steam output or
                                                                           8.6E-04 lb per
                                                                           MWh).
17. Units designed to burn        a. CO.............  130 ppm by volume   0.13 lb per MMBtu   1 hr minimum
 liquid fuel that are non-                             on a dry basis      of steam output     sampling time.
 continental units.                                    corrected to 3-     or 1.4 lb per
                                                       percent oxygen,     MWh; three-run
                                                       three-run average   average.
                                                       based on stack
                                                       test.
                                  b. Filterable PM    2.2E-01 lb per      2.7E-01 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 2 dscm per
                                                       input; or (8.6E-    output or 3.1 lb    run.
                                                       04 lb per MMBtu     per MWh; or (1.1E-
                                                       of heat input).     03 lb per MMBtu
                                                                           of steam output
                                                                           or 1.2E-02 lb per
                                                                           MWh).
18. Units designed to burn gas 2  a. CO.............  130 ppm by volume   0.16 lb per MMBtu   1 hr minimum
 (other) gases.                                        on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.0 lb per MWh.
                                                       percent oxygen.
                                  b. HCl............  1.7E-03 lb per      2.9E-03 lb per      For M26A, collect
                                                       MMBtu of heat       MMBtu of steam      a minimum of 2
                                                       input.              output or 1.8E-02   dscm per run; for
                                                                           lb per MWh.         M26, collect a
                                                                                minimum of 240
                                                                                liters per run.
                                  c. Mercury........  7.9E-06 lb per      1.4E-05 lb per      For M29, collect a
                                                       MMBtu of heat       MMBtu of steam      minimum of 3 dscm
                                                       input.              output or 8.3E-05   per run; for M30A
                                                                           lb per MWh.         or M30B, collect
                                                                                a minimum sample
                                                                                as specified in
                                                                                the method; for
                                                                                ASTM D6784 \b\
                                                                                collect a minimum
                                                                                of 2 dscm.
                                  d. Filterable PM    7.3E-03 lb per      1.3E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 3 dscm per
                                                       input or (2.1E-04   output or 7.6E-02   run.
                                                       lb per MMBtu of     lb per MWh; or
                                                       heat input).        (3.5E-04 lb per
                                                                           MMBtu of steam
                                                                           output or 2.2E-03
                                                                           lb per MWh).
----------------------------------------------------------------------------------------------------------------
\a\ If you are conducting stack tests to demonstrate compliance and your performance tests for this pollutant
  for at least 2 consecutive years show that your emissions are at or below this limit, you can skip testing
  according to Sec.   63.7515 if all of the other provisions of Sec.   63.7515 are met. For all other pollutants
  that do not contain a footnote a, your performance tests for this pollutant for at least 2 consecutive years
  must show that your emissions are at or below 75 percent of this limit in order to qualify for skip testing.
\b\ Incorporated by reference, see Sec.   63.14.
\c\ An owner or operator may request an alternative test method under Sec.   63.7 of this chapter, in order that
  compliance with the carbon monoxide emissions limit be determined using CO2 as a diluent correction in place
  of oxygen at 3 percent. EPA Method 19 F-factors and EPA Method 19 equations must be used to generate the
  appropriate CO2 correction percentage for the fuel type burned in the unit and must also take into account
  that the 3-percent oxygen correction is to be done on a dry basis. The alternative test method request must
  account for any CO2 being added to, or removed from, the emissions gas stream as a result of limestone
  injection, scrubber media, etc.
\d\ Before [date 3 years after date of publication of final rule in the Federal Register] you may comply with
  the emission limits in Table 15 to this subpart. On and after [date 3 years after date of publication of final
  rule in the Federal Register], you must comply with the emission limits in Table 2 to this subpart.

0
18. Table 3 of subpart DDDDD is amended by revising the entry for
``5.'' and ``6.'' to read as follows:

      Table 3 to Subpart DDDDD of Part 63--Work Practice Standards
     As stated in Sec.   63.7500, you must comply with the following
                   applicable work practice standards:
------------------------------------------------------------------------
    If your unit is . . .          You must meet the following . . .
------------------------------------------------------------------------

                              * * * * * * *
5. An existing or new boiler   a. You must operate all CMS during
 or process heater subject to   startup.
 emission limits in Table 1    b. For startup of a boiler or process
 or 2 or 11 through 13 to       heater, you must use one or a
 this subpart during startup.   combination of the following clean
                                fuels: Natural gas, synthetic natural
                                gas, propane, other Gas 1 fuels,
                                distillate oil, syngas, ultra-low sulfur
                                diesel, fuel oil-soaked rags, kerosene,
                                hydrogen, paper, cardboard, refinery
                                gas, liquefied petroleum gas, clean dry
                                biomass, and any fuels meeting the
                                appropriate HCl, mercury and TSM
                                emission standards by fuel analysis.
                               c. You have the option of complying using
                                either of the following work practice
                                standards.

                               (1) If you choose to comply using
                                definition (1) of ``startup'' in Sec.
                                63.7575, once you start firing fuels
                                that are not clean fuels you must vent
                                emissions to the main stack(s) and
                                engage all of the applicable control
                                devices except limestone injection in
                                fluidized bed combustion (FBC) boilers,
                                dry scrubber, fabric filter, and
                                selective catalytic reduction (SCR). You
                                must start your limestone injection in
                                FBC boilers, dry scrubber, fabric
                                filter, and SCR systems as expeditiously
                                as possible. Startup ends when steam or
                                heat is supplied for any purpose, OR
                               (2) If you choose to comply using
                                definition (2) of ``startup'' in Sec.
                                63.7575, once you start to feed fuels
                                that are not clean fuels, you must vent
                                emissions to the main stack(s) and
                                engage all of the applicable control
                                devices so as to comply with the
                                emission limits within 4 hours of start
                                of supplying useful thermal energy. You
                                must engage and operate PM control
                                within one hour of first feeding fuels
                                that are not clean fuels\a\. You must
                                start all applicable control devices as
                                expeditiously as possible, but, in any
                                case, when necessary to comply with
                                other standards applicable to the source
                                by a permit limit or a rule other than
                                this subpart that require operation of
                                the control devices. You must develop
                                and implement a written startup and
                                shutdown plan, as specified in Sec.
                                63.7505(e).
                               d. You must comply with all applicable
                                emission limits at all times except
                                during startup and shutdown periods at
                                which time you must meet this work
                                practice. You must collect monitoring
                                data during periods of startup, as
                                specified in Sec.   63.7535(b). You must
                                keep records during periods of startup.
                                You must provide reports concerning
                                activities and periods of startup, as
                                specified in Sec.   63.7555.
6. An existing or new boiler   You must operate all CMS during shutdown.
 or process heater subject to   While firing fuels that are not clean
 emission limits in Tables 1    fuels during shutdown, you must vent
 or 2 or 11 through 15 to       emissions to the main stack(s) and
 this subpart during shutdown.  operate all applicable control devices,
                                except limestone injection in FBC
                                boilers, dry scrubber, fabric filter,
                                and SCR but, in any case, when necessary
                                to comply with other standards
                                applicable to the source that require
                                operation of the control device.
                               If, in addition to the fuel used prior to
                                initiation of shutdown, another fuel
                                must be used to support the shutdown
                                process, that additional fuel must be
                                one or a combination of the following
                                clean fuels: Natural gas, synthetic
                                natural gas, propane, other Gas 1 fuels,
                                distillate oil, syngas, ultra-low sulfur
                                diesel, refinery gas, and liquefied
                                petroleum gas.
                               You must comply with all applicable
                                emissions limits at all times except for
                                startup or shutdown periods conforming
                                with this work practice. You must
                                collect monitoring data during periods
                                of shutdown, as specified in Sec.
                                63.7535(b). You must keep records during
                                periods of shutdown. You must provide
                                reports concerning activities and
                                periods of shutdown, as specified in
                                Sec.   63.7555.
------------------------------------------------------------------------

