orders of magnitude more than conventional fans

Barrier walls work well for close up receptors but not as well for far
off receptors

They have an array of technologies such as splash baffle, inlet and
outlet attenuators, aluminum frame baffles, etc.

Follow-up on May 5, 2010

Inquired about degree of increase in O&M costs for plume abatement. I
said that my calculations showed a total fan & pump power increase of
about 15% and he said that would be a reasonable estimate. I noted that
our cooling tower and basin capital costs were about $80/gpm. He said
that his quick calculation was $40/gpm but if you included installation,
controls, mechanical & electrical equipment that this figure was
reasonable. I then noted that using a factor of 2.5 resulted in a
capital cost increase of $200/gpm for plume abatement..

I then noted that O&M costs for conventional towers was often cited as
1%-2% and that our EPA cost estimate includes about $1.25/gpm (about
1.5% of $80) for non-power maintenance and another $1.25 for chemicals
to operate at high COC.  He said that there would also be an increase in
non-power O&M costs due to the larger tower and maintenance of coils and
dampers. He said a 50% to 100% increase in the non-power O&M over that
for the conventional tower would be reasonable.


9.0pt'>EPA-HQ-OAR-2002-0083-0007 <o:p></o:p>

Settlement in the United States Court of Appeals for the District of
  Columbia Circuit in the Matter of AK Steel Corporation vs. USEPA, Case #
  03-1207 <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0008 <o:p></o:p>

Letter to Steve Fruh, USEPA,/Office of Air Quality, Planning &
  Standards/Emission Standards Division from John L. Wittenborn and Russell S.
  Frye, Collier Shannon Scott PLLC re: MACT Standards <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0009 <o:p></o:p>

Petitioners' Preliminary and Non-Binding Statement of Issues to be
  Raised <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0010 <o:p></o:p>

Email to Marvin Branscome, USEPA/RTI from Jim R. Carson re: VEE
  monthly summaries <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0011 <o:p></o:p>

Email to Marvin Branscome, RTI International from Jim Carson re:
  Sinter Plant <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0012 <o:p></o:p>

Attendance List for October 22, 2003 Meeting of USEPA and Steel
  Industry Litigants. <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0013 <o:p></o:p>

Letter to Steve Fruh, USEPA, Office of Air Quality Planning and
  Standards/Emission Standards Division from Bruce A. Steiner, Collier Shannon
  Scott PLLC re: Iron & Steel MACT (Maximum Achievable Control Technology)
  rule <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0014 <o:p></o:p>

Letter to Steve Fruh, USEPA from Rich Zavoda, ISG Cleveland Inc., re:
  Iron and Steel MACT (Maximum Achievable Control Technology)/NESHAP (National
  Emissions Standards for Hazardous Air Pollutants) Discussions <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0015 <o:p></o:p>

Discussion Paper on Performance Test-Based Opacity Limits in the Iron
  & Steel MACT (Maximum Achievable Control Technology) Rule <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0016 <o:p></o:p>

Notes from telephone conversation between Steve Fruh, USEPA, Metals
  Group; Phil Mulrine, USEPA. Metals Group; Steve Silverman, USEPA, Office of
  Genera Counsel; Andy Doyle, US Department Justice; Marvin Branscome, RTI;
  Bruce Steiner, Collier Shannon; Rich Zavoda, International Steel Group; Mike
  Long, International Steel Group; Tom Shepker, WCI Steel; Matthew Scherschel,
  Ispat Intland et al. <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0017 <o:p></o:p>

Proposed Alternative to Iron & Steel MACT (Maximum Achieveable
  Control Technology) Performance Test-Based Opacity Limits <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0018 <o:p></o:p>

Iron and Seel MACT (Maximum Achievable Control Technology) Standard
  for BOF ESP Conceptual Draft - COMS Corrective Action Trigger <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0019 <o:p></o:p>

Settlement of Iron & Steel MACT (Maximum Achievable Control
  Technology) Issues <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0020 <o:p></o:p>

Email to Steve Fruh, USEPA and Phil Mulrine, USEPA from Bruce Steiner,
  Collier, Shannon, Scott, PLLC re: proposed Iron and Steel MACT (Maximum
  Achievable Control Technology) Revisions <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0021 <o:p></o:p>

Memorandum to USEPA/Docket OAR from USEPA/OAQPS/ESD re: Estimate of
  Savings in Monitoring Costs <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0022 <o:p></o:p>

Memorandum to USEPA/Docket OAR from USEPA/OAQPS/ESD re: Opacity Limit
  for Sinter Coolers <o:p></o:p>

09/13/2005 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0023 <o:p></o:p>

Comments submitted by J. Kahn and K. Lin, NEDC Student Project
  Coordinators <o:p></o:p>

10/31/2005 <o:p></o:p>

Posted <o:p></o:p>

PUBLIC SUBMISSIONS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0024 <o:p></o:p>

Comments submitted by D. McWilliams and A. Kacenjar, Squire Sanders -
  Legal Counsel Worldwide <o:p></o:p>

10/31/2005 <o:p></o:p>

Posted <o:p></o:p>

PUBLIC SUBMISSIONS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0025 <o:p></o:p>

Mittal Steel Call Summary <o:p></o:p>

05/17/2006 <o:p></o:p>

Posted <o:p></o:p>

SUPPORTING & RELATED MATERIALS <o:p></o:p>

EPA-HQ-OAR-2002-0083 <o:p></o:p>

EPA-HQ-OAR-2002-0083-0026 <o:p></o:p>

National Emission Standards for Hazardous Air Pollutants for
  Integrated Iron and Steel Manufacturing Facilities <o:p></o:p>

07/13/2006 <o:p></o:p>

Posted <o:p></o:p>

RULES <o:p></o:p>

<o:p> </o:p>


HUMAN HEALTH SUBCOMMITTEE

DRAFT AGENDA

October 10, 2008

12:00 pm – 2:30 pm Eastern Time

Participation by Teleconference Only

866-299-3188

code:<PHONE_NUMBER>#

12:30-12:40 pm	Welcome

	-  Roll Call	Dr. James Klaunig

	- Overview of Agenda	Subcommittee Chair

12:40-12:45 pm	BOSC DFO Remarks	Ms. Heather Drumm, ORD

12:45-1:00 pm	Materials Overview	Dr. Sally Darney, Human Health National Program Director, ORD

1:00-1:30 pm	ORD Overview	Dr. Kevin Teichman, Deputy Assistant Administrator for Science, ORD

1:15-1:30 pm	Overview of Charge/	Dr. James Klaunig, Subcommittee

	Rating Program Performance	Chair & Phillip Juengst, Accountability Team Leader, ORD

1:30-2:00	Overview of ORD’s Human 	Dr. Sally Darney, Human Health

	Health Program	National Program Director, ORD

2:00-2:05 pm	Public Comment

2:05-2:30 pm 	Preparation for Next Call and Face-to-Face 	Dr. James Klaunig,

	Meeting	Subcommittee Chair

	- Discuss Writing Assignments

	- Identify Additional Information Needs

2:30 pm	Adjourn

            A Federal Advisory Committee for the U.S. Environmental Protection Agency’s Office of Research and Development


