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Quarterly Inventory
• The quarterly Inventory subfunction is selected by the user desiring
• to ascertain the amount of Information available for a site-pollutant-year-
quarter combination. If the combination exists on the quarterly file,
• the programs provide the user with the number of observations recorded;
the maximum value that occurred; and, if the criteria restraints are
• met, the arithmetic mean.
• The user is offered a chance to print the valid command list for
this subfunction. If the comnand list is needed, the user should reply
• 'yes1. If the command list is unnecessary, the user should reply 'no'.
The user begins to make his selections after the messages, 'START
| ENTERING COMMANDS', and 'COMMAND?1. 'COMMAND?1 is always used to indicate
g when the user can enter commands.
™ Basically the commands can be divided into two types. The selection
fl commands are used to specify location, pollutant, and time information.
The action commands are used to instruct the program to perform some task.
| The selection commands and their functions are:
— (1) 'state*??1 the code for the state desired. Example:
* state=01,
• (2) 'area-.'?:'?' the code for the city or county desired.
Example: area* 1300.
| (3) 'site*???' the site number within the state. Example:
site=001,
• (4) 'agency*?' - the code for the sponsoring agency. Example:
Iagency-g.
^
I
I
-------
(5) 'project*??1 - the cod« for the type of sampling.
Example: project-01.
(6) 'pollutant0?????' - the code for the pollutant dtsired.
Example: pollutant*11101.
(7) 'method*??' - the code for the sampling method.
Example: method=91.
(8) '1nterval=?' - the code for the sampling interval.
Example: interval=7.
(9) 'year*??' - the y«ar desired. Example: year*66.
(10) 'quarter=??' - the quarter desired. Example: quarter«01.
(11) 'key=????????????????????????' - (24 characters)
the complete key for the information composed
of the state, area, site, agency, project,
pollutant, method, Interval, year, and quarter
in the order listed. The 'key' command is
provided as a quick method of entering the
desired Information. A partial key can be
entered to position the file at a desired point
so the find and next commands can be used to
retrieve subsequent information.
The action commands and their results are:
(1) 'find1 - indicates that the user has entered all the
selection Information he wishes to sptdfy.
The program uses the Information specified
and attempts to find a matching key on the
summary file. If a match Is found, the Info-
mat Ion for the sltt-pollutant-yetr-quarttr
c->:Lin«tion is printed and the 'COMMAND'
16
-------
I
I-
prompt follows. If a match was not found,
| the message, 'NO MATCH FOUND FOR KEY
- key CORRECT OR ASK FOR NEXT RECORD1 is
• returned. The user has the option of
fl requesting the next sequential combination
via the 'next' command or entering new
J selection information. If the key requested
is greater than the largest key recorded in
I the file, the message, 'KEY key_ GREATER THAN
• HIGHEST POSSIBLE KEY. ENTER KEY LESS THAN
OR EQUAL highest key't is printed. Any valid
• command other than 'next1 can be entered at
this point.
• (2) 'next ??' - indicates that the user wishes to have the
• information for the next '??' sequential
combinations printed. The '??' represents
• any two digit number from 01 to 99. If '??'
is entered as blanks, one is assumed. If
P the end of the file is reached, the message,
- 'END OF DATA ENTER NEW COMMAND', 1s printed.
• The user can enter any valid command other
• than 'next'.
If an invalid entry for '??' is entered,
J the user 1s notified and a new command is
called for.
I ^
I
I
-------
(3) 'end1 - signals the end of user requests for the
quarterly Inventory function. The program
returns control 10 the master program and
other functions can be requested.
Please note that the entire command can be entered or the first
two letters of the command can be used. Example: next 02 or ne 02.
18
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21
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Yearly Inventory
The yearly Inventory subfunction 1s selected by the user desiring
to ascertain the amount of Information available for a site-pollutant-
year combination. If the combination exists on the yearly file, the
program provides the user with the number of observations recorded;
the maximum value that occurred; and, if the criteria restraints are met,
the arithmetic mean.
The user is offered a chance to print the valid command list for
this subfunction. If the command list is needed, the user should reply
'yes1. If the command list 1s unnecessary, the user should reply 'no1.
The user begins to make his selections after the messages, 'START
ENTERING COMMANDS', and 'COMMAND?1. 'COMMAND?1 is always used to indicate
when the user can enter commands.
Basically the commands can be divided into two types. The selection
commands are used to specify location, pollutant, and date information.
The action commands are used to instruct the program to perform some task.
The selection commands and their functions are:
(1) 'state=??' - the code for the state desired. Example:
state*01.
(2) 'area=????' - the code for the city or county desired.
(3) 'site*???' •• the site number within the state. Example:
site-1300.
(4) 'agency2?' - the code for the sponsoring agency. Example:
ajency*g.
22
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(5) 'project3??' - the code for the type of sampling.
Example: project=01
(6) 'pollutant-?????' - the code for the pollutant desired.
Example: pollutant=l 1101 .
(7) 'method*??' - the code for the sampling interval.
Example: method=91 .
(8) 'Interval8?' - the code for the sampling interval.
Example: interval2?.
(9) 'year*??1 - the year desired. Example: /e«r«Cfc
(10) 'key*??????????????????????' - (22 characters)
the complete kev for the information composed
of the state, area, site, agency, project, pollutant,
method, interval and year in the order listed.
The 'key' command is provided as a quick method
of entering the desired information. Example:
key=011300001qOmiOl91766. A partial key can
be entered to position the file at a desired point
to enable the use of the find and next commands
to retrieve subseouent information.
The action commands and their results are:
'find' - indicates that the user has entered all the
selection information he wishes to specify. The
program uses the information specified and
attempts to find a matching key on the summary
file. If a match is found, the information
for the site-pollutant-year combination is
printed and the 'COfiMAND' promot follows.
If a match was not found, the message, 'NO
23
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MATCH FOUND FOR KEY' key_ 'CORRECT OR ASK
FOR NEXT RECORD1 i, printed. If the key
requested is greater than the largest key
recorded in the file, the message, 'KEY
key_ 'GREATER THAN HIGHEST POSSIBLE KEY.
ENTER KEY LESS THAN OR EQUAL 'highest key',
is printed. Any valid command other than
'next' can be entered at this point.
(2) 'next ??' - indicates that the user wishes to have the
in format1 on for u,<.- next '?">' sequential
combinations printed. The '??' represents
any two digit nur,;rer from 01 to 99. If
'::' is entered a; blanks, one is assumed.
If the end of the file is reached, the
f.e^d-jfc, 'END OF DATA ENTfK NEW COMMAND1,
is pnrited. The user can enter any valid
L0>nr.id' '-'. other than 'next'.
If an invalid entry for '??' is entered,
the user is notified and a new command is
called for.
(3) 'end' - signals the end of user requests for the
yrat iy inventory function. The program
rfcU-rn:, control to the master program and
other functions can be requested.
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• Please note that the entire command can be entered or the first two
letters of the command can be used. Example: next 02 or ne 02.
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I
I-
I Quarterly Summary
• The quarterly summary subfunction is selected by the user desiring
statistical information for a site-pollutant-year-quarter combination.
• If the combination exists on the quarterly file, the user can obtain
the information he specified utilizing the summary information selection
M commands. If the combination does not exist on the file, the user has
• the option of specifying a new combination or requesting the sequential
combination following the key he specified.
• The first choice the user must make regards the listing of valid
program commands. The user is given the option of printing the commands
1 or proceeding directly to tne data selection. If 'yes1 is entered, the
•» commands are listed. If 'no' is entered, the user is asked to enter his
first command.
fl The program commands can be divided into two classes. The selection
commands specify the data desired and the action corrinands request the
• program perform some task. The selection commands can be further divided
_ into site-pollutant commands and summary information commands.
• The site-pollutant selection commands are:
• (1) 'state*??' - the state desired. Example: state=01.
(2) 'area=????' - the code for the city or county desired.
• Example: area=1300.
(3) 'site*???1 - the site number within the area desired.
P Example: site=001.
• (4) 'agency-? • the code for the sponsoring agency.
L «uii.^le: agency-*.).
I
I
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(5) 'project3??' - the code for the type of sar.plinq.
Fxample: projected.
(6) 'pollutant*?????1 - the code for the pollutant desired.
Example: pollutant=11101.
(7) *method=??' - the code for the sampling method.
Example: method=°l.
(8) 'interval--?' - the code for the sanTlino interval.
Example: interval^/.