* * * * *
0
19. Table 4 to subpart DDDDD is amended by revising the column headings
to read as follows:

  Table 4 to Subpart DDDDD of Part 63--Operating Limits for Boilers and
                             Process Heaters
    As stated in Sec.   63.7500, you must comply with the applicable
                            operating limits:
------------------------------------------------------------------------
 When complying with a Table 1, 2, 11, 12,
  13, 14, or 15 numerical emission limit         You must meet these
                using . . .                    operating limits . . .
------------------------------------------------------------------------

                              * * * * * * *
------------------------------------------------------------------------

* * * * *
0
20. Table 7 to subpart DDDDD is amended by revising footnote ``b'' to
read as follows:

 Table 7 to Subpart DDDDD of Part 63--Establishing Operating Limits a b
     As stated in Sec.   63.7520, you must comply with the following
             requirements for establishing operating limits:
------------------------------------------------------------------------

--------------------------------------------

                               * * * * *
------------------------------------------------------------------------
\b\ If you conduct multiple performance tests, you must set the minimum
  liquid flow rate and pressure drop operating limits at the higher of
  the minimum values established during the performance tests. For a
  minimum oxygen level, if you conduct multiple performance tests, you
  must set the minimum oxygen level at the lower of the minimum values
  established during the performance tests. For maximum operating load,
  if you conduct multiple performance tests, you must set the maximum
  operating load at the lower of the maximum values established during
  the performance tests.

0
21. Table 8 to subpart DDDDD is amended by revising the entry for
``8.'' to read as follows:

Table 8 to Subpart DDDDD of Part 63--Demonstrating Continuous Compliance
  As stated in Sec.   63.7540, you must show continuous compliance with
 the emission limitations for each boiler or process heater according to
                             the following:
------------------------------------------------------------------------
     If you must meet the
following operating limits or       You must demonstrate continuous
work practice standards . . .             compliance by . . .
------------------------------------------------------------------------

                              * * * * * * *
8. Emission limits using fuel  a. Conduct monthly fuel analysis for HCl
 analysis.                      or mercury or TSM according to Table 6
                                to this subpart; and
                               b. Reduce the data to 12-month rolling
                                averages; and
                               c. Maintain the 12-month rolling average
                                at or below the applicable emission
                                limit for HCl or mercury or TSM in
                                Tables 1 and 2 or 11 through 15 to this
                                subpart.
                               d. Calculate the HCI, mercury, and/or TSM
                                emission rate from the boiler or process
                                heater in units of lb/MMBtu using
                                Equations 7, 8, and/or 9 in Sec.
                                63.7530.

                              * * * * * * *
------------------------------------------------------------------------

* * * * *
0
22. Add Table 14 to subpart DDDDD of part 63 to read as follows:

 Table 14 to Subpart DDDDD of Part 63--Alternative Emission Limits for New or Reconstructed Boilers and Process
                                                     Heaters
   As stated in Sec.   63.7500, you may continue to comply with the following applicable emission limits until
 [date 3 years after date of publication of final rule in the Federal Register]: [Units with heat input capacity
                                     of 10 million Btu per hour or greater]
----------------------------------------------------------------------------------------------------------------
                                                                           Or the emissions
                                                      The emissions must    must not exceed
                                                        not exceed the       the following        Using this
If your boiler or process heater   For the following  following emission  alternative output- specified sampling
  is in this subcategory . . .     pollutants . . .     limits, except       based limits,    volume or test run
                                                      during startup and     except during      duration . . .
                                                        shutdown . . .        startup and
                                                                            shutdown . . .
----------------------------------------------------------------------------------------------------------------
1. Units in all subcategories     a. HCl............  2.2E-02 lb per      2.5E-02 lb per      For M26A, collect
 designed to burn solid fuel.                          MMBtu of heat       MMBtu of steam      a minimum of 1
                                                       input.              output or 0.28 lb   dscm per run; for
                                                                           per MWh.            M26 collect a
                                                                                minimum of 120
                                                                                liters per run.
                                  b. Mercury........  8.0E-07 \a\ lb per  8.7E-07 \a\ lb per  For M29, collect a
                                                       MMBtu of heat       MMBtu of steam      minimum of 4 dscm
                                                       input.              output or 1.1E-05   per run; for M30A
                                                                           \a\ lb per MWh.     or M30B, collect
                                                                                a minimum sample
                                                                                as specified in
                                                                                the method; for
                                                                                ASTM D6784 \b\
                                                                                collect a minimum
                                                                                of 4 dscm.
2. Units designed to burn coal/   a. Filterable PM    1.1E-03 lb per      1.1E-03 lb per      Collect a minimum
 solid fossil fuel.                (or TSM).           MMBtu of heat       MMBtu of steam      of 3 dscm per
                                                       input; or (2.3E-    output or 1.4E-02   run.
                                                       05 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (2.7E-05 lb per
                                                                           MMBtu of steam
                                                                           output or 2.9E-04
                                                                           lb per MWh).
3. Pulverized coal boilers        a. Carbon monoxide  130 ppm by volume   0.11 lb per MMBtu   1 hr minimum
 designed to burn coal/solid       (CO) (or CEMS).     on a dry basis      of steam output     sampling time.
 fossil fuel.                                          corrected to 3-     or 1.4 lb per
                                                       percent oxygen,     MWh; three-run
                                                       three-run           average.
                                                       average; or (320
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\d\ 30-day
                                                       rolling average).
4. Stokers/others designed to     a. CO (or CEMS)...  130 ppm by volume   0.12 lb per MMBtu   1 hr minimum
 burn coal/solid fossil fuel.                          on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.4 lb per
                                                       percent oxygen,     MWh; three-run
                                                       three-run           average.
                                                       average; or (340
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\d\ 30-day
                                                       rolling average).
5. Fluidized bed units designed   a. CO (or CEMS)...  130 ppm by volume   0.11 lb per MMBtu   1 hr minimum
 to burn coal/solid fossil fuel.                       on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.4 lb per
                                                       percent oxygen,     MWh; three-run
                                                       three-run           average.
                                                       average; or (230
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\d\ 30-day
                                                       rolling average).
6. Fluidized bed units with an    a. CO (or CEMS)...  140 ppm by volume   1.2E-01 lb per      1 hr minimum
 integrated heat exchanger                             on a dry basis      MMBtu of steam      sampling time.
 designed to burn coal/solid                           corrected to 3-     output or 1.5 lb
 fossil fuel.                                          percent oxygen,     per MWh; three-
                                                       three-run           run average.
                                                       average; or (150
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\d\ 30-day
                                                       rolling average).
7. Stokers/sloped grate/others    a. CO (or CEMS)...  620 ppm by volume   5.8E-01 lb per      1 hr minimum
 designed to burn wet biomass                          on a dry basis      MMBtu of steam      sampling time.
 fuel.                                                 corrected to 3-     output or 6.8 lb
                                                       percent oxygen,     per MWh; three-
                                                       three-run           run average.
                                                       average; or (390
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\d\ 30-day
                                                       rolling average).
                                  b. Filterable PM    3.0E-02 lb per      3.5E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 2 dscm per
                                                       input; or (2.6E-    output or 4.2E-01   run.
                                                       05 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (2.7E-05 lb per
                                                                           MMBtu of steam
                                                                           output or 3.7E-04
                                                                           lb per MWh).