Data Collection Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water DO222272 SPC 2/ 23/ 00 9: 58a 0.013 8,513 2.046 0.367 9,223 2.084 6,040 DO222273 SPC 2/ 23/ 00 10: 02a 0.01 8,527 2.042 0.366 9,265 2.082 6077 Table C 6. Collection Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0223002 SPC 2/ 23/ 00 11: 16a 0.001 9,238 1.97 0.359 9,774 1.964 6658 D0223003 SPC 2/ 23/ 00 11: 20a 0.001 9,325 2.013 0.359 9,810 1.956 6,674 D0223004 SPC 2/ 23/ 00 11: 41a 0.008 9,179 1.994 0.359 9,654 1.941 6,547 D0223005 SPC 2/ 23/ 00 11: 46a 0.007 9,297 1.957 0.358 9,727 1.956 6,662 D0223006 SPC 2/ 23/ 00 11: 50a 0.009 9,619 1.957 0.357 9,934 1.969 6,870 D0223007 SPC 2/ 23/ 00 11: 55a 0.009 9,658 1.949 0.356 9,986 1.97 6,965 D0223008 SPC 2/ 23/ 00 11: 59a 0.01 9,401 1.952 0.357 9,787 1.969 6,711 D0223009 SPC 2/ 23/ 00 12: 04p 0.008 9,470 1.968 0.357 9,880 1.977 6,798 D0223010 SPC 2/ 23/ 00 12: 08p 0.008 9,971 1.974 0.356 10,245 1.999 7,144 D0223011 SPC 2/ 23/ 00 12: 13p 0.009 10,339 1.96 0.355 10,656 1.997 7,527 D0223012 SPC 2/ 23/ 00 12: 17p 0.009 10,017 1.935 0.355 10,342 1.964 7,257 D0223013 SPC 2/ 23/ 00 12: 22p 0.008 10,130 1.932 0.356 10,459 1.986 7,348 D0223014 SPC 2/ 23/ 00 12: 26p 0.012 10,619 1.929 0.354 10,908 1.997 7,806 D0223015 SPC 2/ 23/ 00 12: 31p 0.01 10,976 1.956 0.356 11,529 1.998 8,043 D0223016 SPC 2/ 23/ 00 12: 36p 0.01 11,029 1.947 0.355 11,591 2.016 8,153 D0223017 SPC 2/ 23/ 00 12: 40p 0.01 10,961 1.951 0.356 11,535 2.021 8,104 D0223018 SPC 2/ 23/ 00 12: 45p 0.008 10,918 1.947 0.356 11,380 2.008 7,969 D0223019 SPC 2/ 23/ 00 12: 49p 0.008 10,987 1.946 0.355 11,626 2.018 8,122 D0223020 SPC 2/ 23/ 00 12: 54p 0.012 11,162 1.964 0.355 11,730 1.978 8,270 D0223021 SPC 2/ 23/ 00 12: 58p 0.009 11,187 1.968 0.354 11,848 1.977 8,338 D0223022 SPC 2/ 23/ 00 1: 03p 0.011 11,381 1.944 0.354 11,962 2.164 8,192 D0223023 SPC 2/ 23/ 00 1: 07p 0.011 11,670 1.946 0.353 12,182 2.039 8,586 D0223024 SPC 2/ 23/ 00 1: 12p 0.011 11,927 1.952 0.352 12,553 2.09 8,901 D0223025 SPC 2/ 23/ 00 1: 16p 0.011 11,851 1.936 0.352 12,464 2.016 8,881 D0223026 SPC 2/ 23/ 00 1: 21p 0.012 11,737 1.935 0.353 12,354 1.996 8,762 D0223027 SPC 2/ 23/ 00 1: 25p 0.011 11,901 1.934 0.352 12,437 2.007 8,845 D0223028 SPC 2/ 23/ 00 1: 30p 0.011 12,043 2.153 0.354 12,671 2.026 9,030 D0223029 SPC 2/ 23/ 00 1: 34p 0.011 12,240 2.484 0.357 12,930 2.01 9,120 D0223030 SPC 2/ 23/ 00 1: 39p 0.009 12,218 2.632 0.359 12,987 2.02 9,136 D0223031 SPC 2/ 23/ 00 1: 44p 0.009 12,105 2.372 0.356 12,739 2.043 9,049 C 57 Table C 6. ( Continued) Collection Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0223032 SPC 2/ 23/ 00 1: 48p 0.009 12,175 1.984 0.35 12,772 2.098 9,102 D0223033 SPC 2/ 23/ 00 1: 53p 0.009 12,481 1.975 0.349 12,896 2.112 9,256 D0223034 SPC 2/ 23/ 00 1: 57p 0.008 12,394 1.995 0.352 12,870 2.121 9,223 D0223035 SPC 2/ 23/ 00 2: 02p 0.007 12,465 1.966 0.349 12,886 2.074 9,226 D0223036 SPC 2/ 23/ 00 2: 06p 0.009 12,668 2.043 0.349 13,166 2.144 9,524 D0223037 SPC 2/ 23/ 00 2: 11p 0.007 12,560 1.977 0.349 13,108 2.062 9,440 D0223038 SPC 2/ 23/ 00 2: 15p 0.01 12,763 1.97 0.348 13,234 2.106 9,525 D0223039 SPC 2/ 23/ 00 2: 20p 0.007 12,940 1.994 0.35 13,365 2.098 9,602 D0223040 SPC 2/ 23/ 00 2: 24p 0.005 13,053 1.976 0.349 13,580 2.08 9,743 D0223041 SPC 2/ 23/ 00 2: 29p 0.006 13,183 2.02 0.349 13,959 2.209 9,879 D0223042 SPC 2/ 23/ 00 2: 33p 0.007 13,154 1.958 0.349 13,867 2.095 9,894 D0223043 SPC 2/ 23/ 00 2: 38p 0.007 13,383 1.97 0.349 14,135 2.027 10,013 D0223044 SPC 2/ 23/ 00 2: 42p 0.011 13,565 1.994 0.348 14,322 2.044 10,192 D0223045 SPC 2/ 23/ 00 2: 47p 0.009 13,615 1.994 0.349 14,380 2.088 10,194 D0223046 SPC 2/ 23/ 00 2: 51p 0.007 13,288 1.985 0.349 14,163 2.129 10,030 D0223047 SPC 2/ 23/ 00 2: 56p 0.007 13,567 1.981 0.348 14,323 2.129 10,194 D0223048 SPC 2/ 23/ 00 3: 00p 0.008 13,677 2.095 0.349 14,465 2.143 10,310 D0223049 SPC 2/ 23/ 00 3: 05p 0.007 13,799 2.041 0.348 14,606 2.092 10,397 D0223050 SPC 2/ 23/ 00 3: 10p 0.007 13,790 2.029 0.348 14,635 2.152 10,487 D0223051 SPC 2/ 23/ 00 3: 14p 0.007 13,792 2.026 0.347 14,502 2.134 10,328 D0223052 SPC 2/ 23/ 00 3: 19p 0.006 13,705 2.104 0.349 14,428 2.152 10,234 D0223053 SPC 2/ 23/ 00 3: 23p 0.007 13,643 2.039 0.349 14,485 2.15 10,272 D0223054 SPC 2/ 23/ 00 3: 28p 0.007 13,536 2.002 0.348 14,371 2.092 10,210 D0223055 SPC 2/ 23/ 00 3: 32p 0.007 13,604 2.005 0.348 14,329 2.083 10,166 D0223056 SPC 2/ 23/ 00 3: 37p 0.007 13,748 1.981 0.347 14,592 2.111 10,444 D0223057 SPC 2/ 23/ 00 3: 41p 0.005 14,130 1.995 0.347 14,844 2.119 10,640 D0223058 SPC 2/ 23/ 00 3: 46p 0.007 14,296 1.989 0.347 15,115 2.076 10,892 D0223059 SPC 2/ 23/ 00 3: 50p 0.006 14,326 2.03 0.346 15,135 2.058 10,917 D0223060 SPC 2/ 23/ 00 3: 55p 0.006 14,230 2.017 0.347 15,043 2.075 10,806 D0223061 SPC 2/ 23/ 00 3: 59p 0.021 14,266 2.002 0.346 15,109 2.071 10,923 C 58 Table C 6. ( Continued) Collection Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0223062 SPC 2/ 23/ 00 4: 04p 0.013 14,391 1.992 0.346 15,202 2.123 10,978 D0223063 SPC 2/ 23/ 00 4: 08p 0.007 14,229 1.988 0.346 14,950 2.195 10,719 D0223064 SPC 2/ 23/ 00 4: 13p 0.022 14,104 1.984 0.346 15,003 2.032 10,811 D0223065 SPC 2/ 23/ 00 4: 17p 0.013 14,297 1.986 0.345 15,100 2.107 10,894 D0223066 SPC 2/ 23/ 00 4: 22p 0.031 14,253 1.993 0.346 15,159 2.205 10,933 D0223067 SPC 2/ 23/ 00 4: 26p 0.022 14,042 1.983 0.347 14,920 2.064 10,728 D0223068 SPC 2/ 23/ 00 4: 31p 0.033 14,106 1.985 0.346 15,137 2.127 10,903 D0223069 SPC 2/ 23/ 00 4: 36p 0.04 14,193 1.979 0.345 15,224 2.119 11,026 D0223070 SPC 2/ 23/ 00 4: 40p 0.042 14,073 1.969 0.345 15,199 2.136 10,954 D0223071 SPC 2/ 23/ 00 4: 45p 0.043 14,122 1.967 0.345 15,295 2.198 11,057 D0223072 SPC 2/ 23/ 00 4: 49p 0.042 14,108 1.97 0.344 15,264 2.176 11,075 D0223073 SPC 2/ 23/ 00 4: 54p 0.042 14,331 1.938 0.341 15,239 2.325 11,044 D0223074 SPC 2/ 23/ 00 4: 58p 0.042 14,184 1.942 0.346 15,276 2.37 11,125 D0223075 SPC 2/ 23/ 00 5: 03p 0.042 14,396 1.929 0.336 15,149 2.195 10,943 D0223076 SPC 2/ 23/ 00 5: 07p 0.044 14,554 1.962 0.337 15,278 2.336 11,146 D0223077 SPC 2/ 23/ 00 5: 12p 0.042 14,474 1.921 0.336 15,231 2.274 11,081 D0223078 SPC 2/ 23/ 00 5: 16p 0.042 14,627 1.92 0.338 15,298 2.071 11,205 D0223079 SPC 2/ 23/ 00 5: 21p 0.045 14,633 1.924 0.338 15,419 2.188 11,265 D0223080 SPC 2/ 23/ 00 5: 25p 0.044 14,478 1.923 0.337 15,191 2.177 11,123 D0223081 SPC 2/ 23/ 00 5: 30p 0.043 14,474 1.924 0.338 15,131 2.138 11,017 D0223082 SPC 2/ 23/ 00 5: 35p 0.038 14,699 1.942 0.337 15,261 2.2 11,054 D0223083 SPC 2/ 23/ 00 5: 39p 0.041 14,522 1.933 0.338 15,234 2.043 11,102 D0223084 SPC 2/ 23/ 00 5: 44p 0.043 14,489 1.923 0.338 15,279 2.216 11,155 D0223085 SPC 2/ 23/ 00 5: 48p 0.043 14,573 1.932 0.338 15,312 2.248 11,194 D0223086 SPC 2/ 23/ 00 5: 53p 0.046 14,410 1.939 0.339 15,231 2.172 11,147 D0223087 SPC 2/ 23/ 00 5: 57p 0.043 14,811 1.93 0.338 15,507 2.143 11,370 D0223088 SPC 2/ 23/ 00 6: 02p 0.044 14,769 1.92 0.338 15,533 1.962 11,428 D0223089 SPC 2/ 23/ 00 6: 06p 0.047 15,053 1.914 0.338 15,640 1.927 11,570 D0223090 SPC 2/ 23/ 00 6: 11p 0.048 15,008 1.914 0.34 15,658 1.922 11,606 D0223091 SPC 2/ 23/ 00 6: 15p 0.042 14,905 1.911 0.339 15,513 1.898 11,498 C 59 Table C 6. ( Continued) Collection Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0223092 SPC 2/ 23/ 00 6: 20p 0.047 14,790 1.919 0.339 15,531 1.893 11,490 D0223093 SPC 2/ 23/ 00 6: 25p 0.047 14,677 1.924 0.339 15,496 1.912 11,496 D0223094 SPC 2/ 23/ 00 6: 29p 0.045 14,700 1.925 0.341 15,446 1.9 11,388 D0223095 SPC 2/ 23/ 00 6: 34p 0.047 14,595 1.926 0.341 15,405 1.916 11,397 D0223096 SPC 2/ 23/ 00 6: 38p 0.044 14,701 1.922 0.341 15,445 1.915 11,405 D0223097 SPC 2/ 23/ 00 6: 43p 0.044 14,835 1.923 0.342 15,425 1.919 11,425 D0223098 SPC 2/ 23/ 00 6: 47p 0.048 14,598 1.922 0.341 15,396 1.917 11,450 D0223099 SPC 2/ 23/ 00 6: 52p 0.049 14,631 1.924 0.341 15,443 1.933 11,507 D0223100 SPC 2/ 23/ 00 6: 56p 0.047 14,542 1.924 0.342 15,345 1.922 11,416 D0223101 SPC 2/ 23/ 00 7: 01p 0.045 14,634 1.927 0.342 15,289 1.903 11,333 D0223102 SPC 2/ 23/ 00 7: 05p 0.05 14,563 1.931 0.343 15,293 1.908 11,368 D0223103 SPC 2/ 23/ 00 7: 10p 0.049 14,521 1.934 0.345 15,297 1.91 11,332 D0223104 SPC 2/ 23/ 00 7: 15p 0.05 14,648 2.029 0.344 15,444 1.933 11,520 D0223105 SPC 2/ 23/ 00 7: 19p 0.05 14,643 2.035 0.345 15,402 1.945 11,432 D0223106 SPC 2/ 23/ 00 7: 24p 0.045 14,556 1.977 0.345 15,232 1.925 11,287 D0223107 SPC 2/ 23/ 00 7: 28p 0.047 14,701 1.959 0.344 15,304 1.927 11,384 D0223108 SPC 2/ 23/ 00 7: 33p 0.046 14,436 1.96 0.344 15,129 1.912 11,167 D0223109 SPC 2/ 23/ 00 7: 37p 0.048 14,407 1.953 0.344 15,137 1.922 11,166 D0223110 SPC 2/ 23/ 00 7: 42p 0.049 14,485 1.952 0.344 15,280 1.95 11,361 D0223111 SPC 2/ 23/ 00 7: 46p 0.05 14,512 1.954 0.344 15,451 1.95 11,532 D0223112 SPC 2/ 23/ 00 7: 51p 0.049 14,672 1.95 0.344 15,535 1.989 11,602 D0223113 SPC 2/ 23/ 00 7: 55p 0.047 14,681 1.946 0.345 15,490 2.088 11,538 D0223114 SPC 2/ 23/ 00 8: 00p 0.046 14,815 1.948 0.344 15,542 1.964 11,637 D0223115 SPC 2/ 23/ 00 8: 04p 0.046 14,971 1.954 0.344 15,589 1.963 11,697 D0223116 SPC 2/ 23/ 00 8: 09p 0.048 14,673 1.983 0.345 15,407 1.904 11,468 D0223117 SPC 2/ 23/ 00 8: 14p 0.047 14,860 1.99 0.345 15,548 1.91 11,630 D0223118 SPC 2/ 23/ 00 8: 18p 0.045 15,346 1.97 0.344 16,104 2.115 12,064 D0223119 SPC 2/ 23/ 00 8: 23p 0.05 15,366 1.984 0.344 16,400 2.527 12,153 D0223120 SPC 2/ 23/ 00 8: 27p 0.047 15,645 1.976 0.345 16,735 2.948 12,349 D0223121 SPC 2/ 23/ 00 8: 32p 0.046 15,748 1.968 0.345 16,797 2.819 12,456 C 60 Table C 6. ( Continued) Collection Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0223122 SPC 2/ 23/ 00 8: 36p 0.046 15,666 1.971 0.346 16,667 2.819 12,346 D0223123 SPC 2/ 23/ 00 8: 41p 0.048 15,625 1.975 0.346 16,627 2.394 12,268 D0223124 SPC 2/ 23/ 00 8: 45p 0.048 15,581 2.075 0.345 16,675 2.273 12,243 D0223125 SPC 2/ 23/ 00 8: 50p 0.047 15,578 1.974 0.344 16,581 2.118 12,219 D0223126 SPC 2/ 23/ 00 8: 54p 0.051 15,437 1.978 0.344 16,468 2.157 12,191 D0223127 SPC 2/ 23/ 00 8: 59p 0.048 15,276 1.949 0.345 16,144 2.027 12,086 D0223128 SPC 2/ 23/ 00 9: 04p 0.049 15,058 1.941 0.345 15,794 2.131 11,833 D0223129 SPC 2/ 23/ 00 9: 08p 0.05 14,860 1.939 0.347 15,518 2.121 11,644 D0223130 SPC 2/ 23/ 00 9: 13p 0.051 14,945 1.947 0.347 15,711 2.088 11,782 D0223131 SPC 2/ 23/ 00 9: 17p 0.049 15,025 1.956 0.347 15,871 2.339 11,883 D0223132 SPC 2/ 23/ 00 9: 22p 0.049 15,132 1.956 0.347 15,843 2.842 11,912 D0223133 SPC 2/ 23/ 00 9: 26p 0.052 14,920 1.95 0.346 15,655 2.726 11,785 D0223134 SPC 2/ 23/ 00 9: 31p 0.048 14,992 1.959 0.347 15,642 2.861 11,723 D0223135 SPC 2/ 23/ 00 9: 35p 0.052 15,125 1.962 0.347 15,749 2.855 11,780 D0223136 SPC 2/ 23/ 00 9: 40p 0.048 15,330 1.965 0.345 16,408 3.373 12,225 D0223137 SPC 2/ 23/ 00 9: 44p 0.047 15,433 1.981 0.347 16,718 4.308 12,305 D0223138 SPC 2/ 23/ 00 9: 49p 0.047 15,652 1.976 0.348 16,723 4.543 12,368 D0223139 SPC 2/ 23/ 00 9: 53p 0.048 15,233 1.977 0.348 16,639 4.687 12,233 D0223140 SPC 2/ 23/ 00 9: 58p 0.046 15,058 1.951 0.347 15,920 3.864 11,951 D0223141 SPC 2/ 23/ 00 10: 02p 0.049 14,884 1.953 0.349 15,606 3.166 11,689 D0223142 SPC 2/ 23/ 00 10: 07p 0.05 14,545 2.02 0.35 15,574 2.897 11,615 D0223143 SPC 2/ 23/ 00 10: 12p 0.05 14,881 1.963 0.349 15,662 2.736 11,772 D0223144 SPC 2/ 23/ 00 10: 16p 0.047 15,291 1.975 0.347 16,344 2.728 12,180 D0223145 SPC 2/ 23/ 00 10: 21p 0.05 15,470 1.994 0.348 16,746 2.443 12,452 D0223146 SPC 2/ 23/ 00 10: 25p 0.049 15,849 1.988 0.349 16,625 2.337 12,371 D0223147 SPC 2/ 23/ 00 10: 30p 0.049 15,336 1.982 0.348 16,395 2.482 12,112 D0223148 SPC 2/ 23/ 00 10: 34p 0.053 15,443 1.989 0.349 16,299 2.4 12,093 D0223149 SPC 2/ 23/ 00 10: 39p 0.051 15,137 1.982 0.348 16,063 2.253 12,092 D0223150 SPC 2/ 23/ 00 10: 43p 0.053 15,502 2.028 0.35 16,704 2.221 12,454 D0223151 SPC 2/ 23/ 00 10: 48p 0.051 15,199 2.043 0.349 16,039 2.351 12,080 C 61 Table C 6. ( Continued) Collection Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0223152 SPC 2/ 23/ 00 10: 52p 0.053 14,677 1.956 0.349 15,627 2.34 11,858 D0223153 SPC 2/ 23/ 00 10: 57p 0.056 15,099 1.973 0.349 15,735 2.371 11,883 D0223154 SPC 2/ 23/ 00 11: 02p 0.057 14,763 1.97 0.349 15,482 2.449 11,649 D0223155 SPC 2/ 23/ 00 11: 06p 0.055 14,339 1.984 0.35 15,504 2.358 11,674 D0223156 SPC 2/ 23/ 00 11: 11p 0.057 14,439 2.059 0.351 15,312 2.353 11,489 D0223157 SPC 2/ 23/ 00 11: 15p 0.053 14,661 1.971 0.35 15,546 2.414 11,703 D0223158 SPC 2/ 23/ 00 11: 20p 0.053 14,954 1.964 0.351 15,375 2.487 11,563 D0223159 SPC 2/ 23/ 00 11: 24p 0.056 14,421 1.966 0.351 15,281 2.53 11,487 D0223160 SPC 2/ 23/ 00 11: 29p 0.054 14,360 1.985 0.352 15,070 2.444 11,253 D0223161 SPC 2/ 23/ 00 11: 33p 0.053 14,351 2.032 0.354 15,136 2.28 11,302 D0223162 SPC 2/ 23/ 00 11: 38p 0.057 14,340 1.998 0.353 15,205 2.299 11,344 D0223163 SPC 2/ 23/ 00 11: 42p 0.056 14,405 1.991 0.353 15,212 2.329 11,403 D0223164 SPC 2/ 23/ 00 11: 47p 0.053 14,459 2.013 0.353 15,325 2.376 11,501 D0223165 SPC 2/ 23/ 00 11: 52p 0.056 14,342 2.031 0.353 15,192 2.316 11,345 D0223166 SPC 2/ 23/ 00 11: 56p 0.051 14,395 2.061 0.354 15,102 2.251 11,191 D0223167 SPC 2/ 24/ 00 12: 01a 0.052 14,513 2.006 0.353 15,287 2.308 11,557 D0223168 SPC 2/ 24/ 00 12: 05a 0.052 14,858 2.009 0.353 15,595 2.296 11,826 D0223169 SPC 2/ 24/ 00 12: 10a 0.054 14,867 2.006 0.353 15,776 2.214 11,966 D0223170 SPC 2/ 24/ 00 12: 14a 0.051 14,728 1.992 0.353 15,569 2.217 11,804 D0223171 SPC 2/ 24/ 00 12: 19a 0.051 14,809 2.001 0.354 15,532 2.23 11,759 D0223172 SPC 2/ 24/ 00 12: 23a 0.053 14,497 1.991 0.354 15,337 2.149 11,510 D0223173 SPC 2/ 24/ 00 12: 28a 0.053 14,406 1.987 0.354 15,237 2.133 11,484 D0223174 SPC 2/ 24/ 00 12: 32a 0.055 14,358 1.995 0.354 15,295 2.135 11,554 D0223175 SPC 2/ 24/ 00 12: 37a 0.056 14,206 1.992 0.354 15,200 2.127 11,465 D0223176 SPC 2/ 24/ 00 12: 42a 0.053 14,262 1.991 0.355 15,033 2.089 11,291 D0223177 SPC 2/ 24/ 00 12: 46a 0.051 13,767 1.984 0.355 14,593 2.094 10,880 D0223178 SPC 2/ 24/ 00 12: 51a 0.049 13,807 1.976 0.356 14,460 2.088 10,853 D0223179 SPC 2/ 24/ 00 12: 55a 0.052 14,037 1.991 0.356 14,664 2.117 10,932 D0223180 SPC 2/ 24/ 00 1: 00a 0.052 13,745 1.986 0.357 14,545 2.17 10,827 D0223181 SPC 2/ 24/ 00 1: 04a 0.044 13,659 1.98 0.356 14,447 2.246 10,800 C 62 Table C 6. ( Continued) Collection Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0223182 SPC 2/ 24/ 00 1: 09a 0.04 14,088 2 0.356 14,767 2.151 11,042 D0223183 SPC 2/ 24/ 00 1: 13a 0.043 13,929 2.004 0.357 14,648 2.129 10,951 D0223184 SPC 2/ 24/ 00 1: 18a 0.046 13,854 2.029 0.356 14,561 2.188 10,771 D0223185 SPC 2/ 24/ 00 1: 22a 0.047 13,717 2.019 0.356 14,504 2.233 10,828 D0223186 SPC 2/ 24/ 00 1: 27a 0.042 13,822 2.036 0.357 14,543 2.355 10,776 D0223187 SPC 2/ 24/ 00 1: 32a 0.039 13,784 2.028 0.358 14,448 2.316 10,609 D0223188 SPC 2/ 24/ 00 1: 36a 0.037 13,780 2.021 0.358 14,383 2.142 10,695 D0223189 SPC 2/ 24/ 00 1: 41a 0.049 13,831 2.047 0.357 14,665 2.207 10,829 D0223190 SPC 2/ 24/ 00 1: 45a 0.054 14,353 2.082 0.356 14,984 2.244 11,220 D0223191 SPC 2/ 24/ 00 1: 50a 0.05 13,949 2.084 0.356 14,827 2.202 11,017 D0223192 SPC 2/ 24/ 00 1: 54a 0.052 14,076 2.057 0.356 14,797 2.044 11,089 D0223193 SPC 2/ 24/ 00 1: 59a 0.056 13,653 2.033 0.357 14,528 2.121 10,831 D0223194 SPC 2/ 24/ 00 2: 03a 0.057 13,572 2.049 0.358 14,468 2.278 10,677 D0223195 SPC 2/ 24/ 00 2: 08a 0.053 13,372 2.051 0.358 14,374 2.281 10,660 D0223196 SPC 2/ 24/ 00 2: 13a 0.047 13,537 2.043 0.358 14,379 2.289 10,706 D0223197 SPC 2/ 24/ 00 2: 17a 0.051 13,672 2.057 0.358 14,334 2.331 10,557 D0223198 SPC 2/ 24/ 00 2: 22a 0.054 13,203 2.042 0.357 14,063 2.353 10,394 D0223199 SPC 2/ 24/ 00 2: 26a 0.056 13,386 2.07 0.358 14,170 2.385 10,427 D0223200 SPC 2/ 24/ 00 2: 31a 0.054 13,470 2.082 0.359 14,311 2.349 10,554 D0223201 SPC 2/ 24/ 00 2: 35a 0.052 13,455 2.09 0.358 14,214 2.338 10,447 D0223202 SPC 2/ 24/ 00 2: 40a 0.061 13,676 2.167 0.36 14,546 2.731 10,713 D0223203 SPC 2/ 24/ 00 2: 44a 0.058 13,691 2.137 0.359 14,521 2.609 10,787 D0223204 SPC 2/ 24/ 00 2: 49a 0.057 13,368 2.123 0.359 14,304 2.453 10,507 D0223205 SPC 2/ 24/ 00 2: 53a 0.056 13,247 2.124 0.359 14,237 2.38 10,487 D0223206 SPC 2/ 24/ 00 2: 58a 0.056 13,484 2.143 0.36 14,272 2.638 10,549 D0223207 SPC 2/ 24/ 00 3: 03a 0.053 13,536 2.21 0.36 14,279 2.569 10,420 D0223208 SPC 2/ 24/ 00 3: 07a 0.054 13,419 2.171 0.36 14,383 2.586 10,517 D0223209 SPC 2/ 24/ 00 3: 12a 0.056 13,314 2.116 0.359 14,133 2.472 10,363 D0223210 SPC 2/ 24/ 00 3: 16a 0.055 13,190 2.13 0.359 14,160 2.403 10,387 D0223211 SPC 2/ 24/ 00 3: 21a 0.054 13,197 2.133 0.359 14,106 2.346 10,324 C 63 Table C 6. ( Continued) Collection Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0223212 SPC 2/ 24/ 00 3: 25a 0.055 13,585 2.181 0.36 14,487 2.444 10,661 D0223213 SPC 2/ 24/ 00 3: 30a 0.058 13,606 2.184 0.36 14,513 2.749 10,799 D0223214 SPC 2/ 24/ 00 3: 34a 0.051 13,298 2.159 0.36 14,141 2.404 10,342 D0223215 SPC 2/ 24/ 00 3: 39a 0.054 13,166 2.153 0.36 14,097 2.271 10,299 D0223216 SPC 2/ 24/ 00 3: 43a 0.058 13,278 2.211 0.361 14,224 2.333 10,419 D0223217 SPC 2/ 24/ 00 3: 48a 0.056 13,229 2.17 0.359 14,232 2.256 10,445 D0223218 SPC 2/ 24/ 00 3: 53a 0.055 13,125 2.155 0.36 14,057 2.179 10,337 D0223219 SPC 2/ 24/ 00 3: 57a 0.057 13,079 2.149 0.361 13,690 2.144 10,174 D0223220 SPC 2/ 24/ 00 4: 02a 0.056 13,433 2.167 0.36 14,208 2.181 10,452 D0223221 SPC 2/ 24/ 00 4: 06a 0.054 13,433 2.183 0.36 14,296 2.175 10,535 D0223222 SPC 2/ 24/ 00 4: 11a 0.056 13,517 2.18 0.361 14,356 2.184 10,604 D0223223 SPC 2/ 24/ 00 4: 15a 0.057 13,541 2.187 0.361 14,390 2.224 10,596 D0223224 SPC 2/ 24/ 00 4: 20a 0.056 13,608 2.189 0.361 14,501 2.252 10,715 D0223225 SPC 2/ 24/ 00 4: 24a 0.057 13,646 2.207 0.362 14,535 2.306 10,762 D0223226 SPC 2/ 24/ 00 4: 29a 0.055 13,799 2.222 0.364 14,600 2.435 10,764 D0223227 SPC 2/ 24/ 00 4: 34a 0.053 13,739 2.242 0.364 14,518 2.531 10,691 D0223228 SPC 2/ 24/ 00 4: 38a 0.055 13,728 2.281 0.365 14,526 2.801 10,660 D0223229 SPC 2/ 24/ 00 4: 43a 0.057 13,218 2.244 0.364 14,145 3.004 10,367 D0223230 SPC 2/ 24/ 00 4: 47a 0.058 13,024 2.212 0.363 13,689 2.928 10,122 D0223231 SPC 2/ 24/ 00 4: 52a 0.058 12,734 2.214 0.363 13,481 2.762 10,067 D0223232 SPC 2/ 24/ 00 4: 56a 0.055 12,787 2.374 0.364 13,276 2.626 9,843 D0223233 SPC 2/ 24/ 00 5: 01a 0.054 12,876 2.269 0.363 13,308 2.449 9,852 D0223234 SPC 2/ 24/ 00 5: 05a 0.05 13,317 2.251 0.363 13,785 2.519 10,135 D0223235 SPC 2/ 24/ 00 5: 10a 0.05 13,184 2.269 0.364 13,801 2.643 10,169 D0223236 SPC 2/ 24/ 00 5: 15a 0.051 13,053 2.346 0.366 13,721 3.057 10,108 D0223237 SPC 2/ 24/ 00 5: 19a 0.052 12,703 2.291 0.365 13,221 2.769 9,783 D0223238 SPC 2/ 24/ 00 5: 24a 0.055 12,807 2.33 0.369 13,484 3.013 10,003 D0223239 SPC 2/ 24/ 00 5: 28a 0.052 12,793 2.342 0.373 13,428 3.064 9,989 D0223240 SPC 2/ 24/ 00 5: 33a 0.052 12,875 2.414 0.372 13,399 3.203 9,866 D0223241 SPC 2/ 24/ 00 5: 37a 0.05 12,866 2.398 0.374 13,325 3.439 9,790 C 64 C 64 Table C 6. ( Continued) Collection Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0223242 SPC 2/ 24/ 00 5: 42a 0.05 13,136 2.385 0.377 13,687 3.57 10,011 D0223243 SPC 2/ 24/ 00 5: 46a 0.052 13,105 2.404 0.371 13,888 3.21 10,178 D0223244 SPC 2/ 24/ 00 5: 51a 0.052 13,313 2.441 0.368 14,192 3.022 10,381 D0223245 SPC 2/ 24/ 00 5: 56a 0.052 13,446 2.45 0.367 14,303 2.904 10,453 D0223246 SPC 2/ 24/ 00 6: 00a 0.052 13,278 2.428 0.367 14,134 2.958 10,296 D0223247 SPC 2/ 24/ 00 6: 05a 0.052 13,073 2.422 0.367 13,816 2.939 10,072 D0223248 SPC 2/ 24/ 00 6: 09a 0.052 13,147 2.422 0.367 13,944 2.893 10,232 D0223249 SPC 2/ 24/ 00 6: 14a 0.055 13,038 2.425 0.367 13,957 2.786 10,195 D0223250 SPC 2/ 24/ 00 6: 18a 0.056 13,113 2.754 0.372 14,120 2.69 10,160 D0223251 SPC 2/ 24/ 00 6: 23a 0.056 12,903 2.624 0.372 13,773 2.65 10,014 D0223252 SPC 2/ 24/ 00 6: 28a 0.057 12,964 2.456 0.373 13,833 2.653 10,190 D0223253 SPC 2/ 24/ 00 6: 32a 0.056 13,105 2.396 0.373 13,930 2.741 10,201 D0223254 SPC 2/ 24/ 00 6: 37a 0.054 13,133 2.376 0.373 14,091 2.798 10,218 D0223255 SPC 2/ 24/ 00 6: 41a 0.054 13,430 2.33 0.369 14,234 3.79 10,354 D0223256 SPC 2/ 24/ 00 6: 46a 0.051 13,325 2.325 0.369 14,169 3.842 10,285 D0223257 SPC 2/ 24/ 00 6: 50a 0.05 13,030 2.445 0.373 13,717 3.127 10,032 D0223258 SPC 2/ 24/ 00 6: 55a 0.053 13,045 2.612 0.374 13,662 3.054 9,943 D0223259 SPC 2/ 24/ 00 6: 59a 0.053 12,856 2.557 0.374 13,518 3.168 9,878 D0223260 SPC 2/ 24/ 00 7: 04a 0.053 12,698 2.559 0.374 13,345 3.185 9,819 D0223261 SPC 2/ 24/ 00 7: 09a 0.054 12,837 2.609 0.374 13,498 3.192 9,906 D0223262 SPC 2/ 24/ 00 7: 13a 0.053 13,082 2.58 0.374 13,719 3.142 10,021 D0223263 SPC 2/ 24/ 00 7: 18a 0.053 13,072 2.469 0.374 13,640 3.103 10,025 D0223264 SPC 2/ 24/ 00 7: 22a 0.052 13,320 2.486 0.373 14,172 3.099 10,284 D0223265 SPC 2/ 24/ 00 7: 27a 0.05 13,837 2.598 0.373 14,765 3.157 10,810 D0223266 SPC 2/ 24/ 00 7: 31a 0.048 13,934 2.561 0.371 14,833 3.13 10,931 D0223267 SPC 2/ 24/ 00 7: 36a 0.046 13,944 2.47 0.372 14,856 2.933 10,928 D0223268 SPC 2/ 24/ 00 7: 40a 0.037 14,307 2.417 0.373 15,058 2.846 11,183 D0223269 SPC 2/ 24/ 00 7: 45a 0.042 13,968 2.388 0.374 14,756 2.81 10,913 D0223270 SPC 2/ 24/ 00 7: 50a 0.048 13,717 2.377 0.374 14,632 2.87 10,782 D0223271 SPC 2/ 24/ 00 7: 54a 0.051 13,993 2.46 0.375 14,955 3.048 11,070 C 65 C 65 Table C 6. ( Continued) Collection Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0223272 SPC 2/ 24/ 00 7: 59a 0.05 14,363 2.495 0.376 15,198 3.316 11,323 D0223273 SPC 2/ 24/ 00 8: 03a 0.054 14,307 2.449 0.375 15,150 3.259 11,313 D0223274 SPC 2/ 24/ 00 8: 08a 0.057 13,909 2.538 0.374 14,956 3.169 11,055 D0223275 SPC 2/ 24/ 00 8: 12a 0.054 13,759 2.569 0.376 14,752 3.3 10,791 D0223276 SPC 2/ 24/ 00 8: 17a 0.053 13,717 2.646 0.377 14,722 3.187 10,771 D0223277 SPC 2/ 24/ 00 8: 22a 0.051 13,752 2.493 0.374 14,553 3.155 10,704 D0223278 SPC 2/ 24/ 00 8: 26a 0.051 13,613 2.497 0.374 14,540 3.19 10,674 D0223279 SPC 2/ 24/ 00 8: 31a 0.052 13,542 2.49 0.373 14,519 3.154 10,664 D0223280 SPC 2/ 24/ 00 8: 35a 0.052 13,778 2.474 0.374 14,669 3.098 10,825 D0223281 SPC 2/ 24/ 00 8: 40a 0.05 13,888 2.459 0.375 14,728 3.138 10,807 D0223282 SPC 2/ 24/ 00 8: 44a 0.048 14,081 2.483 0.384 14,915 3.2 10,961 D0223283 SPC 2/ 24/ 00 8: 49a 0.052 14,019 2.521 0.393 15,011 3.186 11092 C 66 Table C 7. Data Collection Information Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0224002 SPC 2/ 24/ 00 9: 40a 0.047 15684 2.243 0.356 17442 2.367 13145 D0224003 SPC 2/ 24/ 00 9: 45a 0.046 15,897 2.199 0.354 17,643 2.251 13,343 D0224004 SPC 2/ 24/ 00 9: 53a 0.043 15,881 2.15 0.353 17,750 2.175 13,474 D0224005 SPC 2/ 24/ 00 9: 57a 0.042 16,189 2.233 0.354 17,932 2.161 13,597 D0224006 SPC 2/ 24/ 00 10: 02a 0.04 16,048 2.176 0.354 17,881 2.213 13,606 D0224007 SPC 2/ 24/ 00 10: 06a 0.039 16,226 2.161 0.353 17,883 2.255 13,590 D0224008 SPC 2/ 24/ 00 10: 11a 0.04 16,141 2.202 0.354 17,900 2.325 13,558 D0224009 SPC 2/ 24/ 00 10: 15a 0.044 16,247 2.148 0.353 17,990 2.492 13,634 D0224010 SPC 2/ 24/ 00 10: 20a 0.04 16,365 2.143 0.352 17,960 2.557 13,601 D0224011 SPC 2/ 24/ 00 10: 24a 0.039 16,341 2.16 0.352 17,912 2.624 13,566 D0224012 SPC 2/ 24/ 00 10: 29a 0.038 16,208 2.166 0.352 17,943 2.541 13,589 D0224013 SPC 2/ 24/ 00 10: 35a 0.042 16,344 2.113 0.349 18,123 2.415 13,782 D0224014 SPC 2/ 24/ 00 10: 40a 0.043 16,463 2.159 0.349 18,162 2.37 13,768 D0224015 SPC 2/ 24/ 00 10: 44a 0.042 16,534 2.173 0.35 18,184 2.358 13,761 D0224016 SPC 2/ 24/ 00 10: 49a 0.041 16,505 2.114 0.349 18,180 2.335 13,822 D0224017 SPC 2/ 24/ 00 10: 53a 0.044 16,423 2.116 0.348 18,195 2.322 13,864 D0224018 SPC 2/ 24/ 00 10: 58a 0.042 16,568 2.104 0.347 18,282 2.322 13,914 D0224019 SPC 2/ 24/ 00 11: 02a 0.04 16,659 2.097 0.346 18,307 2.298 13,991 D0224020 SPC 2/ 24/ 00 11: 07a 0.042 16,714 2.09 0.345 18,417 2.362 13,986 D0224021 SPC 2/ 24/ 00 11: 11a 0.044 16,709 2.101 0.345 18,526 2.357 14,006 D0224022 SPC 2/ 24/ 00 11: 16a 0.041 16,705 2.094 0.344 18,386 2.25 13,960 D0224023 SPC 2/ 24/ 00 11: 21a 0.043 16,792 2.079 0.343 18,674 2.191 14,041 D0224024 SPC 2/ 24/ 00 11: 25a 0.043 16,971 2.074 0.342 18,803 2.248 14,110 D0224025 SPC 2/ 24/ 00 11: 30a 0.039 17,142 2.039 0.34 18,950 2.216 14,190 D0224026 SPC 2/ 24/ 00 11: 34a 0.04 17,046 2.018 0.34 18,814 2.087 14,062 D0224027 SPC 2/ 24/ 00 11: 39a 0.039 16,924 2.009 0.339 18,542 2.058 13,982 D0224028 SPC 2/ 24/ 00 11: 43a 0.039 16,868 1.994 0.339 18,494 2.05 13,987 D0224029 SPC 2/ 24/ 00 11: 48a 0.033 16,921 2 0.34 18,542 2.175 14,013 D0224030 SPC 2/ 24/ 00 11: 52a 0.042 16,964 2.006 0.338 18,579 2.129 14,025 D0224031 SPC 2/ 24/ 00 11: 57a 0.035 16,804 1.994 0.339 18,230 2.157 13,781 C 67 Table C 7. ( Continued)