(9) 'year=??' - the code for the vear desired. Example: year=66
(10) 'quarter3??' - the code for the quarter desired. Exanple: ouarter=01.
(11) 'key=???????????????'???????? - (24 characters)
the complete key for tne information composed
of the state, area, site, agency, project,
pollutant, method, year, and quarter in the
order listed. The 'key' command is provided
as a ouick method of enterinq information.
Example kev=--0]130L001q0111 !ClC'176tPl .
P partial Key can be entered to position the file at
a desired noint to erahL- tr <•> user to enter the find and
next commands to retrieve suhseouent information.
The summary information selection commands are:
(1) 'observ' - tn^ nun^er of observations stored in the
tidta tank for the comtination specified.
(2) 'max1 - the maximum observation that occurred for
the combination specified.
(3) 'rnin1 - tne minimum observation that occurred for
the combination snecifiea.
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(4) 'amean' - the arithmetic mean. The value is printed
only if the criteria restraints of NADB are
met.
(5) 'gmean1 - the geometric mean. The value is printed
only if the criteria restraints of NADB are met.
(6) 'astdev1 - the arithmetic standard deviation. The value
is printed only if the criteria restraints
of NADB are met.
(7) 'gstdev' - the geometric standard deviation. The value
is printed only if the criteria restraints
of NADB are met.
(8) '%observ' - the percentage of possible observations that
are present. This value is blank for time
intervals that would make the value meaningless.
(9) 'zsub1 - the value substituted for data values less
than the minimum detectable in the computations,
This value represents an approximation to one
f-alf the minimum detectable.
(10) 'zcnt' - the number of times the 'zsub' value was
substituted in the computations.
Initially, the program is set up not to print any of the summary
information. Specific requests for items are made by entering the appro-
priate command after the 'COMMAND?' prompt. If at a later point in the
program some item of information requested is no longer needed, printing
31
-------
of this Information can be suppressed by entering the letter X followed
by the summary information selection command corresponding to that
information. For example, if the maximum value was requested by the
command, 'max', the command to suppress the printing would be 'xmax1.
The action commands and their results are:
(1) 'find1 - indicates that the user has entered all the
selection information desired. The program
uses the information specified and attempts
to find a matching key on the summary file.
If a match is found, the information for the
site-pollutant-year-quarter combination
requested is printed, followed by the
'COMMAND?' prompt. If the match was not
found, the message, 'NO MATCH FOUND FOR KEY
key CORRECT OR ASK FOR NEXT RECORD,' is
returned. The user has the option of
requesting the next sequential combination
via the 'next1 command or entering new
selection information. If the key requested
is greater than the largest key recorded in
the file, the message, KEY 'key' GREATER
THAN HIGHEST POSSIBLE KEY. ENTER KEY LESS
THAN OR EQUAL 'highest key', is printed.
Any valid command other than 'next' can be
entered at this point.
32
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I
(2) 'next ??' - Indicates that the user wishes to have the
I Information selected for the next '??'
• sequential combinations printed. The '??'
represents any two digit number from 01 to
I 99. If '??' is entered as blanks, one is
assumed. If the end of the file is reached,
§ the message, 'END OF DATA ENTER NEW COMMAND1,
. is printed. The user can enter any valid
* command other than 'next'.
• (3) 'end' - signals the end of user requests for the
quarterly summary function. The program
|| returns control to the master program and
other functions can be requested.
• Please note that the entire command can be entered or the first two
Ij letters of the command can be used. The only time the two letter
abbreviation is not sufficient is when negating the summary information
• commands. The negative command requires at least three letters. For
example, if 'max' was specified and no longer wanted, the user can
• suppress the maximum by entering xmax or xma.
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• ^ Yearly Summary
| The yearly summary subf unction is selected by the user desiring
. statistical information for a site-pollutant-year combination. If the
combination exists on the yearly file, the user can obtain the information
ft he specified utilizing the summary information selection commands. If
the combination does not exist on the file, the user has the option of
£ specifying a new combination or requesting the sequential combination
— following the key he specified.
" The first choice the user must make regards the listing of valid
• program commands. The user is given the option of printing the commands
or proceeding directly to the data selection. If 'yes' is entered, the
• commands are listed. If 'no1 is entered, the user is asked to enter his
first command.
• The program commands can be divided into two classes. The selection
«| commands specify the data desired and the action commands request program
perform some task. The selection commands can be further divided into
• site-pollutant commands and summary information commands.
The site-pollutant selection commands are:
j| (1) 'state-??1 - the state desired. Example: state*01.
— (2) 'area=????' - the code for the city or county desired.
™ Example: area=1300.
• (3) 'site*???1 - the site number within the area desired.
^
I
Example: site=001.
(4) 'agency=?' - the code for the sponsoring agency.
Example: agency=g.
37
I
-------
(5) 'project0??' - the code for the type of sampling.
Example: project»01
(6) 'pollutant*?????' - the code for the pollutant desired.
Example: pollutant»11101.
(7) 'method*??' - the code for the samoling method.
Example: method-91.
(8) 'interval3?' - the code for the sampling interval.
Example: interval*?.
(9) 'year=??' - the code for the year desired. Example: year=66,
(10) 'key=??????????????????????' - (22 characters)
the complete key for the information composed
•
of the state, area, site, agency, project,
pollutant, method and year in the order
listed. The 'key' command is provided as
a quick method of entering information.
Example: ke.y=C11300001 qOllllGl 91766. />
partial key can be entered to position the
file at a desired point to enable the user
to enter the find and next commands to
retrieve subsequent information.
TI.e summary information selection commands are:
(1) 'observ' - the number of observations stored in the
data bank for the comhinaion specified.
(2) 'max1 - the maximum observation that occurred for
combination specified.
(3) 'min' - the minimum observation that occurred
for the combination specified.
38
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I
I — (4) 'amean' - the aritmetic mean. The value is
_ printed only 1f the criteria restraints
™ of NADB are met.
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(5) 'gmean' - the geometric mean. The value 1s printed
only If the criteria restraints of NADB
are met.
(6) 'astdev' - the arithmetic standard deviation. The value
Is printed only If the criteria restraints
of NADB are met.
(7) 'gstdev' - the geometric standard deviation. The value
is printed only if the criteria restraints
of NADB are met.
(8) 'Xobserv' - the percentage of possible observations that
are present. This value is blank for time
intervals that would make the value meaningless.
(9) 'zsub' - the value substituted for data values less than
the minimum detectable in the computations.
This value represents an approximation of one
half the minimum detectable.
(10) 'zcnt1 - the number of times the 'zsub' value was
substituted in the computations.
Initially, the program is set up not to print any of the summary
information. Specific requests for items are made by entering the
appropriate command after the /COM1AND?' prompt. If at a later point in
the program some item of information requested is no longer needed,
printing of this information can be suppressed by entering the letter X
followed by the summary information selection command corresponding to
that information. For example, if the maximum value was requested by
40
-------
I
I
the command, 'max', the command to suppress the printing would be
J 'xmax*.
The action commands and their results are:
• (1) 'find' - Indicates that the user has entered all the
£ selection Information desired. The program
uses the Information specified and attempts
• to find a matching key on the summary file.
If a match 1s found, the Information for
| the site-pollutant-year combination requested
_ 1s printed, followed by the 'COMMAND?' prompt.
* If the match was not found, the message, 'NO
• MATCH FOUND FOR KEY key_ CORRECT OR ASK FOR
NEXT RECORD', 1s returned. The user has the
] option of requesting the next sequential
_ combination via the 'next* command or entering
" new selection Information. If the key
• requested 1s greater than the largest key
recorded 1n the file, the message, KEY 'key'
I GREATER THAN HIGHEST POSSIBLE KEY. ENTER KEY
LESS THAN OR EQUAL 'highest key'. 1s printed.
• Any valid command other than 'next' can be
m entered at this point.
(2) 'next ??' - Indicates that the user wishes to have the
• information selected for the next '??'
i
i
i
-------
sequential combinations printed. The '??'
represents any two digit number from 01 to
99. If '??' Is entered as blanks, one 1s
assumed. If the end of the file 1s reached,
the message, 'END OF DATA ENTER NEW COMMAND1,
is printed. The user can enter any valid
command other than 'next'.
If an Invalid entry for '??' 1s entered,
the user Is notified and a new command Is
called for.
(3) 'end1 - signals the end of user requests for the
yearly summary function. The program returns
control to the master program and other
functions can be requested.