8. Stokers/sloped grate/others    a. CO.............  460 ppm by volume   4.2E-01 lb per      1 hr minimum
 designed to burn kiln-dried                           on a dry basis      MMBtu of steam      sampling time.
 biomass fuel.                                         corrected to 3-     output or 5.1 lb
                                                       percent oxygen.     per MWh.
                                  b. Filterable PM    3.0E-02 lb per      3.5E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 2 dscm per
                                                       input; or (4.0E-    output or 4.2E-01   run.
                                                       03 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (4.2E-03 lb per
                                                                           MMBtu of steam
                                                                           output or 5.6E-02
                                                                           lb per MWh).
9. Fluidized bed units designed   a. CO (or CEMS)...  230 ppm by volume   2.2E-01 lb per      1 hr minimum
 to burn biomass/bio-based                             on a dry basis      MMBtu of steam      sampling time.
 solids.                                               corrected to 3-     output or 2.6 lb
                                                       percent oxygen,     per MWh; three-
                                                       three-run           run average.
                                                       average; or (310
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\d\ 30-day
                                                       rolling average).
                                  b. Filterable PM    9.8E-03 lb per      1.2E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 3 dscm per
                                                       input; or (8.3E-    output or 0.14 lb   run.
                                                       05 \a\ lb per       per MWh; or (1.1E-
                                                       MMBtu of heat       04 \a\ lb per
                                                       input).             MMBtu of steam
                                                                           output or 1.2E-03
                                                                           \a\ lb per MWh).
10. Suspension burners designed   a. CO (or CEMS)...  2,400 ppm by        1.9 lb per MMBtu    1 hr minimum
 to burn biomass/bio-based                             volume on a dry     of steam output     sampling time.
 solids.                                               basis corrected     or 27 lb per MWh;
                                                       to 3-percent        three-run average.
                                                       oxygen, three-run
                                                       average; or
                                                       (2,000 ppm by
                                                       volume on a dry
                                                       basis corrected
                                                       to 3-percent
                                                       oxygen,\d\ 10-day
                                                       rolling average).
                                  b. Filterable PM    3.0E-02 lb per      3.1E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 2 dscm per
                                                       input; or (6.5E-    output or 4.2E-01   run.
                                                       03 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (6.6E-03 lb per
                                                                           MMBtu of steam
                                                                           output or 9.1E-02
                                                                           lb per MWh).
11. Dutch Ovens/Pile burners      a. CO (or CEMS)...  330 ppm by volume   3.5E-01 lb per      1 hr minimum
 designed to burn biomass/bio-                         on a dry basis      MMBtu of steam      sampling time.
 based solids.                                         corrected to 3-     output or 3.6 lb
                                                       percent oxygen,     per MWh; three-
                                                       three-run           run average.
                                                       average; or (520
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\d\ 10-day
                                                       rolling average).
                                  b. Filterable PM    3.2E-03 lb per      4.3E-03 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 3 dscm per
                                                       input; or (3.9E-    output or 4.5E-02   run.
                                                       05 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (5.2E-05 lb per
                                                                           MMBtu of steam
                                                                           output or 5.5E-04
                                                                           lb per MWh).
12. Fuel cell units designed to   a. CO.............  910 ppm by volume   1.1 lb per MMBtu    1 hr minimum
 burn biomass/bio-based solids.                        on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.0E+01 lb per
                                                       percent oxygen.     MWh.
                                  b. Filterable PM    2.0E-02 lb per      3.0E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 2 dscm per
                                                       input; or (2.9E-    output or 2.8E-01   run.
                                                       05 \a\ lb per       lb per MWh; or
                                                       MMBtu of heat       (5.1E-05 lb per
                                                       input).             MMBtu of steam
                                                                           output or 4.1E-04
                                                                           lb per MWh).
13. Hybrid suspension grate       a. CO (or CEMS)...  1,100 ppm by        1.4 lb per MMBtu    1 hr minimum
 boiler designed to burn biomass/                      volume on a dry     of steam output     sampling time.
 bio-based solids.                                     basis corrected     or 12 lb per MWh;
                                                       to 3-percent        three-run average.
                                                       oxygen, three-run
                                                       average; or (900
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\d\ 30-day
                                                       rolling average).
                                  b. Filterable PM    2.6E-02 lb per      3.3E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 3 dscm per
                                                       input; or (4.4E-    output or 3.7E-01   run.
                                                       04 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (5.5E-04 lb per
                                                                           MMBtu of steam
                                                                           output or 6.2E-03
                                                                           lb per MWh).
14. Units designed to burn        a. HCl............  4.4E-04 lb per      4.8E-04 lb per      For M26A: Collect
 liquid fuel.                                          MMBtu of heat       MMBtu of steam      a minimum of 2
                                                       input.              output or 6.1E-03   dscm per run; for
                                                                           lb per MWh.         M26, collect a
                                                                                minimum of 240
                                                                                liters per run.
                                  b. Mercury........  4.8E-07 \a\ lb per  5.3E-07 \a\ lb per  For M29, collect a
                                                       MMBtu of heat       MMBtu of steam      minimum of 4 dscm
                                                       input.              output or 6.7E-06   per run; for M30A
                                                                           \a\ lb per MWh.     or M30B, collect
                                                                                a minimum sample
                                                                                as specified in
                                                                                the method; for
                                                                                ASTM D6784 \b\
                                                                                collect a minimum
                                                                                of 4 dscm.
15. Units designed to burn heavy  a. CO.............  130 ppm by volume   0.13 lb per MMBtu   1 hr minimum
 liquid fuel.                                          on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.4 lb per
                                                       percent oxygen,     MWh; three-run
                                                       three-run average.  average.
                                  b. Filterable PM    1.3E-02 lb per      1.5E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 3 dscm per
                                                       input; or (7.5E-    output or 1.8E-01   run.
                                                       05 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (8.2E-05 lb per
                                                                           MMBtu of steam
                                                                           output or 1.1E-03
                                                                           lb per MWh).
16. Units designed to burn light  a. CO.............  130 ppm by volume   0.13 lb per MMBtu   1 hr minimum
 liquid fuel.                                          on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.4 lb per MWh.
                                                       percent oxygen.

                                  b. Filterable PM    1.1E-03 \a\ lb per  1.2E-03 \a\ lb per  Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 3 dscm per
                                                       input; or (2.9E-    output or 1.6E-02   run.
                                                       05 lb per MMBtu     \a\ lb per MWh;
                                                       of heat input).     or (3.2E-05 lb
                                                                           per MMBtu of
                                                                           steam output or
                                                                           4.0E-04 lb per
                                                                           MWh).
17. Units designed to burn        a. CO.............  130 ppm by volume   0.13 lb per MMBtu   1 hr minimum
 liquid fuel that are non-                             on a dry basis      of steam output     sampling time.
 continental units.                                    corrected to 3-     or 1.4 lb per
                                                       percent oxygen,     MWh; three-run
                                                       three-run average   average.
                                                       based on stack
                                                       test.
                                  b. Filterable PM    2.3E-02 lb per      2.5E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 4 dscm per
                                                       input; or (8.6E-    output or 3.2E-01   run.
                                                       04 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (9.4E-04 lb per
                                                                           MMBtu of steam
                                                                           output or 1.2E-02
                                                                           lb per MWh).
18. Units designed to burn gas 2  a. CO.............  130 ppm by volume   0.16 lb per MMBtu   1 hr minimum
 (other) gases.                                        on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.0 lb per MWh.
                                                       percent oxygen.
                                  b. HCl............  1.7E-03 lb per      2.9E-03 lb per      For M26A, Collect
                                                       MMBtu of heat       MMBtu of steam      a minimum of 2
                                                       input.              output or 1.8E-02   dscm per run; for
                                                                           lb per MWh.         M26, collect a
                                                                                minimum of 240
                                                                                liters per run.
                                  c. Mercury........  7.9E-06 lb per      1.4E-05 lb per      For M29, collect a
                                                       MMBtu of heat       MMBtu of steam      minimum of 3 dscm
                                                       input.              output or 8.3E-05   per run; for M30A
                                                                           lb per MWh.         or M30B, collect
                                                                                a minimum sample
                                                                                as specified in
                                                                                the method; for
                                                                                ASTM D6784 \b\
                                                                                collect a minimum
                                                                                of 3 dscm.
                                  d. Filterable PM    6.7E-03 lb per      1.2E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 3 dscm per
                                                       input; or (2.1E-    output or 7.0E-02   run.
                                                       04 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (3.5E-04 lb per
                                                                           MMBtu of steam
                                                                           output or 2.2E-03
                                                                           lb per MWh).
----------------------------------------------------------------------------------------------------------------