Data Collection Information Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0224032 SPC 2/ 24/ 00 12: 01p 0.038 16,839 1.985 0.338 18,467 2.222 13,975 D0224033 SPC 2/ 24/ 00 12: 06p 0.038 16,796 1.968 0.338 18,313 2.063 13,839 D0224034 SPC 2/ 24/ 00 12: 10p 0.039 16,654 1.965 0.338 18,124 2.091 13,663 D0224035 SPC 2/ 24/ 00 12: 15p 0.028 16,662 1.969 0.34 18,125 2.058 13,629 D0224036 SPC 2/ 24/ 00 12: 19p 0.03 16,480 1.964 0.34 17,943 1.932 13,516 D0224037 SPC 2/ 24/ 00 12: 24p 0.033 16,547 1.968 0.339 18,121 1.972 13,694 D0224038 SPC 2/ 24/ 00 12: 28p 0.03 16,869 1.975 0.339 18,315 1.999 13,838 D0224039 SPC 2/ 24/ 00 12: 33p 0.032 16,848 1.988 0.339 18,365 1.968 13,881 D0224040 SPC 2/ 24/ 00 12: 37p 0.032 16,891 2.002 0.339 18,349 2.01 13,896 D0224041 SPC 2/ 24/ 00 12: 42p 0.029 16,563 1.961 0.339 18,035 1.885 13,596 D0224042 SPC 2/ 24/ 00 12: 47p 0.032 16,647 1.961 0.339 18,167 1.945 13,775 D0224043 SPC 2/ 24/ 00 12: 51p 0.038 16,746 1.973 0.338 18,257 1.966 13,801 D0224044 SPC 2/ 24/ 00 12: 56p 0.036 16,831 1.966 0.338 18,441 2.136 13,980 D0224045 SPC 2/ 24/ 00 1: 00p 0.032 17,001 1.982 0.338 18,591 2.148 14,041 D0224046 SPC 2/ 24/ 00 1: 05p 0.039 17,036 1.99 0.337 18,727 2.498 14,042 D0224047 SPC 2/ 24/ 00 1: 09p 0.042 16,768 1.983 0.337 18,345 2.409 13,857 D0224048 SPC 2/ 24/ 00 1: 14p 0.039 16,605 1.975 0.337 18,177 2.282 13,671 D0224049 SPC 2/ 24/ 00 1: 18p 0.039 16,412 1.969 0.338 17,963 2.221 13,493 D0224050 SPC 2/ 24/ 00 1: 23p 0.037 16,767 1.971 0.337 18,154 2.246 13,666 D0224051 SPC 2/ 24/ 00 1: 27p 0.029 16,720 1.981 0.338 18,233 2.239 13,748 D0224052 SPC 2/ 24/ 00 1: 32p 0.033 17,052 1.977 0.338 18,705 2.126 14,056 D0224053 SPC 2/ 24/ 00 1: 36p 0.037 16,939 1.985 0.337 18,603 2.091 14,053 D0224054 SPC 2/ 24/ 00 1: 41p 0.038 16,773 1.994 0.338 18,325 2.024 13,861 D0224055 SPC 2/ 24/ 00 1: 45p 0.038 16,825 1.985 0.337 18,366 2.095 13,912 D0224056 SPC 2/ 24/ 00 1: 50p 0.035 16,856 1.971 0.337 18,390 2.072 13,924 D0224057 SPC 2/ 24/ 00 1: 54p 0.039 16,792 1.983 0.336 18,447 2.056 13,989 D0224058 SPC 2/ 24/ 00 1: 59p 0.034 16,927 1.97 0.336 18,417 2.075 13,937 D0224059 SPC 2/ 24/ 00 2: 03p 0.034 16,916 1.991 0.337 18,455 2.128 13,914 D0224060 SPC 2/ 24/ 00 2: 08p 0.037 16,882 1.986 0.336 18,483 2.327 13,956 D0224061 SPC 2/ 24/ 00 2: 13p 0.038 16,820 1.99 0.336 18,733 2.092 14,088 C 68 Table C 7. ( Continued)