Please note that the entire command can be entered or the first two
letters of the command can be used. The only time the two letter
abbreviation is not sufficient is when negating the summary information
commands. The negative command requires at least three letters. For
example, if 'max* was specified and no longer wanted, the user can
suppress the maximum by entering 'xmax' or 'xma'.
42
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Pollutant Names
I The pollutant names subfunction 1s selected by users desiring the
_ pollutant name corresponding to a five digit pollutant code. If the
™ code 1s one for which a pollutant name has been assigned by NADB staff,
• the name Is returned. If the code entered is not matched, a new pollutant
must be specified or the command 'end1 entered.
J The commands associated with this function are:
(1) 'pollutant3?????' - the code for which a pollutant name is
• desired. Example: pollutant=11101.
• (2) 'find' - Indicates that the user has specified a
pollutant code and is ready for the program
• to search for the name. If a match is
found, the pollutant name 1s printed. If
• a match was not found, the message, 'INVALID
m POLLUTANT CODE = pollutant code. ENTER NEW
POLLUTANT CODE', is printed. The user can
• enter a new code or the 'end1 command.
(3) 'next ??' - requests that the next '??' sequential
| pollutant names be printed. '??' represents
g any two digit number from 01 to 99. If blanks
* are entered for '??', 01 is assumed. If the
• end of the data file is encountered while
processing this command, the message, 'END
| OF DATA. ENTER NEW CODE', is printed.
I-
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-------
_ (4) 'end1 - signals the end of requests for pollutant
* names. Control 1s returned to the master
• program.
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Please note that the entire command can be entered or the first two
letters of the command. For example, next 02 or ne 02 1s a valid command.
47
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UNITS TADI.C
The: unit:, table sub-function prints the um-cnt i!/'.!
units cnd;.r; oncl their n.-;ndr. .•••^f-ocinU'
with this M.'hfunction. Upon completion 01 tl.c table listing,
control is returned to the ir.?j,t'.-v prr'^r-"1.
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I
|v~
Remote Batch Submissions
| The master program for the data bank Interactive system 1s
_ automatically Invoked when the command, nadbtso, 1s entered. If
™ parm (noprint) or parm (nop) 1s not specified, the master program
• automatically lists the possible function requests and their de-
scription. To request that the descriptions not be printed, enter:
I nadbtso parm (noprint) or nadbtso parm (nop). Otherwise, enter:
nadbsto.
• The possible function requests and their descriptions are:
• (1) qfreq - quarterly frequencies. Common percentlles
are printed for each state requested by year
• quarter. The state(s) or region desired
must be specified.
• (2) yfreq - yearly frequencies. Yfreq 1s like qfreq
• except the Information 1s given on a yearly
basis.
V (3) rawdl - raw data listing for 24 hour or greater data
values. The year and single pollutant desired
| must be specified along with the state(s) or
_ region desired.
• (4) end - signals the user's desire to terminate the
• terminal session. When this command 1s entered,
an appropriate message 1s printed and the data
£ bank procedure 1s completed. The user should
allow a short time for the system to submit the
•^ remote batch jobs specified and reallocate the
• resources dedicated to the user.
50
I
-------
I
1^,
The site, glnv, ylnv, gsum, ysum, and poll commands are
- used 1n the Interactive access explained 1n that section of
™ the manual.
• When the system has completed Us tasks, the user 1s notified
that he has logged off the system. He should turn off the terminal
• and coupler and return the phone to Its cradle.
Initially the user 1s requested to enter his user Identification
• number. This number Is required to submit remote batch jobs.
• The user 1s prompted to choose a function by the program message
SITE, QINV, YINV, QSUM, YSUM, POLL, QFREQ, YFREQ, RAWDL, OR END? The
• user types his selection and pushes the return key. The master program
evaluates the user request. If the request 1s valid the corresponding
I subprogram Is called and control relinquished to the subprogram. The
• 'END* command does not require a subprogram since 1t just Indicates
the session termination. If the user command 1s not one of the valid
8 commands, the user receives a message Indicating the command 1s Invalid
and 1s given the opportunity to enter a new command.
| The user can choose to enter the complete command or abbreviate
_ the command to the first two letters. An example 1s 'si1 for 'site-'.
™ The program processes both commands In the same manner.
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™ Quarterly Frequencies
I ^ The quarterly frequency subfunction 1s selected by the user
• desiring common percent He distributions on a quarterly basis. The
user must specify either a region desired or the state(s) desired.
I If a user chooses to specify the states desired, he may specify a
maximum of five states.
I The user 1s given the opportunity to 11st the valid commands
_ Initially. If the list 1s needed, the user should reply yes. Other-
™ wise the user should reply no.
• After the user makes this Initial decision, he Is requested to
enter the Identification assigned to the terminal to which the output
| 1s to be sent. For example, on the RTCC computer, 1f you wish your
— print sent to the computer room, you enter: local.
* The user batch account number Is also required for both sub-
• missions. The user 1s required to enter the assigned code.
The program prompts the user with messages, 'START ENTERING
| COMMANDS' and 'COMMAND?' to enter his selections. The possible
commands are:
I (1) 'year-??1 - The single year for which data 1s desired.
— If this command 1s not used, all years are
™ printed. Example: year-66.
• (2) 'quarter-??' - The single quarter for which data 1s desired.
If this command 1s not used, all quarters
| are printed. Example: quarter»01.
(3) 'pollutant-?????' - The single pollutant for which data 1s
• desired. If this command 1s not used, all
pollutants are printed.
Example: pollutant-Ill01.
I
I
-------
(4) 'Interval*?1 - The single Interval for which data 1s desired.
If this command 1s not used, all Intervals
are printed. Example: Interval=7.
(5) 'state*??,??,??,??,??1- The 11st of states desired separated
by commas. The maximum number of states that
can be specified 1s five. If the state
command Is entered, any region command
entered previously 1s Ignored. Example:
state»01.
(6) 'region*??' - The region desired. If the region command
1s entered, any state command entered
previously is ignored. Example: region=01.
(7) 'end' - Signals that the request specifications are
complete. The batch job is prepared for
submission and the specifications printed.
The user is given an opportunity to either
request the job as specified or to force
the job to fail.
All commands can be entered in their entirety or abbreviated to
the first two letters of the command. A valid entry for either the
region command or the state command is required for job submission.
If any command except end is entered and you wish to cancel it, enter
the command followed by the number of ampersands corresponding to the
number of digits required by the command. An example of cancelling
a command is: pos&&&&&.
54
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N YOU WISH TO ACCESS.
M,YSUM, POLL, QFREQ, YFREQ. RANDL, OR END?
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I
B Yearly Frequencies
• The yearly frequency subfunction is selected by the user desiring
common percent!le distributions on a yearly basis. The user must
I specify either a region desired or the state(s) desired. If a user
chooses to specify the states desired, he may specify a maximum of
• five states.
• The user 1s given the opportunity to list the valid commands
Initially. If the 11st 1s needed, the user should reply yes. Other-
• wise the user should reply no.
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• enter the identification assigned to the terminal to which the output
• 1s to be sent. For example, on the RTCC computer, if you wish your
print sent to the computer room, you enter: local.
I The user batch account number is also required for batch
submissions. The user is required to enter the assigned code.
I The program prompts the user with messages, 'START ENTERING
_ COMMANDS' and 'COMMAND?' to enter his selections. The possible
commands are:
• (1) 'year*??' - The single year for which data is desired.
If this command 1s not used, all years are
I printed. Example: year-66.
(2) 'pollutant=?????'- The single pollutant for which data is
| desired. If this command is not used, all
•pollutants are printed. Example:
pollutant=11101.
• j (3) 'interval*?' - The single interval for which data 1s desired.
I
If this command is not used, all Intervals
are printed. Example: interval*?.
59
-------
I
I
I
(4) 'state-??,??,??,??,??1- The list of states desired separated
by commas. The maximum number of states that
can be specified 1s five. If the state
command 1s entered, any region command •
entered previously 1s Ignored. Example:
state«01. I
(5) 'region-??' - The region desired. If the region command •
1s entered, any state command entered
previously 1s Ignored. Example: reg1on«01. I
(6) 'end* - signals that the request specifications are
complete. The batch job Is prepared for |
V
submission and the specifications printed.
The user 1s given an opportunity to either .
request the job as specified or to force
the job to fall.
All commands can be entered In their entirety or abbreviated to
the first two letters of the command. A valid entry for either the
region command or the state command Is required for job submission.
If any command except end Is entered and you wish to cancel 1t, enter
the command followed by the number of ampersands corresponding to the
number of digits required by the command. An example of cancelling
a command Is: po-44444.