0
23. Add Table 15 to subpart DDDDD of part 63 to read as follows:

   Table 15 to Subpart DDDDD of Part 63--Alternative Emission Limits for Existing Boilers and Process Heaters
As stated in Sec.   63.7500, you may continue to comply with following emission limits until [date 3 years after
  date of publication of final rule in the Federal Register]: [Units with heat input capacity of 10 million Btu
                                              per hour or greater]
----------------------------------------------------------------------------------------------------------------
                                                                          The emissions must
                                                      The emissions must    not exceed the
                                                        not exceed the         following          Using this
If your boiler or process heater   For the following  following emission  alternative output- specified sampling
  is in this  subcategory . . .    pollutants . . .     limits, except       based limits,       volume or test
                                                      during startup and     except during    run duration . . .
                                                        shutdown . . .        startup and
                                                                            shutdown . . .
----------------------------------------------------------------------------------------------------------------
1. Units in all subcategories     a. HCl............  2.2E-02 lb per      2.5E-02 lb per      For M26A, Collect
 designed to burn solid fuel.                          MMBtu of heat       MMBtu of steam      a minimum of 1
                                                       input.              output or 0.27 lb   dscm per run; for
                                                                           per MWh.            M26, collect a
                                                                                minimum of 120
                                                                                liters per run.
                                  b. Mercury........  5.7E-06 lb per      6.4E-06 lb per      For M29, collect a
                                                       MMBtu of heat       MMBtu of steam      minimum of 3 dscm
                                                       input.              output or 7.3E-05   per run; for M30A
                                                                           lb per MWh.         or M30B, collect
                                                                                a minimum sample
                                                                                as specified in
                                                                                the method; for
                                                                                ASTM D6784 \b\
                                                                                collect a minimum
                                                                                of 3 dscm.
2. Units design to burn coal/     a. Filterable PM    4.0E-02 lb per      4.2E-02 lb per      Collect a minimum
 solid fossil fuel.                (or TSM).           MMBtu of heat       MMBtu of steam      of 2 dscm per
                                                       input; or (5.3E-    output or 4.9E-01   run.
                                                       05 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (5.6E-05 lb per
                                                                           MMBtu of steam
                                                                           output or 6.5E-04
                                                                           lb per MWh).
3. Pulverized coal boilers        a. CO (or CEMS)...  130 ppm by volume   0.11 lb per MMBtu   1 hr minimum
 designed to burn coal/solid                           on a dry basis      of steam output     sampling time.
 fossil fuel.                                          corrected to 3-     or 1.4 lb per
                                                       percent oxygen,     MWh; three-run
                                                       three-run           average.
                                                       average; or (320
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\c\ 30-day
                                                       rolling average).
4. Stokers/others designed to     a. CO (or CEMS)...  160 ppm by volume   0.14 lb per MMBtu   1 hr minimum
 burn coal/solid fossil fuel.                          on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.7 lb per
                                                       percent oxygen,     MWh; three-run
                                                       three-run           average.
                                                       average; or (340
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\c\ 30-day
                                                       rolling average).

5. Fluidized bed units designed   a. CO (or CEMS)...  130 ppm by volume   0.12 lb per MMBtu   1 hr minimum
 to burn coal/solid fossil fuel.                       on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.4 lb per
                                                       percent oxygen,     MWh; three-run
                                                       three-run           average.
                                                       average; or (230
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\c\ 30-day
                                                       rolling average).
6. Fluidized bed units with an    a. CO (or CEMS)...  140 ppm by volume   1.3E-01 lb per      1 hr minimum
 integrated heat exchanger                             on a dry basis      MMBtu of steam      sampling time.
 designed to burn coal/solid                           corrected to 3-     output or 1.5 lb
 fossil fuel.                                          percent oxygen,     per MWh; three-
                                                       three-run           run average.
                                                       average; or (150
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\c\ 30-day
                                                       rolling average).
7. Stokers/sloped grate/others    a. CO (or CEMS)...  1,500 ppm by        1.4 lb per MMBtu    1 hr minimum
 designed to burn wet biomass                          volume on a dry     of steam output     sampling time.
 fuel.                                                 basis corrected     or 17 lb per MWh;
                                                       to 3-percent        three-run average.
                                                       oxygen, three-run
                                                       average; or (720
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\c\ 30-day
                                                       rolling average).
                                  b. Filterable PM    3.7E-02 lb per      4.3E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 2 dscm per
                                                       input; or (2.4E-    output or 5.2E-01   run.
                                                       04 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (2.8E-04 lb per
                                                                           MMBtu of steam
                                                                           output or 3.4E-04
                                                                           lb per MWh).
8. Stokers/sloped grate/others    a. CO.............  460 ppm by volume   4.2E-01 lb per      1 hr minimum
 designed to burn kiln-dried                           on a dry basis      MMBtu of steam      sampling time.
 biomass fuel.                                         corrected to 3-     output or 5.1 lb
                                                       percent oxygen.     per MWh.
                                  b. Filterable PM    3.2E-01 lb per      3.7E-01 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 1 dscm per
                                                       input; or (4.0E-    output or 4.5 lb    run.
                                                       03 lb per MMBtu     per MWh; or (4.6E-
                                                       of heat input).     03 lb per MMBtu
                                                                           of steam output
                                                                           or 5.6E-02 lb per
                                                                           MWh).
9. Fluidized bed units designed   a. CO (or CEMS)...  470 ppm by volume   4.6E-01 lb per      1 hr minimum
 to burn biomass/bio-based solid.                      on a dry basis      MMBtu of steam      sampling time.
                                                       corrected to 3-     output or 5.2 lb
                                                       percent oxygen,     per MWh; three-
                                                       three-run           run average.
                                                       average; or (310
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\c\ 30-day
                                                       rolling average).
                                  b. Filterable PM    1.1E-01 lb per      1.4E-01 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 1 dscm per
                                                       input; or (1.2E-    output or 1.6 lb    run.
                                                       03 lb per MMBtu     per MWh; or (1.5E-
                                                       of heat input).     03 lb per MMBtu
                                                                           of steam output
                                                                           or 1.7E-02 lb per
                                                                           MWh).
10. Suspension burners designed   a. CO (or CEMS)...  2,400 ppm by        1.9 lb per MMBtu    1 hr minimum
 to burn biomass/bio-based solid.                      volume on a dry     of steam output     sampling time.
                                                       basis corrected     or 27 lb per MWh;
                                                       to 3-percent        three-run average.
                                                       oxygen, three-run
                                                       average; or
                                                       (2,000 ppm by
                                                       volume on a dry
                                                       basis corrected
                                                       to 3-percent
                                                       oxygen,\c\ 10-day
                                                       rolling average).
                                  b. Filterable PM    5.1E-02 lb per      5.2E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 2 dscm per
                                                       input; or (6.5E-    output or 7.1E-01   run.
                                                       03 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (6.6E-03 lb per
                                                                           MMBtu of steam
                                                                           output or 9.1E-02
                                                                           lb per MWh).
11. Dutch Ovens/Pile burners      a. CO (or CEMS)...  770 ppm by volume   8.4E-01 lb per      1 hr minimum
 designed to burn biomass/bio-                         on a dry basis      MMBtu of steam      sampling time.
 based solid.                                          corrected to 3-     output or 8.4 lb
                                                       percent oxygen,     per MWh; three-
                                                       three-run           run average.
                                                       average; or (520
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\c\ 10-day
                                                       rolling average).
                                  b. Filterable PM    2.8E-01 lb per      3.9E-01 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 1 dscm per
                                                       input; or (2.0E-    output or 3.9 lb    run.
                                                       03 lb per MMBtu     per MWh; or (2.8E-
                                                       of heat input).     03 lb per MMBtu
                                                                           of steam output
                                                                           or 2.8E-02 lb per
                                                                           MWh).
12. Fuel cell units designed to   a. CO.............  1,100 ppm by        2.4 lb per MMBtu    1 hr minimum
 burn biomass/bio-based solid.                         volume on a dry     of steam output     sampling time.
                                                       basis corrected     or 12 lb per MWh.
                                                       to 3-percent
                                                       oxygen.
                                  b. Filterable PM    2.0E-02 lb per      5.5E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 2 dscm per
                                                       input; or (5.8E-    output or 2.8E-01   run.
                                                       03 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (1.6E-02 lb per
                                                                           MMBtu of steam
                                                                           output or 8.1E-02
                                                                           lb per MWh).
13. Hybrid suspension grate       a. CO (or CEMS)...  3,500 ppm by        3.5 lb per MMBtu    1 hr minimum
 units designed to burn biomass/                       volume on a dry     of steam output     sampling time.
 bio-based solid.                                      basis corrected     or 39 lb per MWh;
                                                       to 3-percent        three-run average.
                                                       oxygen, three-run
                                                       average; or (900
                                                       ppm by volume on
                                                       a dry basis
                                                       corrected to 3-
                                                       percent
                                                       oxygen,\c\ 30-day
                                                       rolling average).