Data Collection Information Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0224062 SPC 2/ 24/ 00 2: 17p 0.037 17,012 1.978 0.336 18,843 2.037 14,134 D0224063 SPC 2/ 24/ 00 2: 22p 0.03 17,079 1.985 0.336 18,625 2.285 13,994 D0224064 SPC 2/ 24/ 00 2: 26p 0.034 17,082 2.007 0.336 18,554 2.321 13,945 D0224065 SPC 2/ 24/ 00 2: 31p 0.037 16,900 1.972 0.335 18,322 2.22 13,784 D0224066 SPC 2/ 24/ 00 2: 35p 0.039 16,795 1.978 0.335 18,301 2.344 13,721 D0224067 SPC 2/ 24/ 00 2: 40p 0.034 16,680 1.982 0.336 18,179 2.434 13,647 D0224068 SPC 2/ 24/ 00 2: 44p 0.035 16,469 2.004 0.336 17,989 2.289 13,438 D0224069 SPC 2/ 24/ 00 2: 49p 0.039 16,528 1.981 0.335 18,002 2.267 13,493 D0224070 SPC 2/ 24/ 00 2: 53p 0.04 16,444 1.972 0.336 18,022 2.283 13,483 D0224071 SPC 2/ 24/ 00 2: 58p 0.04 16,634 1.981 0.336 18,127 2.455 13,585 D0224072 SPC 2/ 24/ 00 3: 02p 0.033 16,710 1.983 0.336 18,087 2.431 13,590 D0224073 SPC 2/ 24/ 00 3: 07p 0.036 16,555 1.974 0.336 18,054 2.31 13,538 D0224074 SPC 2/ 24/ 00 3: 11p 0.035 16,868 1.969 0.336 18,257 2.321 13,773 D0224075 SPC 2/ 24/ 00 3: 16p 0.037 16,742 1.972 0.336 18,070 2.394 13,564 D0224076 SPC 2/ 24/ 00 3: 20p 0.036 16,857 1.976 0.336 18,293 2.366 13,777 D0224077 SPC 2/ 24/ 00 3: 25p 0.033 17,034 2.001 0.336 18,686 2.447 13,985 D0224078 SPC 2/ 24/ 00 3: 29p 0.035 16,820 1.974 0.336 18,358 2.513 13,848 D0224079 SPC 2/ 24/ 00 3: 34p 0.038 16,523 1.982 0.336 18,086 2.389 13,547 D0224080 SPC 2/ 24/ 00 3: 39p 0.037 16,733 2.03 0.337 18,249 2.328 13,696 D0224081 SPC 2/ 24/ 00 3: 43p 0.038 16,508 1.985 0.336 18,021 2.267 13,480 D0224082 SPC 2/ 24/ 00 3: 48p 0.038 16,473 1.992 0.336 17,976 2.264 13,478 D0224083 SPC 2/ 24/ 00 3: 52p 0.035 16,719 1.982 0.337 18,067 2.233 13,531 D0224084 SPC 2/ 24/ 00 3: 57p 0.035 16,988 1.98 0.336 18,482 2.38 13,923 D0224085 SPC 2/ 24/ 00 4: 01p 0.035 16,905 1.976 0.336 18,308 2.412 13,786 D0224086 SPC 2/ 24/ 00 4: 06p 0.038 16,654 1.981 0.336 18,136 2.19 13,535 D0224087 SPC 2/ 24/ 00 4: 10p 0.031 16,801 1.977 0.336 18,151 2.298 13,581 D0224088 SPC 2/ 24/ 00 4: 15p 0.029 16,850 1.977 0.336 18,202 2.128 13,630 D0224089 SPC 2/ 24/ 00 4: 19p 0.028 16,754 1.98 0.336 18,239 2.07 13,697 D0224090 SPC 2/ 24/ 00 4: 24p 0.036 16,662 1.985 0.336 18,053 2.222 13,476 D0224091 SPC 2/ 24/ 00 4: 28p 0.035 16,624 1.992 0.337 18,068 2.458 13,477 C 69 Table C 7. ( Continued)

Data Collection Information Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0224092 SPC 2/ 24/ 00 4: 33p 0.037 16,719 1.976 0.337 18,119 2.535 13,553 D0224093 SPC 2/ 24/ 00 4: 37p 0.036 16,740 1.982 0.336 18,153 2.623 13,632 D0224094 SPC 2/ 24/ 00 4: 42p 0.038 17,026 1.981 0.336 18,312 2.922 13,745 D0224095 SPC 2/ 24/ 00 4: 47p 0.038 16,736 1.979 0.337 18,225 3.116 13,683 D0224096 SPC 2/ 24/ 00 4: 51p 0.038 16,882 1.981 0.336 18,329 3.296 13,773 D0224097 SPC 2/ 24/ 00 4: 56p 0.04 16,785 1.98 0.336 18,242 2.971 13,720 D0224098 SPC 2/ 24/ 00 5: 00p 0.04 16,748 1.986 0.336 18,185 2.57 13,646 D0224099 SPC 2/ 24/ 00 5: 05p 0.037 16,931 1.984 0.337 18,276 2.656 13,736 D0224100 SPC 2/ 24/ 00 5: 09p 0.037 16,830 1.984 0.337 18,285 2.785 13,764 D0224101 SPC 2/ 24/ 00 5: 14p 0.039 16,774 1.98 0.337 18,214 2.699 13,687 D0224102 SPC 2/ 24/ 00 5: 18p 0.039 16,813 1.98 0.337 18,192 2.627 13,703 D0224103 SPC 2/ 24/ 00 5: 23p 0.04 16,687 1.986 0.337 18,117 2.683 13,584 D0224104 SPC 2/ 24/ 00 5: 27p 0.037 16,665 1.987 0.337 18,148 2.749 13,629 D0224105 SPC 2/ 24/ 00 5: 32p 0.038 16,770 1.987 0.337 18,149 2.864 13,635 D0224106 SPC 2/ 24/ 00 5: 37p 0.038 16,679 1.989 0.337 18,265 3.22 13,719 D0224107 SPC 2/ 24/ 00 5: 41p 0.037 16,996 1.991 0.337 18,496 3.945 13,873 D0224108 SPC 2/ 24/ 00 5: 46p 0.036 17,141 1.992 0.336 18,806 4.26 13,915 D0224109 SPC 2/ 24/ 00 5: 50p 0.036 17,163 1.997 0.337 18,732 4.028 13,949 D0224110 SPC 2/ 24/ 00 5: 55p 0.036 17,108 1.993 0.337 18,706 3.761 13,968 D0224111 SPC 2/ 24/ 00 5: 59p 0.038 17,035 1.99 0.337 18,691 3.67 13,962 D0224112 SPC 2/ 24/ 00 6: 04p 0.039 17,090 1.989 0.337 18,672 3.59 13,967 D0224113 SPC 2/ 24/ 00 6: 08p 0.038 17,143 1.991 0.337 18,840 3.689 14,023 D0224114 SPC 2/ 24/ 00 6: 13p 0.035 17,243 1.995 0.337 18,862 3.704 14,050 D0224115 SPC 2/ 24/ 00 6: 17p 0.04 17,338 2.001 0.338 18,970 3.766 14,037 D0224116 SPC 2/ 24/ 00 6: 22p 0.036 17,245 1.999 0.338 19,084 3.809 14,113 D0224117 SPC 2/ 24/ 00 6: 26p 0.038 17,400 2.004 0.338 19,276 4.061 14,202 D0224118 SPC 2/ 24/ 00 6: 31p 0.037 17,563 2.02 0.339 19,342 4.386 14,222 D0224119 SPC 2/ 24/ 00 6: 36p 0.035 17,648 2.023 0.339 19,346 4.824 14,248 D0224120 SPC 2/ 24/ 00 6: 40p 0.036 17,661 2.02 0.34 19,371 4.874 14,280 D0224121 SPC 2/ 24/ 00 6: 45p 0.037 17,635 2.023 0.339 19,325 4.388 14,260 C 70 Table C 7. ( Continued)