60
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I
I-
m Raw Data Listing
• The raw data listing subf unction 1s chosen by the user desiring
• a 11st of data values for 24 hour or greater data. The user Is required
to specify either a region desired or the state(s) desired. The sub-
I program limits the user to a single pollutant and a single year. If
any one of the required Items 1s not specified, the batch job 1s forced
P to fall. The user can also specify the Interval or Intervals desired.
— The default value for the Interval 1s 7 which specifies 24-hour data only.
* The user 1s Initially given the opportunity to list the valid
• commands. If the command 11st Is desired, enter yes. Otherwise, enter no.
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I the Identification assigned to the terminal to which the output is to be
sent. For example, on the RTCC computer 1f you wish your print sent
• to the computer room, you enter: local.
• The user batch account number is also reouired for batch
submissions. The user is required to enter the assigned code.
I The program prompts the user with messages, 'START ENTERING
COMMANDS' and 'COMMAND?' to enter his selections. The possible
P commands are:
(1) 'year*??1 - The year desired. This entry 1s required.
I If no year 1s entered, the job will be forced
• to fall. Example: year=66.
(2) 'pollutant'?????1 - The pollutant desired. This entry is
I required. If no pollutant is specified,
the job will be forced to fall. Example:
pollutant=11101.
I
I
-------
(3) 'Interval-?' - The Interval desired. The Interval 1s 7
unless otherwise specified. If more than
one Interval 1s desired, repeated usage
of the command 1s Involved. Example:
Interval»8.
(4) 'state-??,??,??,??,??'- The 11st of states desired separated
by commas. The maximum number of states
that can be specified 1s five. If the state
command Is entered, any region command
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state-01.
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1s entered, any state command entered
previously 1s Ignored. Example: reg1on*0l.
(6) 'end1 - Signals that the request specifications are
complete. The batch job Is prepared for
submission and the specifications printed.
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request the job as specified or to force
the job to fall.
All commands can be entered 1n their entirety or abbreviated to
the first two letters of the command. A valid entry for either the
state or region command 1s required for job submission. If any command
except end 1s entered and you wish to cancel 1t, enter the command
followed by the number of ampersands corresponding to the number of digits
required by the command. An example of cancelling a command 1s: po*ft&&&&.
66
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STANDARDS PROGRAMS
yr:- « • •
• j • The HADB standards procjrams are a series of programs written
Ij to furnish reports for the pollutants for which standards have boon
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,.... 1 set. These reports encompass the three formats shown in the samples
I . following. Asterisks adjacent to values indicate that the values
^, \ exceed the priniary standard listed at the bottom of the report. rPlus
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the bottom of the report was exceeded. The number of times each
standard was exceeded is totaled at the bottom. Other items en
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£'i percent of possible observations, the basis for the standards, the
I method of collection, and the method of analysis.
The user is initially offered the choice of a command list. If
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• j • The user begins to make his selections following the prompts,
; 'START ENTERING CO^'-ANDS1 and 'COMMAND?'. The 'COMMAND?1 prompt is
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user commands are:
- The state(s) desired. If the region
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equals five states. Example: state-01.03.
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1 70.1
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(4) 'y,.'-"•'•??' - fhr y^r <•';"_; irc'.i. l.liiifL is one yo?r per rc
No daUi is civjilciblc prior Lo I9b7. Ycf>r
a required con^u-nd.
(5) 'one!' - Signifies em! of request.
The entire command or the first two letters of the
can be used.
The user must enter the identification code for the terminal
to which tho print should bo rouu.<-!. For example, remotc?5. The
user's batch recount nur.ber c.nd the user's nsrco is also rc'Cjirirod.
After all the user selections hove been raade and the end co:r:w,%,v.!
has been cnix-rad, the u^er rec>i!2sts are listed end the user can chpust:
to arcept oi' reject the job. Should tlv; job be accepted, it will be
subiiiittrd upon successful completion of tiie n:ic!!;tso proccdi'rt.
70.1.2
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I
• SAROAD Mailed Request System
fl Data are available in formats other than those described in the
previous sections. These can be requested by contacting:
| Environmental Protection Agency
_ National Air Data Branch
• 411 West Chapel Hill Street
• Durham, North Carolina 27701
(919) 688-8146, Ext. 261
• If the number of requests for these routines becomes excessive,
they will be made available under the TSO Air Pollution Access System
m if possible. Some routines are in this section because they require
M special equipment or special skills to use. If you are not a Federal
Government employee, first try to request data from your EPA regional
V office. The addresses of the regional offices can be found in Appendix 2.
When you make a request you must have the SAROAD code. Other
| requests cannot be honored. For example a request for data from
_ Denver, Colorado is insufficient. The request must be for data from
* state 06 and city 0580.
• A list of the codes necessary to request data can be obtained at
the above address.
• Other programs dealing with trend analyses and statistical analyses
are available or being developed. However, we cannot make these available
™ at this time due to a lack of resources. If you have a specific project,
• contact us at the above address and we may be able to offer you the
I
I
-------
programs. Also, 1f you have requests for other programs, contact us
at the above address. Following are descriptions of the available mall
requests.
72
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I
I-
Yearly Report by Quarters
The yearly report by quarters has been used in the past to
g satisfy general requests for data. The report by quarters was used
m because many pollutants follow a seasonal trend and the annual average
• alone is often insufficient to identify the trends. Utilizing this
• report, one can examine patterns by quarter as well as examining
annual trends.
• The yearly report by quarters does not relate the data to the
standards. Therefore, the report will probably receive a more limited
• usage than in the past.
• Sample output for the yearly report by quarters is shown in
Figure 1 on the following page.
I In order to request a yearly report by quarters, the following
information must be provided in the request:
I 1. Pollutants desired. Which pollutant or pollutants are you
« interested in? Are you interested in all pollutants?
™ 2. Method, units, and interval. For each pollutant desired
• . are you interested in a particular method, units, and/or interval?
3. Site combination. Are you interested in a specific site,
J city, county, state, region and/or any combination thereof?
4. Year. Are you interested in a specific year or specific
• years?
• 5. Summarization. Do you want pollutants summarized
separately? Please note that separate summarization involves multiple
requests and can only be done for a few pollutants, not all.
i
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74
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I
Raw Data Ustina (less than ?4 hour)
• The raw data mall request 1s used currently to present data with a
1-hour, 2-hour, or 4-hour sampling Interval. Detailed Information by
| month for each pollutant-site is offered. The basic values (1-hour,
_ 2-hour, or 4-hour) are listed across the page. If 75% or more of the
* values are present for a day, the daily average is calculated. The
• number of values per day is also listed.
Diurnal variation is also displayed for the month. Along the bottom,
• the average for each 1-hour interval (or 2-hour interval, or 4-hour
interval) is displayed if 75% or more of the values are present for that
• interval in that month. The number of values and a maximum is also
• displayed.
A monthly average 1s calculated if 75% or more of the values are
• present and a monthly maximum is listed. Saturdays and Sundays are
identified by an asterisk following the "DAY." The format is as shown
I in Figure 3 on the following page.
The following information must accompany the request for a raw data
M
" listing:
•
1. Pollutant. Which pollutant or pollutants are you interested
2. Method, unit. For each pollutant are you interested in a
— certain method and/or units?
• 3. Interval. Which interval are you interested in?
• 4. Site combination. Are you interested in a specific site,
city, county, state, and/or region?
" 5. Date. Are you interested in a specific month, quarter,
year, or years?
78
I
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APPENDIX I
Criteria Restraints of the NADB for Averaging
In order to assume some integrity of the values, summary statistics
are automatically not calculated unless the data meet certain minimum
criteria. These criteria guarantee a minimum number of samples and that
the samples are distributed throughout the time period.
1. Continuous data (currently this is 1-hour data, 2-hour
data, and 4-hour data).
a. No quarterly statistics are constructed unless 75%
of the individual hourly values are present.
b. No yearly statistics are constructed unless 75% of
the individual hourly values are present.
2. Daily data (24-hour sampling interval). The daily data
is usually generated on a random or systematic schedule, so a straight
percentage is not possible. The following criteria are based on the
old National Air Surveillance Network's schedule of 26 samples per year.
a. No quarterly statistics are constructed unless there
are a minimum of 5 samples per quarter. A second constraint is that
if one month has no values, there must be at least two values in each of
the other two months. To reword this criteria we are excluding data
where there are no samples in each of two months and 5 or more in the
third; and where there are no samples in one month, one sample in
another, and 4 or more in the third.
b. No yearly statistics are constructed unless all four
quarters in the year meet criteria.