                                  b. Filterable PM    4.4E-01 lb per      5.5E-01 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 1 dscm per
                                                       input; or (4.5E-    output or 6.2 lb    run.
                                                       04 lb per MMBtu     per MWh; or (5.7E-
                                                       of heat input).     04 lb per MMBtu
                                                                           of steam output
                                                                           or 6.3E-03 lb per
                                                                           MWh).
14. Units designed to burn        a. HCl............  1.1E-03 lb per      1.4E-03 lb per      For M26A, collect
 liquid fuel.                                          MMBtu of heat       MMBtu of steam      a minimum of 2
                                                       input.              output or 1.6E-02   dscm per run; for
                                                                           lb per MWh.         M26, collect a
                                                                                minimum of 240
                                                                                liters per run.
                                  b. Mercury........  2.0E-06 \a\ lb per  2.5E-06 \a\ lb per  For M29, collect a
                                                       MMBtu of heat       MMBtu of steam      minimum of 3 dscm
                                                       input.              output or 2.8E-05   per run; for M30A
                                                                           lb per MWh.         or M30B collect a
                                                                                minimum sample as
                                                                                specified in the
                                                                                method, for ASTM
                                                                                D6784 \b\ collect
                                                                                a minimum of 2
                                                                                dscm.
15. Units designed to burn heavy  a. CO.............  130 ppm by volume   0.13 lb per MMBtu   1 hr minimum
 liquid fuel.                                          on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.4 lb per
                                                       percent oxygen,     MWh; three-run
                                                       three-run average.  average.
                                  b. Filterable PM    6.2E-02 lb per      7.5E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 1 dscm per
                                                       input; or (2.0E-    output or 8.6E-01   run.
                                                       04 lb per MMBtu     lb per MWh; or
                                                       of heat input).     (2.5E-04 lb per
                                                                           MMBtu of steam
                                                                           output or 2.8E-03
                                                                           lb per MWh).
16. Units designed to burn light  a. CO.............  130 ppm by volume   0.13 lb per MMBtu   1 hr minimum
 liquid fuel.                                          on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.4 lb per MWh.
                                                       percent oxygen.
                                  b. Filterable PM    7.9E-03 \a\ lb per  9.6E-03 \a\ lb per  Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 3 dscm per
                                                       input; or (6.2E-    output or 1.1E-01   run.
                                                       05 lb per MMBtu     \a\ lb per MWh;
                                                       of heat input).     or (7.5E-05 lb
                                                                           per MMBtu of
                                                                           steam output or
                                                                           8.6E-04 lb per
                                                                           MWh).
17. Units designed to burn        a. CO.............  130 ppm by volume   0.13 lb per MMBtu   1 hr minimum
 liquid fuel that are non-                             on a dry basis      of steam output     sampling time.
 continental units.                                    corrected to 3-     or 1.4 lb per
                                                       percent oxygen,     MWh; three-run
                                                       three3-run          average.
                                                       average based on
                                                       stack test.
                                  b. Filterable PM    2.7E-01 lb per      3.3E-01 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of 2 dscm per
                                                       input; or (8.6E-    output or 3.8 lb    run.
                                                       04 lb per MMBtu     per MWh; or (1.1E-
                                                       of heat input).     03 lb per MMBtu
                                                                           of steam output
                                                                           or 1.2E-02 lb per
                                                                           MWh).
18. Units designed to burn gas 2  a. CO.............  130 ppm by volume   0.16 lb per MMBtu   1 hr minimum
 (other) gases.                                        on a dry basis      of steam output     sampling time.
                                                       corrected to 3-     or 1.0 lb per MWh.
                                                       percent oxygen.
                                  b. HCl............  1.7E-03 lb per      2.9E-03 lb per      For M26A, collect
                                                       MMBtu of heat       MMBtu of steam      a minimum of 2
                                                       input.              output or 1.8E-02   dscm per run; for
                                                                           lb per MWh.         M26, collect a
                                                                                minimum of 240
                                                                                liters per run.
                                  c. Mercury........  7.9E-06 lb per      1.4E-05 lb per      For M29, collect a
                                                       MMBtu of heat       MMBtu of steam      minimum of 3 dscm
                                                       input.              output or 8.3E-05   per run; for M30A
                                                                           lb per MWh.         or M30B, collect
                                                                                a minimum sample
                                                                                as specified in
                                                                                the method; for
                                                                                ASTM D6784 \b\
                                                                                collect a minimum
                                                                                of 2 dscm.
                                  d. Filterable PM    6.7E-03 lb per      1.2E-02 lb per      Collect a minimum
                                   (or TSM).           MMBtu of heat       MMBtu of steam      of three dscm per
                                                       input or (2.1E-04   output or 7.0E-02   run.
                                                       lb per MMBtu of     lb per MWh; or
                                                       heat input).        (3.5E-04 lb per
                                                                           MMBtu of steam
                                                                           output or 2.2E-03
                                                                           lb per MWh).
----------------------------------------------------------------------------------------------------------------

[FR Doc. 2020-15121 Filed 8-21-20; 8:45 am]
BILLING CODE 6560-50-P


[Federal Register: February 1, 2010 (Volume 75, Number 20)]
[Notices]
[Page 5156-5157]
[DOCID:fr01fe10-120]