Data Collection Information Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0224122 SPC 2/ 24/ 00 6: 49p 0.034 17,749 2.032 0.34 19,354 4.052 14,270 D0224123 SPC 2/ 24/ 00 6: 54p 0.034 17,627 2.031 0.339 19,353 3.892 14,299 D0224124 SPC 2/ 24/ 00 6: 58p 0.036 17,658 2.054 0.34 19,396 4.202 14,281 D0224125 SPC 2/ 24/ 00 7: 03p 0.036 17,758 2.054 0.34 19,537 4.674 14,351 D0224126 SPC 2/ 24/ 00 7: 07p 0.036 17,772 2.046 0.34 19,684 5.284 14,463 D0224127 SPC 2/ 24/ 00 7: 12p 0.035 18,045 2.048 0.341 19,703 5.333 14,517 D0224128 SPC 2/ 24/ 00 7: 16p 0.035 17,935 2.049 0.341 19,682 5.307 14,489 D0224129 SPC 2/ 24/ 00 7: 21p 0.035 17,868 2.041 0.341 19,657 5.225 14,493 D0224130 SPC 2/ 24/ 00 7: 25p 0.034 17,877 2.039 0.341 19,669 4.833 14,530 D0224131 SPC 2/ 24/ 00 7: 30p 0.034 17,982 2.051 0.341 19,737 4.889 14,567 D0224132 SPC 2/ 24/ 00 7: 35p 0.033 17,906 2.048 0.342 19,704 4.842 14,545 D0224133 SPC 2/ 24/ 00 7: 39p 0.034 17,956 2.046 0.342 19,616 4.581 14,489 D0224134 SPC 2/ 24/ 00 7: 44p 0.036 17,758 2.047 0.341 19,569 4.397 14,478 D0224135 SPC 2/ 24/ 00 7: 48p 0.033 17,843 2.039 0.341 19,533 4.761 14,478 D0224136 SPC 2/ 24/ 00 7: 53p 0.034 17,778 2.036 0.341 19,549 5.522 14,475 D0224137 SPC 2/ 24/ 00 7: 57p 0.036 17,174 2.014 0.34 19,177 4.329 14,251 D0224138 SPC 2/ 24/ 00 8: 02p 0.034 17,287 2.024 0.34 19,005 3.553 14,144 D0224139 SPC 2/ 24/ 00 8: 06p 0.037 17,303 2.031 0.341 19,062 3.153 14,215 D0224140 SPC 2/ 24/ 00 8: 11p 0.039 16,889 2.033 0.343 18,539 2.755 14,072 D0224141 SPC 2/ 24/ 00 8: 15p 0.041 16,778 2.044 0.344 18,398 2.452 13,968 D0224142 SPC 2/ 24/ 00 8: 20p 0.039 16,676 2.037 0.344 18,274 2.578 13,908 D0224143 SPC 2/ 24/ 00 8: 24p 0.036 16,637 2.028 0.344 18,147 2.587 13,763 D0224144 SPC 2/ 24/ 00 8: 29p 0.04 16,551 2.027 0.344 18,125 2.549 13,739 D0224145 SPC 2/ 24/ 00 8: 33p 0.043 16,555 2.029 0.345 18,043 2.664 13,647 D0224146 SPC 2/ 24/ 00 8: 38p 0.042 16,444 2.036 0.346 17,919 2.706 13,566 D0224147 SPC 2/ 24/ 00 8: 43p 0.043 16,417 2.048 0.347 17,864 2.708 13,498 D0224148 SPC 2/ 24/ 00 8: 47p 0.04 16,377 2.036 0.347 17,912 2.621 13,583 D0224149 SPC 2/ 24/ 00 8: 52p 0.039 16,260 2.037 0.347 17,835 2.575 13,507 D0224150 SPC 2/ 24/ 00 8: 56p 0.039 16,152 2.034 0.349 17,690 2.776 13,362 D0224151 SPC 2/ 24/ 00 9: 01p 0.04 16,142 2.033 0.349 17,603 2.782 13,335 C 71 Table C 7. ( Continued)

Data Collection Information Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0224152 SPC 2/ 24/ 00 9: 05p 0.042 15,929 2.028 0.349 17,524 2.731 13,226 D0224153 SPC 2/ 24/ 00 9: 10p 0.043 15,819 2.028 0.349 17,372 2.607 13,075 D0224154 SPC 2/ 24/ 00 9: 14p 0.04 15,755 2.048 0.35 17,235 2.671 12,995 D0224155 SPC 2/ 24/ 00 9: 19p 0.041 15,694 2.038 0.35 17,184 2.673 12,950 D0224156 SPC 2/ 24/ 00 9: 23p 0.042 15,678 2.034 0.348 17,131 2.653 12,895 D0224157 SPC 2/ 24/ 00 9: 28p 0.041 15,857 2.042 0.35 17,179 2.457 12,924 D0224158 SPC 2/ 24/ 00 9: 32p 0.04 15,583 2.043 0.349 17,086 2.37 12,839 D0224159 SPC 2/ 24/ 00 9: 37p 0.039 15,484 2.046 0.35 17,010 2.281 12,783 D0224160 SPC 2/ 24/ 00 9: 41p 0.037 15,480 2.054 0.348 16,977 2.374 12,744 D0224161 SPC 2/ 24/ 00 9: 46p 0.04 15,360 2.069 0.348 16,910 2.495 12,673 D0224162 SPC 2/ 24/ 00 9: 51p 0.042 15,493 2.076 0.349 16,974 2.484 12,684 D0224163 SPC 2/ 24/ 00 9: 55p 0.041 15,224 2.103 0.35 16,768 2.502 12,519 D0224164 SPC 2/ 24/ 00 10: 00p 0.04 15,199 2.134 0.35 16,757 2.519 12,481 D0224165 SPC 2/ 24/ 00 10: 04p 0.04 15,067 2.082 0.349 16,811 2.485 12,594 D0224166 SPC 2/ 24/ 00 10: 09p 0.041 14,864 2.065 0.349 16,832 2.444 12,626 D0224167 SPC 2/ 24/ 00 10: 13p 0.043 15,255 2.066 0.35 16,857 2.427 12,653 D0224168 SPC 2/ 24/ 00 10: 18p 0.044 15,219 2.053 0.349 16,803 2.326 12,607 D0224169 SPC 2/ 24/ 00 10: 22p 0.044 15,076 2.065 0.349 16,780 2.298 12,605 D0224170 SPC 2/ 24/ 00 10: 27p 0.042 15,211 2.084 0.349 16,777 2.197 12,587 D0224171 SPC 2/ 24/ 00 10: 32p 0.041 15,348 2.114 0.35 16,772 2.077 12,581 D0224172 SPC 2/ 24/ 00 10: 36p 0.043 15,169 2.054 0.351 16,668 2.082 12,509 D0224173 SPC 2/ 24/ 00 10: 41p 0.044 14,929 2.061 0.35 16,328 2.236 12,303 D0224174 SPC 2/ 24/ 00 10: 45p 0.041 14,820 2.045 0.352 16,085 2.261 12,208 D0224175 SPC 2/ 24/ 00 10: 50p 0.042 15,067 2.046 0.35 16,517 2.099 12,391 D0224176 SPC 2/ 24/ 00 10: 54p 0.041 15,063 2.056 0.349 16,528 2.058 12,377 D0224177 SPC 2/ 24/ 00 10: 59p 0.044 14,954 2.062 0.349 16,478 2.087 12,358 D0224178 SPC 2/ 24/ 00 11: 03p 0.041 14,992 2.057 0.349 16,425 2.159 12,332 D0224179 SPC 2/ 24/ 00 11: 08p 0.041 14,904 2.052 0.35 16,286 2.174 12,255 D0224180 SPC 2/ 24/ 00 11: 12p 0.041 14,855 2.122 0.352 16,123 2.048 12,150 D0224181 SPC 2/ 24/ 00 11: 17p 0.044 14,908 2.059 0.35 16,190 1.965 12,210 C 72 Table C 7. ( Continued)

Data Collection Information Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0224182 SPC 2/ 24/ 00 11: 22p 0.045 14,793 2.048 0.35 16,256 1.963 12,280 D0224183 SPC 2/ 24/ 00 11: 26p 0.041 14,897 2.048 0.349 16,239 1.974 12,262 D0224184 SPC 2/ 24/ 00 11: 31p 0.043 14,738 2.084 0.351 15,868 2.061 12,031 D0224185 SPC 2/ 24/ 00 11: 35p 0.044 14,561 2.077 0.352 15,812 2.059 12,000 D0224186 SPC 2/ 24/ 00 11: 40p 0.044 14,699 2.055 0.351 15,884 1.973 12,066 D0224187 SPC 2/ 24/ 00 11: 44p 0.041 14,671 2.051 0.351 16,085 1.952 12,179 D0224188 SPC 2/ 24/ 00 11: 49p 0.041 15,052 2.053 0.35 16,540 1.914 12,396 D0224189 SPC 2/ 24/ 00 11: 53p 0.038 15,075 2.052 0.35 16,543 1.938 12,393 D0224190 SPC 2/ 24/ 00 11: 58p 0.04 15,188 2.054 0.349 16,718 1.986 12,494 D0224191 SPC 2/ 25/ 00 12: 02a 0.039 15,212 2.07 0.348 16,727 2.099 12,541 D0224192 SPC 2/ 25/ 00 12: 07a 0.043 15,322 2.076 0.348 16,819 2.247 12,630 D0224193 SPC 2/ 25/ 00 12: 12a 0.041 15,391 2.083 0.35 16,952 2.304 12,713 D0224194 SPC 2/ 25/ 00 12: 16a 0.045 15,368 2.1 0.35 16,927 2.307 12,692 D0224195 SPC 2/ 25/ 00 12: 21a 0.043 15,336 2.119 0.348 16,902 2.433 12,592 D0224196 SPC 2/ 25/ 00 12: 25a 0.043 15,308 2.111 0.348 16,953 2.942 12,684 D0224197 SPC 2/ 25/ 00 12: 30a 0.044 15,450 2.094 0.35 16,994 3.955 12,644 D0224198 SPC 2/ 25/ 00 12: 34a 0.041 15,236 2.094 0.349 16,769 4.159 12,454 D0224199 SPC 2/ 25/ 00 12: 39a 0.04 14,940 2.084 0.351 16,250 4.071 12,113 D0224200 SPC 2/ 25/ 00 12: 43a 0.041 14,671 2.076 0.352 15,869 3.374 12,001 D0224201 SPC 2/ 25/ 00 12: 48a 0.043 14,306 2.063 0.353 15,553 2.813 11,793 D0224202 SPC 2/ 25/ 00 12: 53a 0.042 14,182 2.058 0.354 15,453 2.66 11,706 D0224203 SPC 2/ 25/ 00 12: 57a 0.041 14,210 2.059 0.354 15,623 2.894 11,861 D0224204 SPC 2/ 25/ 00 1: 02a 0.039 14,409 2.049 0.355 15,669 2.714 11,935 D0224205 SPC 2/ 25/ 00 1: 06a 0.042 14,295 2.053 0.355 15,487 2.494 11,752 D0224206 SPC 2/ 25/ 00 1: 11a 0.041 14,069 2.058 0.354 15,391 2.381 11,648 D0224207 SPC 2/ 25/ 00 1: 15a 0.044 14,063 2.061 0.355 15,298 2.273 11,590 D0224208 SPC 2/ 25/ 00 1: 20a 0.042 13,633 2.062 0.356 14,925 2.242 11,158 D0224209 SPC 2/ 25/ 00 1: 25a 0.042 13,382 2.064 0.357 14,649 2.269 10,949 D0224210 SPC 2/ 25/ 00 1: 29a 0.042 13,213 2.066 0.357 14,472 2.241 10,739 D0224211 SPC 2/ 25/ 00 1: 34a 0.04 13,227 2.07 0.357 14,498 2.208 10,798 C 73 Table C 7. ( Continued)

Data Collection Information Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0224212 SPC 2/ 25/ 00 1: 38a 0.042 13,334 2.061 0.357 14,583 2.132 10,861 D0224213 SPC 2/ 25/ 00 1: 43a 0.043 13,429 2.06 0.356 14,643 2.121 10,906 D0224214 SPC 2/ 25/ 00 1: 47a 0.042 13,404 2.062 0.356 14,644 2.118 10,934 D0224215 SPC 2/ 25/ 00 1: 52a 0.043 13,330 2.087 0.357 14,523 2.093 10,818 D0224216 SPC 2/ 25/ 00 1: 56a 0.042 13,253 2.067 0.357 14,474 2.135 10,794 D0224217 SPC 2/ 25/ 00 2: 01a 0.041 13,367 2.068 0.357 14,565 2.159 10,871 D0224218 SPC 2/ 25/ 00 2: 05a 0.042 13,215 2.066 0.357 14,405 2.187 10,733 D0224219 SPC 2/ 25/ 00 2: 10a 0.044 13,106 2.064 0.357 14,260 2.158 10,591 D0224220 SPC 2/ 25/ 00 2: 15a 0.042 13,088 2.095 0.358 14,187 2.121 10,497 D0224221 SPC 2/ 25/ 00 2: 19a 0.04 12,785 2.12 0.358 13,858 2.189 10,272 D0224222 SPC 2/ 25/ 00 2: 24a 0.042 12,681 2.089 0.358 13,998 2.229 10,346 D0224223 SPC 2/ 25/ 00 2: 28a 0.04 12,802 2.087 0.357 13,810 2.345 10,264 D0224224 SPC 2/ 25/ 00 2: 33a 0.039 12,942 2.122 0.357 14,180 2.56 10,445 D0224225 SPC 2/ 25/ 00 2: 37a 0.042 13,357 2.132 0.357 14,565 2.609 10,773 D0224226 SPC 2/ 25/ 00 2: 42a 0.046 13,095 2.156 0.358 14,222 2.834 10,435 D0224227 SPC 2/ 25/ 00 2: 46a 0.044 12,971 2.133 0.357 14,141 2.716 10,344 D0224228 SPC 2/ 25/ 00 2: 51a 0.043 13,130 2.141 0.357 14,295 2.501 10,521 D0224229 SPC 2/ 25/ 00 2: 56a 0.044 13,248 2.137 0.357 14,428 2.694 10,687 D0224230 SPC 2/ 25/ 00 3: 00a 0.043 13,082 2.121 0.357 14,333 2.498 10,592 D0224231 SPC 2/ 25/ 00 3: 05a 0.038 13,057 2.102 0.358 14,282 2.512 10,591 D0224232 SPC 2/ 25/ 00 3: 09a 0.04 13,177 2.116 0.358 14,370 2.842 10,657 D0224233 SPC 2/ 25/ 00 3: 14a 0.046 12,987 2.121 0.358 14,349 3.222 10,583 D0224234 SPC 2/ 25/ 00 3: 18a 0.042 13,493 2.136 0.356 14,754 4.074 10,896 D0224235 SPC 2/ 25/ 00 3: 23a 0.042 13,626 2.142 0.356 14,922 4.844 11,025 D0224236 SPC 2/ 25/ 00 3: 28a 0.043 13,038 2.161 0.358 14,241 4.142 10,375 D0224237 SPC 2/ 25/ 00 3: 32a 0.042 13,073 2.164 0.358 14,349 3.483 10,457 D0224238 SPC 2/ 25/ 00 3: 37a 0.043 13,180 2.158 0.357 14,433 3.386 10,520 D0224239 SPC 2/ 25/ 00 3: 41a 0.043 13,253 2.161 0.357 14,454 3.197 10,576 D0224240 SPC 2/ 25/ 00 3: 46a 0.044 13,129 2.136 0.358 14,369 3.122 10,510 D0224241 SPC 2/ 25/ 00 3: 50a 0.044 13,103 2.126 0.358 14,408 3.156 10,497 C 74 C 74 Table C 7. ( Continued)