80
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3. Monthly data.
a. No quarterly statistics are constructed unless two
I months have values.
b. No yearly statistics are constructed unless all four
• quarters meet criteria.
m 4. Quarterly data.
No yearly statistics are constructed unless all four quarters
I are present.
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APPENDIX II
ENVIRONMENTAL PROTECTION AGENCY
Regional Administrators
John A. S. McGlennon
Region I
John F. Kennedy Federal Bldg
Room 2303
Boston, Mass. 02203
Phone: 614-223-7210
Connecticut, Maine, Mass.
New Hampshire, Rhode Island, Vermont
Gerald M. Hansler
Region II
26 Federal Plaza
Room 2525
New York, N. Y. 10007
Phone: 212-264-2525
New Jersey, New York, Puerto Rico
Virgin Islands
Edward W. Furia, Jr.
Region III
Curtis Building
6th and Walnut Streets
Philadelphia, Pennsylvania 19106
Phone: 215-597-4506
Delaware, District of Columbia, Maryland
Pennsylvania, Virginia, W. Virginia
Jack E. Ravan
Region IV
Suite 300
1421 Peachtree Street
Atlanta, Georgia 30309
Phone: 404-526-5727
Alabama, Florida, Georgia, Mississippi
Kentucky, N. Carolina, 5. Carolina
Tennessee
Francis T. Mayo
Region V
1 North Wacker Drive
Chicago, Illinois 60606
Phone: 312-353-5250
Illinois, Indiana, Minnesota, Michigan
Ohio, Wisconsin
Arthur W. Busch
Region VI
1600 Patterson St.
Suite 1100
Dallas, Texas 75201
Phone: 214-749-1962
Arkansas, Louisiana, N. Mexico,
Oklahoma, Texas
Jerome H. Svore
Region VII
1735 Baltimore Ave.
Kansas City, Missouri 64108
Phone: 816-374-5493
Iowa, Kansas, Missouri,
Nebraska
John Green
Region VIII
1860 Lincoln Street
Denver, Colorado 80203
Phone: 303-837-3895
Colorado, Montana, N. Dakota,
South Dakota, Utah, Wyoming
Paul DeFalco, Jr.
Region IX
100 California Street
San Francisco, California 94111
Phone: 415-556-2320
Arizona, California, Hawaii
Nevada, Guam, American Samoa
James L. Agee
Region X
1200 6th Avenue
Seattle, Washington 98101
Phone: 206-442-1200
Washington, Oregon, Idaho
Alaska
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APPENDIX III
EBCDIC Keyboard (Port Numb* \\tmi)
MAR
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torrespondence Keyboard (Part Numbar 1169703)
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1 Figure 1. IBM 2741 Communication Terminal Keyboard!
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• 10 TSO Terminal* (R*t*a» 20.1)
I ATtt.
OS
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IF YOU GIVE THIS "AWAL TO A.'IOTHER INOIVIDUAL, PLTASE FILL OUT TME
FOLLO'.'INfi:
.^PDRESS OF
HEW OI/NER
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THIS IS TO ALLO'J US TO KEEP A CURRENT LI^T OF MM'JAL OWNERS.
I'./E 'JILL BE PERIODICALLY SEND I, T. niJT REPLACfT.'.TS A.'ii) AD
TO THE 'WIIIAL.
* MAIL THIS FORM TO: NATIONAL Air? DATA T>A.'ICM
1411 '-JEST CilAPEL HILL ST
OUnM/VI, .'^"TH C^OLr.'A 27701
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SAROAO ACCESS
IF YOU GIVE THIS MANUAL TO ANOTHER
FOLLO'lINfi:
JWMT
wro
MAWAL
MIVIOUAL, PLEASE FILL OUT THE
ADDRESS OF
NEW OWNER
THIS IS TO ALLO'.J US TO KEEP A CURRENT LIST OF MANUAL OWNERS.
'JE '//ILL BE PERIODICALLY SENDING OUT REPLACEMENTS AND ADDITP.'IS
TO THE MANUAL.
MAIL THIS FORM TO:
NATIONAL AIR DATA BRANCH
EPA
411 !-/EST CHAPEL HILL STPEET
DUnHA!1, NORTH CAROLINA 27701
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SUBJECT:
FROM:
UNITED .STATES Ef-.'VincVvWEMTAL JT.OTF.CTION AGENCY
Office of Air Quality Planning end Standards
Research Triangle Park, North Carolina 27711
SAROAD Terminal Users Manual Update //I DATE:
TO: TSO Users
1
Please make the following changes in the SAROAD Terminal
Users Manual: . . - • ' ..
INSERT PAGES: 49J - 49.1.2 DELETE PAGES: 75,76,77
70.1 --.70.1.8
70.2 - 70.2.10 - '•"•
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Gerald J. Men Is
Chief
t-'C*. td l'!?.'!t'.'""J.'"-!! L O'j','!. I'.'f!
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nPA form U?"-<; (JVv. 6-72)
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ft 00, SSPCP • • . Dett: HOV. .21,
Street: tow Sulfur Coal Shortages and Compliance Schedules
**; • Directors, A1r and Water Programs Divisions
Regions I-X
On November 3, 1972, the Administrator sent a memorandum (copy
attached)- to Regional Administrators to reiterate EPA policy and
priorities relative to SIP revisions and compliance schedules required
to reduce the projected 1975-77 low sulfur coal deficit.
The elimination of this deficit in a manner compatible with the
objectives of the Clean Air Act is of primary concern. Ultimately,
•this will require revisions to SIP's to extend the date of compliance
for many coal-burning power plants in Priority II and III regions.
State agencies, of course, play the major role in solving this problem.
So that we may assess progress and keep several headquarters groups
Informed, we would appreciate periodic reports from each Region on each
State with low sulfur fuel problems relative to efforts to reduce the
short-term need for low sulfur coal. As appropriate, these reports
Should include information on the following:
1. Current estimate of the low sulfur fuel deficit and discussion
of any special problems.
2. Attitude of the State agencies toward the problem and toward
wi!Tic cX<,Ci"i jlGi'iS.
3. Current proposed variances, hearings scheduled and other action
. ' • underway by the States that could lead to reduction in short-term demand
for low sulfur fuels.
4. Requirements for support from this office.
These can be short, memo reports and are for internal use only.
I would like a first report from all regions by December 4. Subsequent
reports need be submitted only for States where the problem is acuta.
I will request additional reports when and as needed.
B. J. Steigerwald
Director
Stationary Source Pollution
Control Programs.
Enclosure
cc: Robert Sansom
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cc: W. Megonnsll
J. Padgett
. ; P. Blerbaum
M. Storlazzi, Region I
C. Simon, Region II
S, Wassersug, Region III
T. G1bbs, Region IV
V. Yamada, Region V
Dean Mathe\vs, Region VI
D. Durst, Region VII
• N. Huey; Region VIII .
C. Calkins, Region IX
G. Young, Region X
>*
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2 7 DEC 1972
Procedures for Using EPA/OMD Approved Questionnaire {OMB
Nr. 158-R75) to Acquire Data from Individual Sources
Mr. William Megonnell
Stationary Source Enforcement Division
Early this year the attached questionnaire was approved by OMU for
use by EPA In acquiring emissions-related Information directly from
facilities discharging air pollutants Into the atmosphere. Originally,
It was Intended that the questlonnlare would only be enployed by DAMP
personnel, however, we are now receiving numerous requests from EPA
Regional Offices and DSSE personnel for questionnaires to acquire
emissions-related data for sources now being constructed. Moreover, we
expect an Increasing use of this questionnaire as various groups within
EPA require source data to carry cut their responsibilities In monitoring
and evaluating pollution control activities and progress.
Due to the potential political coroplications that could arise from
needlessly contacting private sources for Information, It 1s nandatory
that duplicate usage of these questionnaires be strictly avoided and
that all Information received be routinely Incorporated Into the
National Emissions Data Bank (HEOB). To Insure this, the National Air
Data Branch (NADB) 1s managing distribution of the questionnaires.