-----------------------------------------------------------------------

SECURITIES AND EXCHANGE COMMISSION

[File No. 500-1]

Ariel Corp., Classica Group, Inc., Commodore Environmental
Services, Inc., Dupont Direct Financial Holdings, Inc., New Paradigm
Software Corp. (n/k/a Brunton Vineyards Holdings, Inc.), Polymer
Research Corp. of America, and Shopnet.Com, Inc., Order of Suspension
of Trading

January 28, 2010.
    It appears to the Securities and Exchange Commission that there is
a lack of current and accurate information concerning the securities of
Ariel Corp. because it has not filed any periodic reports since the
period ended June 30, 2001.
    It appears to the Securities and Exchange Commission that there is
a lack of current and accurate information concerning the securities of
Classica Group, Inc. because it has not filed any periodic reports
since the period ended September 30, 2003.
    It appears to the Securities and Exchange Commission that there is
a lack of current and accurate information concerning the securities of
Commodore Environmental Services, Inc. because it has not filed any
periodic reports since the period ended June 30, 2004.
    It appears to the Securities and Exchange Commission that there is
a lack of current and accurate information concerning the securities of
Dupont Direct Financial Holdings, Inc. because it has not filed any
periodic reports since the period ended March 31, 2004.
    It appears to the Securities and Exchange Commission that there is
a

lack of current and accurate information concerning the securities of
New Paradigm Software Corp. (n/k/a Brunton Vineyards Holdings, Inc.)
because it has not filed any periodic reports since the period ended
June 30, 2001.
    It appears to the Securities and Exchange Commission that there is
a lack of current and accurate information concerning the securities of
Polymer Research Corp. of America because it has not filed any periodic
reports since the period ended September 30, 2003.
    It appears to the Securities and Exchange Commission that there is
a lack of current and accurate information concerning the securities of
Shopnet.Com, Inc. because it has not filed any periodic reports since
the period ended June 30, 2003.
    The Commission is of the opinion that the public interest and the
protection of investors require a suspension of trading in the
securities of the above-listed companies. Therefore, it is ordered,
pursuant to Section 12(k) of the Securities Exchange Act of 1934, that
trading in the securities of the above-listed companies is suspended
for the period from 9:30 a.m. EST on January 28, 2010, through 11:59
p.m. EST on February 10, 2010.

    By the Commission.
Jill M. Peterson,
Assistant Secretary.
[FR Doc. 2010-2123 Filed 1-28-10; 11:15 am]
BILLING CODE 8011-01-P


[Federal Register Volume 77, Number 182 (Wednesday, September 19, 2012)]
[Notices]
[Page 58118]
[FR Doc No: 2012-23029]

-----------------------------------------------------------------------

DEPARTMENT OF ENERGY

Federal Energy Regulatory Commission

[Docket Nos. CP12-509-000; PF11-2-000]

Freeport LNG Development, L.P., FLNG Liquefaction, LLC, FLNG
Liquefaction 2, LLC, FLNG Liquefaction 3, LLC; Notice of Application

    Take notice that on August 31, 2012, Freeport LNG Development,
L.P., FLNG Liquefaction, LLC, FLNG Liquefaction 2, LLC, and FLNG
Liquefaction 3, LLC (collectively referred to as Freeport) filed an
application pursuant to section 3(a) of the Natural Gas Act (NGA) and
Parts 153 and 380 of the Commission's regulations, requesting
authorization to site, construct, own, and operate natural gas
liquefaction and export facilities located on Quintana Island, Brazoria
County, Texas. This filing may also be viewed on the Commission's Web
site at http://www.ferc.gov using the ``eLibrary'' link. Enter the
docket number, excluding the last three digits, in the docket number
field to access the document. For assistance, call<PHONE_NUMBER> or
TTY,<PHONE_NUMBER>.
    The proposed natural gas liquefaction and export facilities will be
constructed adjacent to the existing Freeport LNG Development, L.P.'s
liquefied natural gas (LNG) import terminal on Quintana Island
(Terminal). The main liquefaction equipment will consist of three
liquefaction trains, each capable of producing a nominal 4.4 million
metric tons of LNG per annum (mtpa), for a total capacity of 13.2 mtpa.
In addition, Freeport also proposes to construct natural gas
pretreatment facilities, located approximately 2.5 miles north of the
Terminal, and appurtenant structures to support the natural gas
liquefaction and export operations.
    Any questions regarding this application should be directed to John
B. Tobola, Freeport LNG Development, L.P., 333 Clay Street, Suite 5050,
Houston, Texas 77002, or by calling<PHONE_NUMBER>; or Lisa M. Tonery,
Fulbright & Jaworski L.L.P., 666 Fifth Avenue, New York, New York
10103,<PHONE_NUMBER><EMAIL_ADDRESS>    On January 5, 2011, the Commission staff granted Freeport's request
to use the pre-filing process and assigned Docket No. PF11-2-000 to
staff activities involving the proposed natural gas liquefaction and
export project. Now, as of the filing of this application on August 31,
2012, the NEPA Pre-Filing Process for this project has ended. From this
time forward, this proceeding will be conducted in Docket No. CP12-509-
000, as noted in the caption of this Notice.
    Pursuant to Section 157.9 of the Commission's rules, 18 CFR 157.9,
within 90 days of this Notice the Commission staff will either:
complete its environmental assessment (EA) and place it into the
Commission's public record (eLibrary) for this proceeding, or issue a
Notice of Schedule for Environmental Review. If a Notice of Schedule
for Environmental Review is issued, it will indicate, among other
milestones, the anticipated date for the Commission staff's issuance of
the final environmental impact statement (FEIS) or EA for this
proposal. The filing of the EA in the Commission's public record for
this proceeding or the issuance of a Notice of Schedule for
Environmental Review will serve to notify federal and state agencies of
the timing for the completion of all necessary reviews, and the
subsequent need to complete all federal authorizations within 90 days
of the date of issuance of the Commission staff's FEIS or EA.
    There are two ways to become involved in the Commission's review of
this project. First, any person wishing to obtain legal status by
becoming a party to the proceedings for this project should, on or
before the comment date stated below, file with the Federal Energy
Regulatory Commission, 888 First Street NE., Washington, DC 20426, a
motion to intervene in accordance with the requirements of the
Commission's Rules of Practice and Procedure (18 CFR 385.214 or
385.211) and the Regulations under the NGA (18 CFR 157.10). A person
obtaining party status will be placed on the service list maintained by
the Secretary of the Commission and will receive copies of all
documents filed by the applicant and by all other parties. A party must
submit 14 copies of filings made with the Commission and must mail a
copy to the applicant and to every other party in the proceeding. Only
parties to the proceeding can ask for court review of Commission orders
in the proceeding.
    However, a person does not have to intervene in order to have
comments considered. The second way to participate is by filing with
the Secretary of the Commission, as soon as possible, an original and
two copies of comments in support of or in opposition to this project.
The Commission will consider these comments in determining the
appropriate action to be taken, but the filing of a comment alone will
not serve to make the filer a party to the proceeding. The Commission's
rules require that persons filing comments in opposition to the project
provide copies of their protests only to the party or parties directly
involved in the protest.
    Persons who wish to comment only on the environmental review of
this project should submit an original and two copies of their comments
to the Secretary of the Commission. Environmental commenters will be
placed on the Commission's environmental mailing list, will receive
copies of the environmental documents, and will be notified of meetings
associated with the Commission's environmental review process.
Environmental commenters will not be required to serve copies of filed
documents on all other parties. However, the non-party commenters will
not receive copies of all documents filed by other parties or issued by
the Commission (except for the mailing of environmental documents
issued by the Commission) and will not have the right to seek court
review of the Commission's final order.
    Motions to intervene, protests and comments may be filed
electronically via the internet in lieu of paper; see, 18 CFR
385.2001(a) (1) (iii) and the instructions on the Commission's web site
under the ``e-Filing'' link. The Commission strongly encourages
electronic filings.
    Comment Date: October 3, 2012