Data Collection Information Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0224242 SPC 2/ 25/ 00 3: 55a 0.043 12,882 2.105 0.358 14,113 2.927 10,341 D0224243 SPC 2/ 25/ 00 3: 59a 0.04 12,667 2.107 0.358 13,583 2.78 10,138 D0224244 SPC 2/ 25/ 00 4: 04a 0.041 12,294 2.118 0.359 13,187 2.748 9,827 D0224245 SPC 2/ 25/ 00 4: 09a 0.042 12,419 2.116 0.359 13,298 2.774 9,936 D0224246 SPC 2/ 25/ 00 4: 13a 0.043 12,399 2.099 0.359 13,227 2.706 9,878 D0224247 SPC 2/ 25/ 00 4: 18a 0.044 12,342 2.12 0.359 13,289 2.731 9,930 D0224248 SPC 2/ 25/ 00 4: 22a 0.043 12,387 2.171 0.359 13,204 2.614 9,839 D0224249 SPC 2/ 25/ 00 4: 27a 0.042 12,162 2.123 0.36 13,039 2.496 9,742 D0224250 SPC 2/ 25/ 00 4: 31a 0.044 11,968 2.109 0.36 12,906 2.421 9,593 D0224251 SPC 2/ 25/ 00 4: 36a 0.044 11,912 2.099 0.36 12,871 2.393 9,580 D0224252 SPC 2/ 25/ 00 4: 41a 0.042 12,021 2.106 0.36 12,974 2.53 9,664 D0224253 SPC 2/ 25/ 00 4: 45a 0.042 12,223 2.116 0.359 13,052 2.618 9,754 D0224254 SPC 2/ 25/ 00 4: 50a 0.041 12,178 2.109 0.36 13,096 2.31 9,789 D0224255 SPC 2/ 25/ 00 4: 54a 0.045 12,246 2.1 0.361 13,160 2.09 9,876 D0224256 SPC 2/ 25/ 00 4: 59a 0.043 12,229 2.153 0.362 13,061 2.157 9,755 D0224257 SPC 2/ 25/ 00 5: 03a 0.043 11,977 2.173 0.362 12,873 2.198 9,551 D0224258 SPC 2/ 25/ 00 5: 08a 0.043 11,817 2.172 0.362 12,755 2.244 9,429 D0224259 SPC 2/ 25/ 00 5: 13a 0.039 11,784 2.175 0.363 12,657 2.26 9,316 D0224260 SPC 2/ 25/ 00 5: 17a 0.043 11,553 2.152 0.363 12,452 2.292 9,154 D0224261 SPC 2/ 25/ 00 5: 22a 0.042 11,639 2.172 0.362 12,579 2.293 9,246 D0224262 SPC 2/ 25/ 00 5: 26a 0.045 11,899 2.15 0.361 12,801 2.288 9,495 D0224263 SPC 2/ 25/ 00 5: 31a 0.045 11,959 2.168 0.361 12,914 2.391 9,568 D0224264 SPC 2/ 25/ 00 5: 35a 0.043 12,038 2.148 0.361 12,935 2.411 9,582 D0224265 SPC 2/ 25/ 00 5: 40a 0.046 11,871 2.137 0.361 12,830 2.323 9,513 D0224266 SPC 2/ 25/ 00 5: 45a 0.042 11,809 2.138 0.361 12,759 2.379 9,476 D0224267 SPC 2/ 25/ 00 5: 49a 0.042 11,673 2.138 0.362 12,546 2.367 9,267 D0224268 SPC 2/ 25/ 00 5: 54a 0.043 11,586 2.208 0.363 12,467 2.342 9,152 D0224269 SPC 2/ 25/ 00 5: 58a 0.042 11,563 2.202 0.363 12,380 2.311 9,074 D0224270 SPC 2/ 25/ 00 6: 03a 0.043 11,592 2.189 0.363 12,429 2.288 9,150 D0224271 SPC 2/ 25/ 00 6: 07a 0.041 11,629 2.219 0.363 12,497 2.282 9,179 C 75 C 75 Table C 7. ( Continued)

Data Collection Information Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water D0224272 SPC 2/ 25/ 00 6: 12a 0.041 11,632 2.255 0.363 12,596 2.249 9,267 D0224273 SPC 2/ 25/ 00 6: 16a 0.041 11,889 2.619 0.365 12,861 2.412 9,386 D0224274 SPC 2/ 25/ 00 6: 21a 0.042 12,113 2.473 0.365 13,019 2.943 9,558 D0224275 SPC 2/ 25/ 00 6: 26a 0.044 11,887 2.304 0.364 12,828 2.836 9,444 D0224276 SPC 2/ 25/ 00 6: 30a 0.043 11,873 2.253 0.364 12,794 2.783 9,451 D0224277 SPC 2/ 25/ 00 6: 35a 0.042 11,846 2.268 0.363 12,777 2.736 9,386 D0224278 SPC 2/ 25/ 00 6: 39a 0.043 11,713 2.407 0.365 12,751 2.657 9,318 D0224279 SPC 2/ 25/ 00 6: 44a 0.042 11,838 2.457 0.365 12,798 2.575 9,361 D0224280 SPC 2/ 25/ 00 6: 48a 0.04 12,011 2.46 0.365 12,853 2.515 9,444 D0224281 SPC 2/ 25/ 00 6: 53a 0.041 11,894 2.515 0.365 12,867 2.531 9,410 D0224282 SPC 2/ 25/ 00 6: 58a 0.039 11,833 2.479 0.365 12,821 2.54 9,381 D0224283 SPC 2/ 25/ 00 7: 02a 0.037 11,665 2.441 0.365 12,640 2.516 9,228 D0224284 SPC 2/ 25/ 00 7: 07a 0.042 11,511 2.406 0.365 12,504 2.522 9,142 D0224285 SPC 2/ 25/ 00 7: 11a 0.042 11,447 2.706 0.368 12,525 2.539 9,037 D0224286 SPC 2/ 25/ 00 7: 16a 0.039 11,597 2.653 0.368 12,587 2.559 9,070 D0224287 SPC 2/ 25/ 00 7: 20a 0.04 11,457 2.726 0.369 12,497 2.577 8,921 D0224288 SPC 2/ 25/ 00 7: 25a 0.042 11,696 2.746 0.368 12,748 2.62 9,190 D0224289 SPC 2/ 25/ 00 7: 29a 0.042 11,756 2.709 0.368 12,786 2.749 9,200 D0224290 SPC 2/ 25/ 00 7: 34a 0.054 11,023 2.691 0.367 12,889 2.759 9,322 D0224291 SPC 2/ 25/ 00 7: 39a 0.059 10,623 2.744 0.369 12,699 2.795 9,046 D0224292 SPC 2/ 25/ 00 7: 43a 0.013 11,605 2.812 0.369 12,692 2.872 8,907 D0224293 SPC 2/ 25/ 00 7: 48a 0.006 11,629 2.886 0.37 12,735 2.999 8,881 D0224294 SPC 2/ 25/ 00 7: 52a 0.003 11,797 2.77 0.368 12,906 3.053 9,226 D0224295 SPC 2/ 25/ 00 7: 57a 0.002 12,090 2.591 0.366 13,153 2.841 9,564 D0224296 SPC 2/ 25/ 00 8: 01a 0.001 12,221 2.62 0.366 13,280 2.79 9,685 D0224297 SPC 2/ 25/ 00 8: 06a 0 12,257 2.551 0.365 13,291 2.809 9,709 D0224298 SPC 2/ 25/ 00 8: 11a 0 12,322 2.499 0.364 13,331 2.776 9,808 D0224299 SPC 2/ 25/ 00 8: 15a 0 12,475 2.462 0.364 13,445 2.775 9,926 D0224300 SPC 2/ 25/ 00 8: 20a 0 12,707 2.566 0.365 14,021 2.926 10,171 D0224301 SPC 2/ 25/ 00 8: 24a 0 12,872 2.564 0.364 14,273 2.917 10,323 C 76 Table C 7. ( Continued)

Data Collection Information Quantification Method Concentrations in ppm Olin Mercury Plant Olin 2 Olin 3 File Date Time sulfur hexafluoride water carbon monoxide nitrous oxide water methane Water C 77 D0224302 SPC 2/ 25/ 00 8: 29a 0 13,065 2.491 0.363 14,447 2.838 10,543 D0224303 SPC 2/ 25/ 00 8: 33a 0 13,233 2.468 0.369 14,661 2.841 10,766 D0224304 SPC 2/ 25/ 00 8: 38a 0 13,306 2.485 0.374 14,762 2.966 10,874 D0224305 SPC 2/ 25/ 00 8: 43a 0 13,420 2.489 0.375 14,835 3.054 10,877 D0224306 SPC 2/ 25/ 00 8: 47a 0 13,500 2.502 0.377 14,912 3.136 10943 D i Appendix D Roof Vent Manual Velocity Data D ii C 79 ( Intentionally Blank) Table D 1. East Platform: Hand Held Anemometer Data At LOA Beam Height Date Sampling Location Points  3  2  1 1 2 3 4 5 6 7 8 9 10 11 12 Average 2/ 22 Meters Fm. S. Wall  0.41  0.2 0.41 0.81 1.2 1.6 2.0 2.4 2.84 3.25 3.66 4.06 4.57 4.88 Inches Fm. S. Wall  16  8 16 32 48 64 80 96 112 128 144 160 180 192 1545 hrs ( Prop) 0 0.6 1 1.1 1.1 1.5 1.5 0.4 1.1 1.1 1.2 1.8 0.6 0 0.9 2/ 23 Meters Fm. S. Wall  0.51  0.1 0 0.41 0.81 1.2 1.6 2.0 2.4 2.84 3.25 3.66 4.06 4.52 4.57 Inches Fm. S. Wall  20  4 0 16 32 48 64 80 96 112 128 144 160 178 180 ~ 1008 hrs ( Prop) 0 0.6 1.2 1.4 1.6 1.6 1.4 1.7 0.1 0.6 0.9 1.2 1.4 0.6 0 1 ~ 1021 hrs ( Hot Wire) 1.5 2 2 1.7 1.6 1.4 0.8 1.2 1.5 1.4 1.9 1.2 1.5 Table D 2. West Platform: Hand Held Anemometer Data At LOA Beam Height Date Sampling Location Points + 3 + 2 + 1 10 9 8 7 6 5 4 3 2 1  1  2  3 Average 2/ 22 Meters Fm. S. Wall 0.05 0.2 0.2 0.61 1.0 1.4 1.8 2.2 2.64 3.05 3.45 3.86 4.27 4.67 4.78 5.08 Inches Fm. S. Wall 2 6 8 24 40 56 72 88 104 120 136 152 168 184 188 200 1500 hrs ( Prop) 0 0.6 1.1 1.7 1.4 0.9 1 0.8 0.8 0.8 1.2 1.5 1.4 1 0.6 0 0.9 2/ 23 1030 hrs ( Prop) 0 0.6 1.6 1.7 1.2 1.1 0.8 0.3 0.5 0.9 1 1.5 1.7 1.2 0.6 0 0.9 D 1 E i Appendix E Manual Velocity Data for Cell Building Openings and Associated Flow Balance Calculations E ii ( Intentionally Blank) Table E 1. Hand Held Velocity Measurements in Cell Building Openings on 2/ 24/ 00a Velocity Sampling Point Approximate " X" Coordinate ( ft from NE corner) b Approximat e " Y" Coordinate ( ft above curb) Available Open Area ( ft2) " Prop" Air Velocity ( m/ s) " Prop" Air Velocity ( fpm) " Prop"

Vol. Flowrate ( acfm) Std. Flowrate ( wscf/ min ) " Hot Wire" Air Velocity ( fpm) " Hot Wire" Vol.

Flowrate ( acfm) Std. Flowrate ( wscf/ min )