Strict control procedures are necessary to prevent unauthorized use of
these questionnaires until EPA personnel are well aware of the potential
political hazards. A list of those persons authorized to receive
Questionnaires 1s now being constructed by f!ADQ. Please advise NADU
(John Bosch: FTS 919-688-8491} of the name of one DSSE representative
authorized to order and receive questionnaires. The two NCDS/SAROAD
representatives 1n each EPA Regional Office will also be Included on
this list, together with the emission Inventory contact in each
Regional Office.,
Administrative rules for using the questionnaires to solicit data
directly from sources are specified in the attachment. These procedures
shall be followed by all persons employing the questionnaire for data
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acquisition. It must be emphasized that authorization for requiring I
sources to complete these questionnaires Is needed In each Instance
and Is the sole responsibility of those persons Initiating the data-
gathering program*
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Robert E. Nellgan
Director •
Monitoring and Data •
Analysis Division
Enclosures
|
cct •
John A.S. McGlennon, Region I •
Gerald M. ilansler, Region II
Edward W. Furl a, Jr., Region III •
Jack E, Ravan, Region IV |
Francis T. Mayo, Region V
Arthur W. Busch, Region VI m
Jerone H. Svore, Region VII •
John A. Green, Region VIII *
Paul DeFalco, Jr., Region IX
James L. Agee, Region X •
Ken Berry, SIB •
EIU:JBosch:fhirm 647:Mu:ext
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GUIDELINE SERIES
OAQPS NO. 1.2-001
January 30, 1973
CRITERIA FOR REVIEW OF TRANSPORTATION
CONTROL MEASURES
US. ENVIRONMENTAL PROTECTION AGENCY
Office of Air Quality Planning and Standards
Research Triangle Park, North Carolina
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ENVIRONMENTAL PROTECTION AGENCY
Office of Air and Water Programs
Research Triangle Park, North Carolina 27711
. ' ** Jan. 30,1973
Subject: Criteria for Review of Transportation Control Measures
To. .
All Regional Air & Water Program Directors
The purpose of this memorandum is to provide criteria to assist
the Regions in the review and approval of State Transportation Control
Measures. The overall philosophy for development of an "approvable"
plan is presented and important elements that should be included
in a good plan are discussed. It is intended that these criteria serve
both as an overall guide and a check list of the content required in
an "approvable" plan. The limits of "reasonableness" that can be
accepted are reviewed, particularly with respect to reductions claimed
for various transportation control strategies.
General
The transportation control measures must meet the requirements of
the Clean Air Act and existing EPA regulations. The Transportation
Control Measures "Guidelines" now published as notice of proposed rule
making (FR 1464, January 12, 1973) specifically apply to this portion
of the State Implementation Plan. The Act and EPA policy make it very
clear that these are, above all, to be State plans and States are to
be given maximum flexibility to meet the standards in whatever way is
optimum for them. Our role is to see that State plans have a reasonable
chance of meeting the standard and that they are generally enforceable.
In an area as new and qualitative as transportation controls this
gives us significant freedom in plan approval. It should be remembered
that where we disapprove a plan, we must propose an EPA plan.
Copies of the recently proposed transportation control plan prepared
by Region IX for the Los Angeles Metropolitan Intrastate Region, pre-
sented by the administrator January 15, 1973, have been distributed to
all Regions. It provides an example of an extremely severe plan, necessary
under the circumstances to comply with the Court Order, the Clean Air Act
and meet the National ambient air quality standards. It is not expected
any other region will require such extensive control measures. However,
there~are several considerations in the Los Angeles plan that are equally
relevant to less severe control measures. They are discussed below.
Control Strategies' Emission Reductions
It can be expected that States will have various percentage reductions
claimed for Inspection, Maintenance and Retrofit of motor vehicles.
Appendix N to the Transportation Control Measures "Guidelines" contains
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•".ithor specif i,: vrK \s '.cr t>.e'
on >-;jther limited tests. They
for current planning purpose ar
of :,ny states rtrateou>r. ^.:i;
transit system: , i nip rove ' ,, --r".
fviyn not been cv.c. 'on^d - -•.- f .'
some guidance as In r>n •• •;.,. ]'-
the "Six Cities" ^eporl '• '<-•
*TT'Crt, Th-°rr ' '"•O',1!'1 '
- -.-.-«- s s me nt of r:--. ;,<:
Severe .-trflt-/: ^t. •-",";•
resfrici ;-m , - ..- , • •--.- . • •
should be ooi .;•;.: c.;-" :-; '. - ; .
ospecidl ly aor~v -•.•'£;•.
transportal/l cr; .'la;:'^ ur i. ( '
Although it r!;-'-^ ;;e ^a:,:. .•
gasoline r^t~ ;-">- " ., plans ^:'
more c-esil.j' '• '••_. c.nted r.,f.-:
vnj' sc^/e ti'f- !-or-!cm wi'/io
th^t : rovicit-j fi,-- letter ~, ;s.;
c''nir.,:p i/-, tf, •-' ' I'cductior-"
..r :',,-'• •-• I- ..; use of i';'
Thr pro:\;/ v:-i.n of the station.-, ••
standa1"-. .•'(,', a-Kj- , it has bren riot,-
'.on;?' ', v '"'• , • io '-•".•''
Tf.u
if very
in the r/"
enn ss
measure • ' - •. t/ ;
adequate";/ ; • "in
in some r-. • t., . . •> • v •• \
rather tiun ti,_c 1l',t.c."'-
in the value.v >r c- '•" :-'.
quirement fc* ..'.. . •
are otder •'^'•'\ i •• • • •,
be a prop-" • :: • •-. - ' <
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The approach for maintaining surveillance of the air quality and
transportation data togetiier with procedures for alternative action, if
needed, should be included as required in the regulations.
Int e r m i 11ant C o n t r ol__Measmres
The initial drafts of the transportation "Guidelines" included as
a control measure motor vehicle operation restrictions such as those
contained in the abatement strategies earn-; ion reduction plans. Hov;ever,
it was considered that problems in enforcenent and adequate forecasting
would mitigate against the feasibility of such strategies. Nevertheless,
as noted in the Proposed Metropolitan Los Angeles Intrastate plan, inter-
mittant controls were discussed which prohibit the use of all but certain
classes of vehicles on cJciy-> when the ambient air quality was expected to
be violated. Although the technical and legal feasibility of such measures
is still uncertain, they may be the most "reasonable" alternative to more
severe strategies applied year around or continously on a seasonal basis.
It is expected, according to some meteorologists, that weather forecasts
based on improved satellite coverage will improve their accuracy, but any
accurate air quality predictions further in advance than 24 hours seem
years^ away. This is particularly true of oxidant concentrations.
Data Requirements
The data thdt -,ubc t.uitiates the assu./pf inns, Calculations , and con-
clusions reijnrciir,; contvo1 measure strategics. Lfiouid be consistent with
the intent of Appendix M to the transportation control "Guidelines".
Since these data art. v :ainr><-j o:, an on call basis, there is some measure
of judgment involved as to whether they are convincing evidence of the
validity of the control measures. A good index of validity would be
their potential suitability as a form for evidence in the event of a
possible lawsuit Arihr reive '.••• Appendix M will preclude "holes" in the
data. However, to be acteutab le, the data does not need to be in the
exact format called for in the guidelines,
Resources & ScheduIes
Resources to be made available to monitor, enforce and accomplish
the mechanical aspect:, of the strategies should be well defined.
Strategies that require massive equipment purchases such as busses or
people movers """Should be capable of achievement in the context that
other areas of the country also will be expanding mass transit and re-
quiring additional equipment. Since EPA cannot promulgate substitute
federal regulations if State resources are not adequate, this portion of
a plan may require negotiation with the State. Generally we must accept
promises that the Statf intends to try for such resources. Schedules
for accomplishing the strategies should be presented and be reasonably
possible of achievement.
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Enforcement
Strategies should be enforceable at the state or local level. Many
options will not bo in the form of regulations that arc directly enforce-
able such as car pools, 'and mass transit. Much judgment will be needed
and it should be remembered that each plan is unique and there may be a
valid basis in many plans for giving credit for these controls.
If strategies are in AQCR's that involve more than one state, it
should be explained how the reductions are apportioned and how the
strategies can be enforced. This is particularly important where large
commuter traffic originates in one state and travels to the business
district of another.
Strategies that involve federal jurisdictions, such as interstate
airlines, should have an explanation as to how the restrictions or pre-
dicted emission reduction will be enforced and what other agencies must
approve the proposals (i.e. FAA).
The Office of Enforcement and General Counsel (OEGC) will review all
plans for legality and enforceability and provide you with their comments.
They will also be available for guidance on legal and enforcement questions
on an individual item basis.