    Dated: September 12, 2012.
Kimberly D. Bose,
Secretary.
[FR Doc. 2012-23029 Filed 9-18-12; 8:45 am]
BILLING CODE 6717-01-P


[Federal Register Volume 88, Number 105 (Thursday, June 1, 2023)]
[Notices]
[Pages 35885-35886]
[FR Doc No: 2023-11570]

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DEPARTMENT OF HEALTH AND HUMAN SERVICES

Food and Drug Administration

[Docket No. FDA-2023-N-0742]

Human Cells, Tissues, and Cellular and Tissue-Based Product
Establishments That Are Improperly Registered in the Electronic Human
Cell and Tissue Establishment Registration System Due to Lack of Annual
Registration Update; Action Dates

AGENCY: Food and Drug Administration, HHS.

ACTION: Notice of intent.

-----------------------------------------------------------------------

SUMMARY: The Food and Drug Administration (FDA) is announcing its
intention to begin inactivating the registration of establishments that
manufacture human cells, tissues, or cellular or tissue-based products
(HCT/Ps) that have not updated their registration during the annual
update period, in accordance with FDA regulations, in the electronic
human cell and tissue establishment registration system (eHCTERS). FDA
regulations require establishments that manufacture certain HCT/Ps to
update their establishment registration annually. These regulations
also require establishments to amend their registration within 30
calendar days of certain changes.

DATES: This notice is applicable August 30, 2023.

FOR FURTHER INFORMATION CONTACT: Andrew C. Harvan, Center for Biologics
Evaluation and Research, Food and Drug Administration, 10903 New
Hampshire Ave., Bldg. 71, Rm. 7301, Silver Spring, MD 20993-0002, 240-
402-7911.

SUPPLEMENTARY INFORMATION:

I. Background

    HCT/Ps are defined in Sec.  1271.3(d) (21 CFR 1271.3(d)) as
articles containing or consisting of human cells or tissues that are
intended for implantation, transplantation, infusion, or transfer into
a human recipient. FDA has a tiered, risk-based approach to the
regulation of HCT/Ps. If all of the criteria in 21 CFR 1271.10(a) are
met, and none of the exceptions in Sec.  1271.15 (21 CFR 1271.15)
apply, then the HCT/P is regulated solely under section 361 of the PHS
Act (42 U.S.C. 264) and the regulations in part 1271 (21 CFR part 1271)
(361 HCT/P), and FDA's premarket review and approval are not required.
    Establishments that manufacture 361 HCT/Ps are required to register
and list their HCT/Ps with FDA's Center for Biologics Evaluation and
Research (CBER) using the electronic registration and listing system
(Sec. Sec.  1271.1(b), 1271.21, and 1271.22 (21 CFR 1271.1(b), 1271.21,
and 1271.22)).1 2 Under Sec.  1271.3(b), establishment
``means a place of business under one management, at one general
physical location, that engages in the manufacture of [HCT/Ps].'' This
includes ``any individual, partnership, corporation, association, or
other legal entity engaged in the manufacture of [HCT/Ps] . . . [and
includes] [f]acilities that engage in contract manufacturing services .
. . .'' Under Sec.  1271.3(e), ``manufacture means, but is not limited
to, any or all steps in the recovery, processing, storage, labeling,
packaging, or distribution of any human cell or tissue, and the
screening or testing of the cell or tissue donor.''
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    \1\ An establishment that meets any of the exceptions in Sec.
1271.15 is not required to register or comply with other
requirements in part 1271.
    \2\ Manufacturers of HCT/Ps that are regulated as drugs,
devices, and/or biological products under section 351 of the PHS Act
(42 U.S.C. 262) and/or the Federal Food, Drug, and Cosmetic Act and
applicable regulations, must register and list their products in
accordance with part 207 or part 807 (21 CFR part 207 or part 807),
as applicable (Sec.  1271.1(b)(2)). FDA does not require
establishments that manufacture HCT/Ps regulated as drugs, devices,
and/or biological products that are only for use in research under
an investigational new drug application (IND) (21 CFR part 312) or
an investigational device exemption (IDE) (21 CFR part 812) to
register and list those HCT/Ps in accordance with part 207 or part
807 if they do not engage in other activities that would require
them to register (21 CFR 207.13(e), 807.65(f), and 812.1).
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    Pursuant to Sec.  1271.21, establishments that manufacture 361 HCT/
Ps must register with FDA and submit a list of every HCT/P that they
manufacture within 5 days after beginning operations. Establishments
are required to update their registration annually each December.
Establishments are also required to update their HCT/P list when
changes occur. Such new information must be submitted at the time of
change, or each June or December, whichever month occurs first. An
establishment may accomplish its required annual registration update in
conjunction with updating its HCT/P list.
    In addition, under 21 CFR 1271.26, if the ownership or location of
the

establishment changes or if there is a change in the establishment's
U.S. agent's name, address, telephone number, or email address, then
establishments must also amend their registration within 30 calendar
days. Of note, the regulations make clear that FDA's ``acceptance of an
establishment registration and HCT/P listing form does not constitute a
determination that an establishment is in compliance with applicable
rules and regulations or that the HCT/P is licensed or approved by
FDA'' (21 CFR 1271.27(b)).
    Registration is performed using CBER's eHCTERS. Establishments
electronically submit required registration and HCT/P listing
information, as well as updates to such information, through their
eHCTERS account.\3\ The public can access eHCTERS to search and review
tissue establishment registration information (registered, inactive,
and pre-registered establishments) through the eHCTERS Public Query
Application.
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    \3\ Electronic submission of HCT/P establishment and product
listing information may be waived in certain circumstances as
described in 21 CFR 1271.23. Submission of a request for a waiver
does not excuse timely compliance with registration and listing
requirements.
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    Complete, accurate, and up-to-date establishment registration and
HCT/P listing information is essential to FDA's mission. If
registration and listing information is outdated or otherwise
unreliable, the integrity of the HCT/P registration and listing
database is compromised. Registration information assists FDA in
identifying industry participants and the scope of HCT/Ps manufactured.
This assists FDA in more efficiently monitoring industry and providing
new information including guidances, policies, and requirements.
Establishment registration information also assists FDA in reacting
swiftly to newly discovered or understood risks by enabling FDA to
quickly alert industry of our concerns and, when appropriate, to
conduct establishment inspections. Without this information, FDA would
not be able to effectively monitor compliance under FDA's risk-based
surveillance inspection program.
    Establishment registration and HCT/P listing information is also
widely used outside of FDA for various purposes. The public uses the
Public Query Application of eHCTERS to search for and locate HCT/P
establishments. For example, certain voluntary healthcare accreditation
organizations require hospitals or surgical centers to annually confirm
that their tissue suppliers are registered with FDA. Therefore,
inclusion of inaccurate or outdated information in eHCTERS can
negatively affect public health.