1a 8.25 9.87 109 1.1 2.2E+ 02 2.4E+ 04 2.6E+ 04 310 3.38E+ 04 3.63E+ 04 1b 8.25 3.29 109 0.65 1.3E+ 02 1.4E+ 04 1.5E+ 04 245 2.67E+ 04 2.87E+ 04 2a 24.75 9.87 109 1.1 2.2E+ 02 2.4E+ 04 2.6E+ 04 410 4.47E+ 04 4.81E+ 04 2b ( C Filter) 29.84 3.29 50.6 0.7 1.4E+ 02 7.1E+ 03 7.6E+ 03 385 1.95E+ 04 2.10E+ 04 3a 41.25 9.87 109 1.3 2.6E+ 02 2.8E+ 04 3.0E+ 04 395 4.31E+ 04 4.63E+ 04 3b 41.25 3.29 109 1.1 2.2E+ 02 2.4E+ 04 2.6E+ 04 290 3.16E+ 04 3.40E+ 04 4a 57.75 9.87 109 1.1 2.2E+ 02 2.4E+ 04 2.6E+ 04 270 2.94E+ 04 3.16E+ 04 4b 57.75 3.29 109 0.9 1.8E+ 02 2.0E+ 04 2.1E+ 04 290 3.16E+ 04 3.40E+ 04 5a 74.25 9.87 109 1 2.0E+ 02 2.2E+ 04 2.4E+ 04 240 2.62E+ 04 2.82E+ 04 5b 74.25 3.29 109 0.7 1.4E+ 02 1.5E+ 04 1.6E+ 04 260 2.83E+ 04 3.04E+ 04 6a 90.75 9.87 109 0.7 1.4E+ 02 1.5E+ 04 1.6E+ 04 245 2.67E+ 04 2.87E+ 04 6b 90.75 3.29 109 0.2 3.9E+ 01 4.3E+ 03 4.6E+ 03 215 2.34E+ 04 2.52E+ 04 7a 8.25 9.87 109 1 2.0E+ 02 2.2E+ 04 2.4E+ 04 240 2.62E+ 04 2.81E+ 04 7b 8.25 3.29 109 0.8 1.6E+ 02 1.7E+ 04 1.8E+ 04 190 2.07E+ 04 2.22E+ 04 8a 24.75 9.87 109 0.8 1.6E+ 02 1.7E+ 04 1.8E+ 04 245 2.67E+ 04 2.87E+ 04 8b 24.75 3.29 109 0.3 5.9E+ 01 6.4E+ 03 6.9E+ 03 195 2.13E+ 04 2.29E+ 04 9a 41.25 9.87 109 0.8 1.6E+ 02 1.7E+ 04 1.8E+ 04 220 2.40E+ 04 2.58E+ 04 9b 41.25 3.29 109 0.1 2.0E+ 01 2.2E+ 03 2.4E+ 03 50 5.45E+ 03 5.85E+ 03 10a 57.75 9.87 109 0.8 1.6E+ 02 1.7E+ 04 1.8E+ 04 245 2.67E+ 04 2.87E+ 04 10b 57.75 3.29 109 0.5 9.8E+ 01 1.1E+ 04 1.2E+ 04 197 2.15E+ 04 2.31E+ 04 11a 74.25 9.87 109 0.5 9.8E+ 01 1.1E+ 04 1.2E+ 04 215 2.34E+ 04 2.51E+ 04 11b 74.25 3.29 109 0.2 3.9E+ 01 4.3E+ 03 4.6E+ 03 113 1.23E+ 04 1.32E+ 04 12a 90.75 9.87 109 0.8 1.6E+ 02 1.7E+ 04 1.8E+ 04 205 2.23E+ 04 2.39E+ 04 12b 90.75 3.29 109 0.3 5.9E+ 01 6.4E+ 03 6.9E+ 03 150 1.64E+ 04 1.76E+ 04 13a 8.25 9.87 109 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 16 1.74E+ 03 1.87E+ 03 13b 8.25 3.29 109 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 11 1.20E+ 03 1.29E+ 03 14 ( Small Door) N/ A N/ A 100 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 108 1.08E+ 04 1.16E+ 04 15 ( Large Door) N/ A N/ A 252 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 65 1.64E+ 04 1.76E+ 04 16a 87.92 2.39 17.2 0.9 1.8E+ 02 3.1E+ 03 3.3E+ 03 153 2.63E+ 03 2.83E+ 03 16b 87.92 0.8 17.2 0.9 1.8E+ 02 3.1E+ 03 3.3E+ 03 131 2.25E+ 03 2.42E+ 03 17a 72.09 2.39 19.4 0.7 1.4E+ 02 2.7E+ 03 2.9E+ 03 225 4.37E+ 03 4.70E+ 03 17b 72.09 0.8 19.4 0.8 1.6E+ 02 3.1E+ 03 3.3E+ 03 177 3.43E+ 03 3.69E+ 03 18a 41.25 2.39 26.2 1 2.0E+ 02 5.2E+ 03 5.6E+ 03 265 6.94E+ 03 7.46E+ 03 E 1 Table E 1. ( Continued)

Velocity Sampling Point Approximate " X" Coordinate ( ft from NE corner) b Approximat e " Y" Coordinate ( ft above curb) Available Open Area ( ft2) " Prop" Air Velocity ( m/ s) " Prop" Air Velocity ( fpm) " Prop"

Vol. Flowrate ( acfm) Std. Flowrate ( wscf/ min ) " Hot Wire" Air Velocity ( fpm) " Hot Wire" Vol.

Flowrate ( acfm) Std. Flowrate ( wscf/ min )

18b 41.25 0.8 26.2 1 2.0E+ 02 5.2E+ 03 5.6E+ 03 83 2.17E+ 03 2.33E+ 03 20a 24.75 5 9.17 0.3 5.9E+ 01 5.4E+ 02 5.8E+ 02 88 8.07E+ 02 8.67E+ 02 20b 24.75 1.67 9.17 0.8 1.6E+ 02 1.5E+ 03 1.6E+ 03 200 1.83E+ 03 1.97E+ 03 21a 12.29 2.39 13.4 0.3 5.9E+ 01 7.9E+ 02 8.5E+ 02 53 7.10E+ 02 7.63E+ 02 21b 12.29 0.8 13.4 0.3 5.9E+ 01 7.9E+ 02 8.5E+ 02 100 1.34E+ 03 1.44E+ 03 22a 11.09 2.39 17.2 0.7 1.4E+ 02 2.4E+ 03 2.6E+ 03 184 3.16E+ 03 3.40E+ 03 22b 11.09 0.8 17.2 0.7 1.4E+ 02 2.4E+ 03 2.6E+ 03 130 2.24E+ 03 2.41E+ 03 23a 19.34 2.39 9.02 0.3 5.9E+ 01 5.3E+ 02 5.7E+ 02 130 1.17E+ 03 1.26E+ 03 23b 19.34 0.8 9.02 0.6 1.2E+ 02 1.1E+ 03 1.2E+ 03 100 9.02E+ 02 9.70E+ 02 24a 41.25 2.39 26.2 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 20 5.24E+ 02 5.63E+ 02 24b 41.25 0.8 26.2 0.3 5.9E+ 01 1.5E+ 03 1.6E+ 03 87 2.28E+ 03 2.45E+ 03 25a 64.46 5 10.3  0.3  5.9E+ 01  6.1E+ 02  6.6E+ 02 140 1.44E+ 03 1.55E+ 03 25b 64.46 1.67 10.3 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 50 5.15E+ 02 5.54E+ 02 26a 100.5 5 10.0 0.3 5.9E+ 01 5.9E+ 02 6.3E+ 02 126 1.26E+ 03 1.35E+ 03 26b 100.5 1.67 10.0 0.3 5.9E+ 01 5.9E+ 02 6.3E+ 02 62 6.20E+ 02 6.66E+ 02 27a 123.8 2.39 26.2 0.3 5.9E+ 01 1.5E+ 03 1.6E+ 03 137 3.59E+ 03 3.86E+ 03 27b 123.8 0.8 26.2 0.5 9.8E+ 01 2.6E+ 03 2.8E+ 03 156 4.09E+ 03 4.40E+ 03 28a 140.3 2.39 26.2 0.5 9.8E+ 01 2.6E+ 03 2.8E+ 03 90 2.36E+ 03 2.54E+ 03 28b 140.3 0.8 26.2 0.5 9.8E+ 01 2.6E+ 03 2.8E+ 03 158 4.14E+ 03 4.45E+ 03 29a 156.8 5 9.44 0.4 7.9E+ 01 7.5E+ 02 8.1E+ 02 45 4.25E+ 02 4.57E+ 02 29b 156.8 1.67 9.44 0.6 1.2E+ 02 1.1E+ 03 1.2E+ 03 120 1.13E+ 03 1.21E+ 03 No. of Fansc 11 2.43E+ 05 2.61E+ 05 2.43E+ 05 2.61E+ 05 Totals 3567.46 6.6E+ 05 7.1E+ 05 9.41E+ 05 1.01E+ 06 Volume of moist air mix @ inlet ( v 1 = actual ft3/ lb m) 12.735 a fpm = ft/ min; acfm = actual ft3/ min; and wscf/ min = wet standard ft3/ min.

b Points 22 29 from SE corner.

c Assumes fan ratings = 22,100 acfm each.

E 2 E 2 Table E 2. ( Continued)

Table E 2. Hand Held Velocity Measurements in Cell Building Openings on 2/ 25/ 00a Velocity Sampling Point Approximate " X" Coordinate ( ft from NE corner) b Approximate " Y" Coordinate ( ft above curb) Available Open Area ( ft2) " Prop" Air Velocity ( m/ s) " Prop" Air Velocity ( fpm) " Prop" Vol.

Flowrate ( acfm) Std. Flowrate ( wscf/ min)

1a 8.25 9.87 109 0.9 1.8E+ 02 2.0E+ 04 2.1E+ 04 1b 8.25 3.29 109 0.4 7.9E+ 01 8.6E+ 03 9.2E+ 03 2a 24.75 9.87 109 0.8 1.6E+ 02 1.7E+ 04 1.8E+ 04 2b ( C Filter) 29.84 3.29 50.6 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 3a 41.25 9.87 109 1 2.0E+ 02 2.2E+ 04 2.3E+ 04 3b 41.25 3.29 109 0.4 7.9E+ 01 8.6E+ 03 9.2E+ 03 4a 57.75 9.87 109 1 2.0E+ 02 2.2E+ 04 2.3E+ 04 4b 57.75 3.29 109 0.5 9.8E+ 01 1.1E+ 04 1.2E+ 04 5a 74.25 9.87 109 0.8 1.6E+ 02 1.7E+ 04 1.8E+ 04 5b 74.25 3.29 109 0.4 7.9E+ 01 8.6E+ 03 9.2E+ 03 6a 90.75 9.87 109 0.3 5.9E+ 01 6.4E+ 03 6.8E+ 03 6b 90.75 3.29 109 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 7a 8.25 9.87 109 0.7 1.4E+ 02 1.5E+ 04 1.6E+ 04 7b 8.25 3.29 109 0.4 7.9E+ 01 8.6E+ 03 9.2E+ 03 8a 24.75 9.87 109 0.6 1.2E+ 02 1.3E+ 04 1.4E+ 04 8b 24.75 3.29 109 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 9a 41.25 9.87 109 0.5 9.8E+ 01 1.1E+ 04 1.2E+ 04 9b 41.25 3.29 109 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 10a 57.75 9.87 109 0.2 3.9E+ 01 4.3E+ 03 4.6E+ 03 10b 57.75 3.29 109 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 11a 74.25 9.87 109 0.1 2.0E+ 01 2.2E+ 03 2.3E+ 03 11b 74.25 3.29 109 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 12a 90.75 9.87 109 0.6 1.2E+ 02 1.3E+ 04 1.4E+ 04 12b 90.75 3.29 109 0.4 7.9E+ 01 8.6E+ 03 9.2E+ 03 13a 8.25 9.87 109 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 13b 8.25 3.29 109 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 14 ( Small Door) N/ A N/ A 100 0.1 2.0E+ 01 2.0E+ 03 2.1E+ 03 15 ( Large Door) N/ A N/ A 252 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 16a 87.92 2.39 17.2 0.7 1.4E+ 02 2.4E+ 03 2.6E+ 03 16b 87.92 0.8 17.2 0.7 1.4E+ 02 2.4E+ 03 2.6E+ 03 17a 72.09 2.39 19.4 0.7 1.4E+ 02 2.7E+ 03 2.9E+ 03 17b 72.09 0.8 19.4 0.8 1.6E+ 02 3.1E+ 03 3.3E+ 03 18a 41.25 2.39 26.2 1.1 2.2E+ 02 5.8E+ 03 6.2E+ 03 E 3 Table E 2. ( Continued)

Velocity Sampling Point Approximate " X" Coordinate ( ft from NE corner) b Approximate " Y" Coordinate ( ft above curb) Available Open Area ( ft2) " Prop" Air Velocity ( m/ s) " Prop" Air Velocity ( fpm) " Prop" Vol.

Flowrate ( acfm) Std. Flowrate ( wscf/ min)

18b 41.25 0.8 26.2 1 2.0E+ 02 5.2E+ 03 5.5E+ 03 20a 24.75 5 9.17 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 20b 24.75 1.67 9.17 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 21a 12.29 2.39 13.4 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 21b 12.29 0.8 13.4 0.9 1.8E+ 02 2.4E+ 03 2.6E+ 03 22a 11.09 2.39 17.2 0.5 9.8E+ 01 1.7E+ 03 1.8E+ 03 22b 11.09 0.8 17.2 0.5 9.8E+ 01 1.7E+ 03 1.8E+ 03 23a 19.34 2.39 9.02 0.5 9.8E+ 01 8.8E+ 02 9.4E+ 02 23b 19.34 0.8 9.02 0.7 1.4E+ 02 1.3E+ 03 1.4E+ 03 24a 41.25 2.39 26.2 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 24b 41.25 0.8 26.2 0.1 2.0E+ 01 5.2E+ 02 5.5E+ 02 25a 64.46 5 10.3  1  2.0E+ 02  2.1E+ 03  2.2E+ 03 25b 64.46 1.67 10.3 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 26a 100.5 5 10.0 0.3 5.9E+ 01 5.9E+ 02 6.3E+ 02 26b 100.5 1.67 10.0 0.7 1.4E+ 02 1.4E+ 03 1.5E+ 03 27a 123.8 2.39 26.2 0.8 1.6E+ 02 4.2E+ 03 4.5E+ 03 27b 123.8 0.8 26.2 0.6 1.2E+ 02 3.1E+ 03 3.3E+ 03 28a 140.3 2.39 26.2 0.7 1.4E+ 02 3.7E+ 03 3.9E+ 03 28b 140.3 0.8 26.2 0.8 1.6E+ 02 4.2E+ 03 4.5E+ 03 29a 156.8 5 9.44 0 0.0E+ 00 0.0E+ 00 0.0E+ 00 29b 156.8 1.67 9.44 0.5 9.8E+ 01 9.3E+ 02 9.9E+ 02 No. of Fansc 13 2.87E+ 05 3.06E+ 05 Totals 3567.46 5.5E+ 05 5.9E+ 05 Volume of moist air mix @ inlet ( v 1 = actual ft3/ lb m) 12.855 a fpm = ft/ min; acfm = actual ft3/ min; and wscf/ min = wet standard ft3/ min.

b Points 22 29 from SE corner.

c Assumes fan ratings = 22,100 acfm each.