Technical Assistance
In addition to the BOA Contract data previously noted (six cities,
fourteen cities and Washington, D.C.), an additional technical assistance
task order is being prepared to provide EPA with an evaluation of the
aggregate impact of the State plans. Two reports will be prepared:
one dealing with the social and economic impact of the transportation
control strategies, due in March 1973, and the other describing the
general and specific features of the various plans. The later report,
due in April 1973, will be useful in the preparation of the preamble to
the Federal Register Publication of approval/disapproval notices con-
cerning the states' Transportation Control Measures.
It can be expected that questions will arise which are not addressed
in these "Guidelines". We plan to call a meeting of Regional Transporta-
tion Control representatives in late February to exchange information
and answer quest'ions you may have. In the interim, please call Dr.
Ron Venezfa, Fred'Winkler, or Don Armstrong, Land Use Planning Branch,
(919) 688-8291, for clarification of any questions or 'discussion of
specific local problems.
Evaluation Report
Based on past experience we can expect many lawsuits on our decision
on these transportation control plans. Therefore, it becomes important
that a comprehensive evaluation report be prepared on each plan showing
clearly the basis for my significant decision made.
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Jn general, EPA does not wish to promulgate regulations unless it
is absolutely necessary. However, overly optimistic plans that would bo
approved now could lead to obvious problems in a few years. Thus the
Regions should maintain close liaison with the states to assure that the
transportation control plans, even with some sections requiring more
definitive data later, are "approvable" in the period between now and
June 15, 1973.
Where it is obvious that EPA must promulgate regulations,
cognizant Regions should make early preparations for the draft of
the preamble, regulations and briefing memorandum similar to that
prepared by Region IX for the Metropolitan Los Angeles Intrastate Region,
According to the Clean Air Act, such regulations must be promulgated
by August 15, 1973. However, the approval cycle is such that drafts of
these plans must be submitted by about April 27, 1973 to allow for the
proposal, hearings, interagency review and incorporation of comments.
We will be sending you soon a more detailed schedule and flow chart for
plan review and approval.
. Steigerwald
Director
Office of Air Quality
Planning and Standards
cc: Transportation representatives
Reviewers
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^l^^^^APTD.,5691
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I fl FINAL REPORT
;| SULFUR OXIDE CONTROL TECHNOLOGY
|| ASSESSMENT PANEL
(SOCTAP)
ON
i |:> PROJECTED UTILIZATION
11* *
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APTD-1569 |
FINAL REPORT .
SULFUR OXIDE .
CONTROL TECHNOLOGY *
ASSESSMENT PANEL I
(SOCTAP) .
ON •
PROJECTED UTILIZATION I
OF STACK GAS CLEANING SYSTEMS .
BY STEAM-ELECTRIC PLANTS *
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Submitted
to the
FEDERAL INTERAGENCY COMMITTEE
EVALUATION OF STATE AIR IMPLEMENTATION PLANS
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by I
Sulfur Oxide Control Technology
Assessment Panel
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April IS, 1973
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TABLE OF CONTENTS
I. INTRODUCTION i
II. SUMMARY AND RECOMMENDATIONS 1
A. Summary 1
1. Technological Status 1
2. Performance 3
3. Cost 4
4. Associated Environmental Factors 5
5. Institutional Barriers 6
6. Forecasting of Utilization of
Flue Gas Desulfurization Systems 7
B. Recommendations. , . 9
III. DESCRIPTION AND TECHNOLOGY STATUS OF
FLUE GAS DESULFURIZATION SYSTEMS 13
A. Wet Lime/Limestone Systems 13
B. Magnesium Oxide Scrubbing 22
C. Catalytic Oxidation (Cat-Ox) 25
D. Wellman-Lord Process (Sodium Base
Scrubbing with Regeneration) , 30
E. Double Alkali Systems 33
F. Dry Limestone Injection. 36
IV. PERFORMANCE AND COST COMPARISONS OF
FLUE GAS DESULFURIZATION SYSTEMS 39
A. General Considerations 39
B. New Versus Retrofit Installations 39
C. Throwaway Versus Saleable Product Systems 40
1. Throwaway Processes 40
2. Recovery Systems 41
D. Development 01 Comparable Cost Projections.... 43
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E. Cost and Performance Comparisons 44
1. Low Sulfur Fuel 46
2. Dry Limestone Injection 46
3. Wet Lime/Limestone Scrubbing 46
4. Magnesium Oxide Scrubbing 47
5. Monsanto Catalytic Oxidation 47
6. Wellman-Lord 47
7. Double Alkali Process 47
F. Specific Cost Examples 47
V. ASSOCIATED ENVIRONMENTAL FACTORS 52
A. Quantification of the Problem 52
B. Throwaway Product Disposal 55
C. Sale of Sulfur Products 56
VI. INSTITUTIONAL BARRIERS TO APPLICATION
OF SULFUR OXIDE CONTROL SYSTEMS 59
A. Institutional Barriers in the Electric
Utility Industry 59
1. Reserve Generating Capacity
and Scheduling of Retrofits 60
2. Lack of Familiarity with Chemical Processing
Technology within the Electric Power
Industry 66
3. Competing Fuel Supply/Environmental
Protection Strategies 67
B. Institutional Barriers in the Control
Systems Industry 69
1. Utility Engineers 70
2. Consulting Engineers 70
3. Scrubber Vendors 70
VII. FORECASTING SULFUR OXIDE CONTROL TECHNOLOGY 75
A. Recent Trends in Orders for Flue
Gas Desulfurization Systems 75
B. Forecasting Applications of Flue Gas
Desulfurization Systems 77
APPENDIX 87
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I . INTRODUCTION
This is the final report* of tho Fedora 1 interagency
committee established to assess the potential for utiliza-
tion of flue gas desulfurization (Snx control) systems by
steam electric plants,
Previous studies have indicated that the implementation
of State Air Implementation Plan (SIP) regulations limiting
the sulfur content of fossil fuel can result in a demand for
low sulfur coal that greatly exceeds the supply. Such studies
have indicated a possible deficit in low sulfur coal in 1975
of as much as 250 million tons. This is equivalent to
100,000 megawatts, expressed as steam electric plant capacity.
Flue gas desulfurization can reduce this shortage by removing
sulfur oxides from th*1 stack gas an lieu of requiring
substitution of low .•r.nlrar t u>l , However, it is currently
estimated that less Midti 1.5,000 megawatts of SOX control would
be available by 19/t;
Stack gas cleaning to reduce sulfur oxides, both in the
near and intermediate future, offers potential as an important
technological option to fuel switching. Recognition of this
by the Federal Interagency Committee responsible for evalua-
tion of SIP's resulted in the formation in May 1972 of an
interagency task force to conduct a more detailed evaluation
of SOX control systems. This group, designated the Sulfur
Oxide Control Technology Assessment Panel (SOCTAP), had as
primary objectives (1) to attempt to quantify the availability
of stack gas cleaning bysxcn-.s to steam, electric utilities in
1975, 1977, and beyond, and (2) to identify possible actions
that might serve to maximize the utilisation of these systems,
if desirable. It is important to note that this study is
limited to stack gas cleaning. It does not attempt to assess
other alternatives to this technology, nor to assess the
relative merits of competing technologies. The task force
consisted of the following members:
R. Berkowitz Knvironmental Protection Agency
S. Gage Office of Science & Technology/
Council on Environmental Quality
B. Haffnei Department of Commerce
*This report rep"Fe~sents the view of the individual SOCTAP
members and not necessarily those of their respective agencies
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R. Jimeson Federal Power Commission
J. Padgett Environmental Protection •'Vjency
F. PrincioLta Environmental Protection Agency
E. Shykind Department; of f\.n>T-iei ct-
We recognized eariy in th^ .;•* u iy M;t. a compi enensive
analysis of every aapt-ct of -;i;., 1 lets :md met with representatives
of the Eciison Elect! , r institvtc ind the National Construc-
tors Association. - -i industry ^ntacts .led ?•> i.o conclude
that information on SOX technology in .T-ipau vis essential
to our study. We t'orefore sent two of our members to
Japan for a first-bund assess*:;*, nc. of this technology.