II. Circumstances Under Which HCT/P Registration and Listing
Information Becomes Inaccurate or Outdated

    Establishments that manufacture HCT/Ps are required to update their
registration annually in December, even if there are no changes or
updates to their information (Sec.  1271.21). Every year, many HCT/P
establishments fail to update their registration information during the
annual update period. In recent years, 390 of 2671, 379 of 2361, and
319 of 2431 registered domestic and foreign establishments failed to
submit their annual registration for 2019, 2020, and 2021,
respectively. Some of the establishments have not submitted their
annual update for more than 2 years.
    After the annual registration period ends, CBER generates a list of
establishments that have failed to submit their annual registration
update. From this list, FDA attempts to follow up with each of these
establishments to rectify their registration status. However, for a
variety of reasons, such as outdated contact information, FDA is not
able to contact some of these establishments. The follow-up process,
including sending a reminder email and contact by phone, requires
considerable additional time and FDA staff resources.
    When establishments fail to update their registration information
in eHCTERS, they are improperly registered in eHCTERS and improperly
displayed in the Public Query Application as ``Registered''. Not only
does this inaccurate and outdated information compromise the integrity
of eHCTERS, it also hinders the public's ability to rely on
establishment registration information.

III. FDA's Intended Response

    To address the above registration and listing problems, FDA is
encouraging establishments that are required to register under part
1271 to review their current registration to ensure its accuracy. Any
registrations that are outdated should be updated as soon as possible.
Establishments are required to annually update their registration
pursuant to FDA regulations. Establishments who do not submit their
annual registration are in violation of the regulations at part 1271.
    Ninety days after publication of this notice, and every January
thereafter, FDA will inactivate an HCT/P establishment's registration
when the establishment fails to submit their annual registration update
during the previous annual update period between November 15 to
December 31. FDA will no longer attempt to follow up with
establishments to rectify their registration status. The eHCTERS Public
Query Application will display the establishment registration status as
``inactive'' and include the last annual registration year. Email
notification of the inactivation will be sent to the reporting official
of the establishment, and the reporting official may access the
establishment's account in eHCTERS to change or update its
registration. If the email notifying the establishment of the change in
registration status to ``inactive'' is undeliverable, FDA will call the
phone number of the establishment to provide notification.
    If an establishment changes or updates its registration in eHCTERS
after its registration has been inactivated due to failure to annually
update registration information, the eHCTERS Public Query Application
will display the establishment's status as ``Registered'' and the last
annual registration year will be updated to the current year.

IV. Resources Available To Assist With Updating Registration and HCT/P
Listings

    Access to part 1271 is available at: https://www.ecfr.gov/current/title-21/chapter-I/subchapter-L/part-1271?toc=1. The instructions for
using eHCTERS to complete HCT/P establishment registration and HCT/P
listing and submitting the annual registration updates, as well as
information on the eHCTERS Public Query Application, are available at:
https://www.fda.gov/vaccines-blood-biologics/biologics-establishment-registration/tissue-establishment-registration. Questions concerning
registration can be emailed to [email protected].

    Dated: May 18, 2023.
Lauren K. Roth,
Associate Commissioner for Policy.
[FR Doc. 2023-11570 Filed 5-31-23; 8:45 am]
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[Federal Register Volume 79, Number 50 (Friday, March 14, 2014)]
[Notices]
[Pages 14506-14507]
[FR Doc No: 2014-05737]

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ENVIRONMENTAL PROTECTION AGENCY

[EPA-R04-OAR-2013-0577; EPA-R04-OAR-2013-0431; and EPA-R04-OAR-2013-
0648; FRL-9907-98-Region-4]

Notice of Issuance of Final Air Permits for Statoil Gulf
Services, LLC, Florida Power & Light--Port Everglades Next Generation
Clean Energy Center, and Tampa Electric Company.

AGENCY: Environmental Protection Agency (EPA).

ACTION: Notice of final action.

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SUMMARY: This notice is to announce that on October 28, 2013, the EPA
issued final Outer Continental Shelf (OCS) air quality permit numbered
OCS-EPA-R4012 for Statoil Gulf Services, LLC (Statoil); and on November
25, 2013 and December 18, 2013, the EPA issued final Prevention of
Significant Deterioration (PSD) air quality permits numbered PSD-EPA-
R4010 and PSD-EPA-R4014 for the Florida Power & Light (FPL)--Port
Everglades Next Generation Clean Energy Center (PEEC) and Tampa
Electric Company (TECO), respectively.

ADDRESSES: The final permits, the EPA's response to public comments for
these permits, and supporting information are available at http://www.epa.gov/region4/air/permits/index.htm. Copies of the final permits
and the EPA's response to comments are also available for review at the
EPA Regional Office and upon request in writing. The EPA requests that
you contact the person listed in the FOR FURTHER INFORMATION CONTACT
section to schedule your inspection. The Regional Office's official
hours of business are Monday through Friday, 8:30 a.m. to 4:30 p.m.
excluding Federal holidays.

FOR FURTHER INFORMATION CONTACT: Please contact Ms. Heather Ceron, Air
Permits Section Chief, Air Planning Branch, Air, Pesticides and Toxics
Management Division, Region 4, U.S. Environmental Protection Agency, 61
Forsyth Street SW., Atlanta, Georgia 30303-8960. The telephone number
is<PHONE_NUMBER>. Ms. Ceron can also be reached via electronic mail at
<EMAIL_ADDRESS>
SUPPLEMENTARY INFORMATION: On August 9, 2013, EPA Region 4 requested
public comments on a preliminary determination to issue an OCS air
permit for Statoil. During the public comment period, which ended on
September 9, 2013, the EPA received no comments.
    On May 31, 2013, EPA Region 4 requested public comments on a
preliminary determination to issue a PSD air quality permit for the FPL
PEEC project. A total of 26 comments from 3 commenters, including 1
request for a public hearing, were received (via email and letter)
during the public comment period, which closed on July 2, 2013.
    On September 24, 2013, EPA Region 4 requested public comments on a
preliminary determination to issue a PSD air quality permit for the
TECO project. A total of 25 comments from two commenters were received
(via email) during the public comment

period, which closed on October 25, 2013.
    The EPA reviewed each comment received and prepared a Response to
Comments document for the two projects. After consideration of the
expressed view of all interested persons, the pertinent federal
statutes and regulations, the applications and supplemental information
submitted by the applicants, and additional material relevant to the
applications and contained in the Administrative Records, the EPA made
final determinations in accordance with title 40 CFR part 52 and part
55 (for Statoil) to issue final air permits.
    Under 40 CFR 124.19(f)(2), notice of any final Agency action
regarding a PSD permit must be published in the Federal Register.
Section 307(b)(1) of the CAA provides for review of final Agency action
that is locally or regionally applicable in the United States Court of
Appeals for the appropriate circuit. Such a petition for review of
final Agency action must be filed within 60 days from the date of
notice of such action in the Federal Register. For purposes of judicial
review under the CAA, final Agency action occurs when a final PSD
permit is issued or denied by the EPA and Agency review procedures are
exhausted, per 40 CFR 124.19(f)(1).
    Any person who filed comments on the draft permits was provided the
opportunity to petition the Environmental Appeals Board by the end of
November 26, 2013 for the Statoil permit, by the end of December 26,
2013 for the PEEC permit, or by the end of January 17, 2014 for the
TECO permit. No petitions were submitted for any of these permits.
Therefore, the Statoil permit became effective on November 27, 2013.
The PEEC permit became effective on December 27, 2013. This date was
changed from December 25, 2013, as stated on the final permit, to
correct for the effective date coinciding with a federal holiday. The
TECO permit became effective on January 18, 2014.

    Dated: February 27, 2014.
Carol L. Kemker,
Acting Director, Air, Pesticides and Toxics, Management Division,
Region 4.
[FR Doc. 2014-05737 Filed 3-13-14; 8:45 am]
BILLING CODE 6560-50-P