G 4 E 4 Table E 3. Roof Vent Optical Anemometer Results on 2/ 24/ 00a LOA Time LOA Reading ( actual m/ s) Vol. Air Flow ( acfm) DB Air Temp. ( o C ) DB Air Temp. ( o F) Std. Flowrate ( wscf/ min) Rel. Humidity (%)

5: 30: 10 1.10 6.14E+ 05 23.4 74.1 6.28E+ 05 49.1 5: 31: 10 1.06 5.91E+ 05 23.4 74.1 6.04E+ 05 49.1 5: 32: 10 1.03 5.75E+ 05 23.4 74.1 5.88E+ 05 49.1 5: 34: 10 1.02 5.69E+ 05 23.4 74.1 5.82E+ 05 49.1 5: 35: 10 1.13 6.30E+ 05 23.4 74.1 6.44E+ 05 49.1 5: 36: 10 1.03 5.75E+ 05 23.4 74.1 5.88E+ 05 49.1 5: 37: 10 1.08 6.02E+ 05 23.4 74.1 6.15E+ 05 49.1 5: 38: 15 1.00 5.58E+ 05 23.4 74.1 5.70E+ 05 49.1 5: 39: 10 1.08 6.02E+ 05 23.4 74.1 6.15E+ 05 49.1 5: 40: 10 1.02 5.69E+ 05 23.4 74.1 5.82E+ 05 49.1 5: 41: 10 1.06 5.91E+ 05 23.4 74.1 6.04E+ 05 49.1 5: 42: 10 1.01 5.63E+ 05 23.4 74.1 5.76E+ 05 49.1 5: 43: 10 0.95 5.30E+ 05 23.4 74.1 5.42E+ 05 49.1 5: 44: 10 0.96 5.36E+ 05 23.4 74.1 5.48E+ 05 49.1 5: 45: 10 0.91 5.08E+ 05 23.5 74.3 5.19E+ 05 49.3 5: 46: 10 0.93 5.19E+ 05 23.5 74.3 5.30E+ 05 49.3 5: 47: 10 0.95 5.30E+ 05 23.5 74.3 5.42E+ 05 49.3 5: 48: 10 1.02 5.69E+ 05 23.5 74.3 5.81E+ 05 49.3 5: 49: 10 0.95 5.30E+ 05 23.5 74.3 5.42E+ 05 49.3 5: 51: 15 1.02 5.69E+ 05 23.5 74.3 5.81E+ 05 49.3 5: 52: 10 1.02 5.69E+ 05 23.5 74.3 5.81E+ 05 49.3 5: 53: 10 0.95 5.30E+ 05 23.5 74.3 5.42E+ 05 49.3 5: 54: 10 1.01 5.63E+ 05 23.5 74.3 5.75E+ 05 49.3 5: 55: 10 0.96 5.36E+ 05 23.5 74.3 5.48E+ 05 49.3 5: 56: 10 1.00 5.58E+ 05 23.5 74.3 5.70E+ 05 49.3 5: 57: 10 1.01 5.63E+ 05 23.5 74.3 5.75E+ 05 49.3 5: 58: 10 0.98 5.47E+ 05 23.5 74.3 5.59E+ 05 49.3 5: 59: 10 0.91 5.08E+ 05 23.5 74.3 5.19E+ 05 49.3 6: 00: 10 0.96 5.36E+ 05 23.6 74.5 5.48E+ 05 49.4 6: 01: 10 1.03 5.75E+ 05 23.6 74.5 5.87E+ 05 49.4 6: 02: 15 0.91 5.08E+ 05 23.6 74.5 5.19E+ 05 49.4 6: 03: 10 0.89 4.96E+ 05 23.6 74.5 5.07E+ 05 49.4 6: 04: 10 0.95 5.30E+ 05 23.6 74.5 5.41E+ 05 49.4 6: 05: 10 0.95 5.30E+ 05 23.6 74.5 5.41E+ 05 49.4 6: 06: 10 0.98 5.47E+ 05 23.6 74.5 5.59E+ 05 49.4 6: 07: 10 0.98 5.47E+ 05 23.6 74.5 5.59E+ 05 49.4 6: 08: 10 1.06 5.91E+ 05 23.6 74.5 6.04E+ 05 49.4 E 5 Table E 3. ( Continued)

LOA Time LOA Reading ( actual m/ s) Vol. Air Flow ( acfm) DB Air Temp. ( o C ) DB Air Temp. ( o F) Std. Flowrate ( wscf/ min) Rel. Humidity (%)

6: 09: 10 0.99 5.52E+ 05 23.6 74.5 5.64E+ 05 49.4 6: 10: 10 1.05 5.86E+ 05 23.6 74.5 5.99E+ 05 49.4 6: 11: 10 1.05 5.86E+ 05 23.6 74.5 5.99E+ 05 49.4 6: 12: 10 0.98 5.47E+ 05 23.6 74.5 5.59E+ 05 49.4 6: 13: 10 0.97 5.41E+ 05 23.6 74.5 5.53E+ 05 49.4 6: 15: 10 0.94 5.24E+ 05 23.5 74.3 5.35E+ 05 49.1 6: 16: 10 1.04 5.80E+ 05 23.5 74.3 5.93E+ 05 49.1 6: 17: 10 1.05 5.86E+ 05 23.5 74.3 5.99E+ 05 49.1 6: 18: 10 1.14 6.36E+ 05 23.5 74.3 6.50E+ 05 49.1 6: 19: 10 1.09 6.08E+ 05 23.5 74.3 6.21E+ 05 49.1 6: 20: 10 1.12 6.25E+ 05 23.5 74.3 6.39E+ 05 49.1 6: 21: 10 1.07 5.97E+ 05 23.5 74.3 6.10E+ 05 49.1 6: 22: 10 1.06 5.91E+ 05 23.5 74.3 6.04E+ 05 49.1 6: 23: 10 1.15 6.42E+ 05 23.5 74.3 6.56E+ 05 49.1 6: 24: 10 1.12 6.25E+ 05 23.5 74.3 6.39E+ 05 49.1 6: 26: 10 1.15 6.42E+ 05 23.5 74.3 6.56E+ 05 49.1 6: 27: 10 1.14 6.36E+ 05 23.5 74.3 6.50E+ 05 49.1 6: 28: 10 1.06 5.91E+ 05 23.5 74.3 6.04E+ 05 49.1 6: 29: 10 1.02 5.69E+ 05 23.5 74.3 5.81E+ 05 49.1 6: 30: 10 1.03 5.75E+ 05 23.6 74.5 5.87E+ 05 48.6 6: 31: 10 1.10 6.14E+ 05 23.6 74.5 6.27E+ 05 48.6 6: 32: 10 1.02 5.69E+ 05 23.6 74.5 5.81E+ 05 48.6 6: 33: 10 0.94 5.24E+ 05 23.6 74.5 5.35E+ 05 48.6 6: 34: 10 0.98 5.47E+ 05 23.6 74.5 5.59E+ 05 48.6 6: 35: 10 1.03 5.75E+ 05 23.6 74.5 5.87E+ 05 48.6 6: 36: 10 1.07 5.97E+ 05 23.6 74.5 6.10E+ 05 48.6 6: 37: 10 1.04 5.80E+ 05 23.6 74.5 5.92E+ 05 48.6 6: 38: 10 1.01 5.63E+ 05 23.6 74.5 5.75E+ 05 48.6 6: 39: 10 0.96 5.36E+ 05 23.6 74.5 5.48E+ 05 48.6 6: 43: 10 0.99 5.52E+ 05 23.6 74.5 5.64E+ 05 48.6 6: 44: 10 0.95 5.30E+ 05 23.6 74.5 5.41E+ 05 48.6 6: 45: 10 0.92 5.13E+ 05 23.7 74.7 5.24E+ 05 48.1 6: 46: 10 0.95 5.30E+ 05 23.7 74.7 5.41E+ 05 48.1 6: 47: 10 1.05 5.86E+ 05 23.7 74.7 5.98E+ 05 48.1 6: 49: 10 0.97 5.41E+ 05 23.7 74.7 5.52E+ 05 48.1 6: 50: 10 1.00 5.58E+ 05 23.7 74.7 5.70E+ 05 48.1 6: 51: 10 0.99 5.52E+ 05 23.7 74.7 5.64E+ 05 48.1 E 6 Table E 3. ( Continued)

LOA Time LOA Reading ( actual m/ s) Vol. Air Flow ( acfm) DB Air Temp. ( o C ) DB Air Temp. ( o F) Std. Flowrate ( wscf/ min) Rel. Humidity (%)

6: 52: 10 0.97 5.41E+ 05 23.7 74.7 5.52E+ 05 48.1 6: 53: 10 1.04 5.80E+ 05 23.7 74.7 5.92E+ 05 48.1 6: 54: 10 1.04 5.80E+ 05 23.7 74.7 5.92E+ 05 48.1 6: 55: 10 1.02 5.69E+ 05 23.7 74.7 5.81E+ 05 48.1 6: 56: 10 1.04 5.80E+ 05 23.7 74.7 5.92E+ 05 48.1 6: 57: 10 1.13 6.30E+ 05 23.7 74.7 6.43E+ 05 48.1 6: 58: 10 1.06 5.91E+ 05 23.7 74.7 6.03E+ 05 48.1 6: 59: 10 0.98 5.47E+ 05 23.7 74.7 5.59E+ 05 48.1 7: 00: 10 0.98 5.47E+ 05 23.5 74.3 5.59E+ 05 48.1 7: 01: 10 0.97 5.41E+ 05 23.5 74.3 5.53E+ 05 48.1 7: 02: 10 1.03 5.75E+ 05 23.5 74.3 5.88E+ 05 48.1 7: 03: 10 0.97 5.41E+ 05 23.5 74.3 5.53E+ 05 48.1 7: 05: 10 1.08 6.02E+ 05 23.5 74.3 6.15E+ 05 48.1 7: 06: 10 1.09 6.08E+ 05 23.5 74.3 6.21E+ 05 48.1 7: 07: 10 0.97 5.41E+ 05 23.5 74.3 5.53E+ 05 48.1 7: 08: 10 1.06 5.91E+ 05 23.5 74.3 6.04E+ 05 48.1 7: 09: 10 1.16 6.47E+ 05 23.5 74.3 6.61E+ 05 48.1 7: 10: 10 1.08 6.02E+ 05 23.5 74.3 6.15E+ 05 48.1 Average 1.02 5.68E+ 05 23.5 74.4 5.81E+ 05 48.9 % Volume Balance 81.8 Volume of moist air mix @ outlet ( v 2 = actual ft3/ lb m) 13.43 % Mass Balance 81.6 a fpm = ft/ min; acfm = actual ft3/ min; and wscf/ min = wet standard ft3/ min.

E 7 Table E 4. Roof Vent Optical Anemometer Results on 2/ 25/ 00a LOA Time LOA Reading ( actual m/ s) Vol. Air Flow ( acfm) DB Air Temp. ( o C ) DB Air Temp. ( o F) Std. Flowrate ( wscf/ min) Rel. Humidity (%)

8: 45: 10 1.03 5.7E+ 05 23.8 74.8 5.81E+ 05 49.5 8: 46: 10 0.99 5.5E+ 05 23.8 74.8 5.61E+ 05 49.5 8: 47: 10 0.96 5.4E+ 05 23.8 74.8 5.50E+ 05 49.5 8: 48: 10 1.06 5.9E+ 05 23.8 74.8 6.01E+ 05 49.5 8: 49: 10 1.02 5.7E+ 05 23.8 74.8 5.81E+ 05 49.5 8: 50: 10 1.00 5.6E+ 05 23.8 74.8 5.71E+ 05 49.5 8: 51: 10 0.97 5.4E+ 05 23.8 74.8 5.50E+ 05 49.5 8: 52: 10 1.04 5.8E+ 05 23.8 74.8 5.91E+ 05 49.5 8: 53: 10 0.95 5.3E+ 05 23.8 74.8 5.40E+ 05 49.5 8: 54: 10 1.06 5.9E+ 05 23.8 74.8 6.01E+ 05 49.5 8: 55: 10 1.11 6.2E+ 05 23.8 74.8 6.32E+ 05 49.5 8: 56: 10 1.11 6.2E+ 05 23.8 74.8 6.32E+ 05 49.5 8: 57: 10 1.07 6.0E+ 05 23.8 74.8 6.12E+ 05 49.5 8: 58: 10 1.06 5.9E+ 05 23.8 74.8 6.01E+ 05 49.5 9: 00: 09 1.04 5.8E+ 05 24 75.2 5.91E+ 05 49.7 9: 00: 10 1.04 5.8E+ 05 24 75.2 5.91E+ 05 49.7 Average 1.03 5.7E+ 05 23.8 74.9 5.87E+ 05 49.5 % Volume Balance 99.5 Volume of moist air mix @ outlet ( v 2 = actual ft3/ lb m) 13.47 % Mass Balance 98.9 a fpm = ft/ min; acfm = actual ft3/ min; and wscf/ min = wet standard ft3/ min.

E 8


[Federal Register Volume 84, Number 109 (Thursday, June 6, 2019)]
[Notices]
[Page 26453]
[FR Doc No: 2019-11835]

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SECURITIES AND EXCHANGE COMMISSION

[Release No. 34-85994; File No. 013-00129]

Initial Form ATS-N Filing; Notice of Extension of Commission
Review Period

May 31, 2019.
    On February 8, 2019, CitiBLOC filed an initial Form ATS-N (``Form
ATS-N'') with the Securities and Exchange Commission (``Commission'').
Pursuant to Rule 304 under the Securities and Exchange Act of 1934
(``Act''), the Commission may, after notice and an opportunity for
hearing, declare an initial Form ATS-N ineffective no later than 120
days from the date of filing with the Commission, or, if applicable,
the extended review period. June 8, 2019 is 120 calendar days from the
date of filing. Pursuant to Rule 304(a)(1)(iv)(B), the Commission may
extend the initial Form ATS-N review period for up to an additional 120
calendar days if the initial Form ATS-N is unusually lengthy or raises
novel or complex issues that require additional time for review.
    CitiBLOC was operating pursuant to an initial operation report on
Form ATS on file with the Commission as of January 7, 2019.\1\ CitiBLOC
filed an initial Form ATS-N on February 8, 2019. During the initial 120
calendar day review period, the Commission staff has been reviewing the
disclosures on CitiBLOC's initial Form ATS-N. In addition, the staff
has been engaged in ongoing discussions with CitiBLOC about its
disclosures and manner of operations, as well as the requirements of
Form ATS-N, to facilitate complete and comprehensible disclosures that
reflect the complexities of those operations.
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    \1\ An NMS Stock ATS (as defined in Rule 300(k) of Regulation
ATS) that was operating pursuant to an initial operation report on
Form ATS on file with the Commission as of January 7, 2019 is a
``Legacy NMS Stock ATS.'' 17 CFR 242.301(b)(2)(viii).
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    Form ATS-N requires NMS Stock ATSs to file with the Commission, and
disclose to the public for the first time, certain information,
including descriptions by the NMS Stock ATSs of their fees, the trading
activities by their broker-dealer operators and their affiliates in the
NMS Stock ATSs, their use of market data, their written standards for
granting access to trading on the NMS Stock ATSs, and their written
safeguards and procedures for protecting their subscribers'
confidential trading information required by revised Rule 301(b)(10) of
Regulation ATS. The initial Form ATS-N disclosures and discussions with
Commission staff have revealed complexities about the operations of
Legacy NMS Stock ATSs including, among other things, matching
functionalities, means of order entry, order interaction and execution
procedures, conditional order processes, segmentation of orders, and
counterparty selection protocols. The Commission staff needs additional
time to review novel and complex issues such as these, which Commission
staff has discussed with CitiBLOC. Extending the initial Form ATS-N
Commission review period for an additional 120 calendar days will
provide Commission staff an opportunity to continue its review of the
initial Form ATS-N disclosures and discussions with CitiBLOC.
    In the conversations between CitiBLOC and Commission staff about
the initial Form ATS-N disclosures and the ATS operations, Commission
staff and CitiBLOC have discussed a potential amendment to update
CitiBLOC's disclosures regarding the complexities of its operations.
Extending the review period will enable the NMS Stock ATS to amend its
disclosures, if appropriate, and allow Commission staff to conduct a
thorough review of amendments to the initial disclosures provided on
the initial Form ATS-N.
    For the reasons given above, the Commission is extending the review
period of the initial Form ATS-N submitted by CitiBLOC. Accordingly,
pursuant to Rule 304(a)(1)(iv)(B), October 6, 2019 is the date by which
the Commission may declare the initial Form ATS-N submitted by CitiBLOC
ineffective.

    By the Commission.
Jill M. Peterson,
Assistant Secretary.
[FR Doc. 2019-11835 Filed 6-5-19; 8:45 am]
 BILLING CODE 8011-01-P