A preliminary draft of thf tinal report was submitted
for review and comment on November 16, 1972, to the Federal
Interagency Committee for Eva.luat.ion of State ." . Implemen-
tation Plans. All information and findings preae.nt.ed are
as of the ^^ o^^thaV^draft reportT Written comments were
received from the Departments of Interior, Con-u-neroe, and
Agriculture, Atomic Energy Cor^u i ^;- ion, Federal Power Commis-
sion, and' che Offi:,-£ c.i ^n;ergt.:ic/ Preparedness. These
comments were rarer wily reviewed cy task force members and
the majority of ^osiments considered within the Fcope of the
SOCTAP charter were Accepted and integrated into the final
report. The rr^j^, ^ .< -rpt.ionj \':\-*:- Uiose by the ;. i'C. The
FPC task f;ir-v rr.r." .;<•-, ind FPC ^oviewers veie nij h trox'e
pessimistic chan the other task force members -,.. .-tiiur
Federal Agencies relative? to the technological -.-status of
stack gas cleanivi. We were :>;;-c .j].ie to reconc-: u- their
viewpoint witn :.hai. •.)!' other r.isk lotce- member fa
Our conclus io-r.o =u:.i t occr'i >t nf.'a " ions are ^ros-rnted in
Section II. Discussions of Sux cor>trol technology, cost
and performance of competing systems, environmental factors,
institutional fact
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II. SUMMARY AND RECOMMENDATIONS
A. Summary
Many factors must be considered in estimating the
utilization of stack gas cleaning systems by the utility
industry. These include technology, cost, adverse environ-
mental effects, institutional barriers, and the ability of
the suppliers to produce and install all of the systems
demanded. These factors interact and combine to determine
both the decision to buy, which must be made by the individual
utility, and the aggregate supply constraints and secondary
impacts which may limit the utilization. Uncertainties in
the assessment of these factors have been a major barrier to
widespread application of stack gas cleaning systems. We
have not made an exhaustive assessment of each factor, but
we believe each has been examined sufficiently to support
the conclusions and recommendations presented. Detailed
findings are discussed in Chapters III-VII. Our major find-
ings are given in the following sections.
1. Technological Status
We have examined the status of stack gas cleaning
technology in the United States and Japan and have concluded
that sulfur dioxide removal from stack gases is technologi-
cally feasible in commercial-sized installations. We have
concluded that the technological feasibility should not now
be considered a decisive element in the utilization of these
systems and that a large fraction of the nation's coal-fired
steam electric plants can ultimately be fitted with commer-
cially available stack gas cleaning systems.
The reliability of currently available systems has been
the subject of some question. We concur that SOX control
systems must exhibit the high degree of reliability required
by the utility industry. We believe that the required reli-
ability will be achieved with the early resolution of a
number of applications engineering problems related to specific
hardware components and system design parameters. Solutions
to each of these problems have been developed and demonstrated
at one or another location. We do recognize, though, that
solutions reached at one installation may not be entirely
transferable to all other installations.
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In view of the fact that a number of large scale
plants scheduled for operation in the U.S. in the near
future will provide additional engineering effort to
solve these problems, we believe that an additional
eighteen months operating experience (or by 1974) should
effectively remove engineering barriers to the application
of stack gas cleaning to many facilities.
Flue gas desulfurization systems can be classified
into two general categories: (a) throwaway product systems
where the sulfur product is disposed of as waste or (b)
saleable product systems where the sulfur product (such
as sulfuric acid) is marketed. The state of the art of
SOX desulfurization technology has advanced rapidly over
the last year. Two plants with throwaway products -
Chemico's calcium hydroxide scrubbing system in Japan and
Babcock and Wilcox's. limestone scrubbing system on a
Commonwealth Edison boiler - and two plants with saleable
products - Chemico's regenerative magnesium oxide process
on a Boston Edison plant and Wellman Lord/MKK regenerative
sodium sulfite process on a boiler in Japan - are considered
particularly significant.
To date, the most successful operation of a throwaway
system has been the Chemico calcium hydroxide scrubber
process which has operated on the coal-fired boiler at
the Mitsui aluminum plant in Japan since March 29, 1972,
without any significant down-time; availability of this
unit has been effectively 100 percent since start-up.
Both sulfur dioxide and particulate removal efficiencies
have been quite high and there is an important similarity
between this application and typical U.S. requirements.
Babcock and Wilcox's limestone scrubbing unit on Common-
wealth Edison's Will County plant near Chicago, since its
start-up in February 1972, has indicated reasonably high
SO2 removal efficiencies and the promise of reliable opera-
tion in the near future. The major problem afflicting the
throwaway processes is developing techniques for disposing
of sludge materials in an ecologically satisfactory manner
without excessive costs. It is considered important that
acceptable disposal techniques be expeditiously developed.
Without these techniques, sludge disposal will remain a
serious constraint to the utilization of throwaway systems
at many power plant locations.
Of the regenerable systems, the Wellman Lord regenerable
sodium sulfite scrubbing process has operated most reliably
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to date. A unit treating flue gas at Japan Synthetic
Rubber's Chiba Plant has shown reliable and efficient
operation since June 1971, producing high quality sulfuric
acid. The main disadvantage of this system is the require-
ment for discarding a sodium sulfate bleed stream which is
ecologically and economically undesirable. However, there
are indications that bleed rates can be substantially
decreased so that less than five percent of incoming flue gas
sulfur need be discarded, compared to the present ten percent.
Chemico's magnesium oxide system at Boston Edison's
Mystic Station started up in April 1972, and has operated
intermittently since then due to mechanical difficulties.
However, sulfur dioxide removal efficiencies have been in
excess of 90% with no apparent scrubber problems. Preliminary
experience with the critical regeneration system has been
promising. There appears to be a high probability for reliable
operation of this unit in the near future. Among the more
advanced processes, this process is somewhat unique in that no
major ecological problems have been identified. However,
problems in marketing large quantities of sulfuric acid may
limit acceptability of saleable product systems to only a
fraction of the total potential flue gas desulfurization market.
2. Performance
When evaluating SO? removal efficiencies, it should be
noted that a removal efficiency of about 75% is needed to
meet the New Source Performance Standards with 3% sulfur
bituminous coal. Generally efficiencies of 85% are sufficient
to meet the sulfur dioxide emission limitations of most State
Implementation Plans.
As discussed above, a number of stack gas cleaning systems
are being tested and evaluated. At the Mitsui aluminum plant
near Omuta, Japan, the Chemico scrubbing unit has exhibited
reliable, essentially trouble-free operation, with removal
efficiencies of 80% to 90% since March 29, 1972. The Wellman-Lord
scrubbing unit, at the Japan Synthetic Rubber plant near Chiba,
has accumulated over 9000 hours of operation since June 1971
with a removal efficiency averaging about 90%.
The only U.S. plants that have yet achieved sufficient
operating experience to report long-term average removal
rates are the Combustion Engineering limestone injection/
wet scrubbing systems. These have exhibited average removal
rates in the range of 60% - 80%. However, performance results
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to date indicate that at the upper end of this range
these systems are more prone to chemical scaling and
other operating problems.
Short-term testing of the Babcock and Wilcox wet
limestone scrubber at Commonwealth Edison's Will County
plant and the Chemico wet magnesium oxide scrubber at
Boston Edison's Mystic plant have exhibited removal
efficiencies of 75-85% and 90%, respectively. It does
not appear that there are insurmountable chemistry
related problems at these higher removal efficiencies
for these two plants.
It should be noted that many stack gas cleaning
processes, particularly lime/limestone wet scrubber
systems, are also capable of efficient particulate
removal. In fact, most planned and installed stack gas
cleaning systems are designed to meet both SC>2 and
particulate removal specifications.
3. Cost
The incremental capital costs for including a stack
gas scrubbing installation in the construction of new
generating plants ranges from a low of $30 to a high of
$50 per kilowatt capacity. This would include particulate
control equipment, where required. The average incremental
cost for new generating plants is expected to be around
$40/kw.
Capital costs for retrofit installations to existing
generating plants in most cases is expected to be in the
$45 to $65/kw range. For some retrofitted plants, installa-
tion costs have been estimated as high as $80/kw or more.
However, the practical limiting cost for retrofitting is
fixed by economic considerations at each particular plant.
Based on the forecasts of the amount of stack gas
cleaning that might possibly be installed under the assump-
tions used in this study, the total investment between 1975
and 1980 for stack gas cleaning would be $8.2 billion in
addition to $78 billion of new generating capacity invest-
ment. This represents almost 10% of the total future capital
requirements for the industry.
The annual costs estimated for stack gas cleaning
range from 1.1 to 3.0 mills per kilowatt-hour, with a mean
of about 2.0 mills/kw-hr. The average national consumer
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cost for power is about 17.8 mills/kw-hr. (1971, Edison
Electric Statistical Yearbook). Assuming stack gas clean-
ing costs are passed on, consumer cost for electricity
could increase by as much as 17%.
Annual costs are difficult to generalize because of the
present lack of sufficient operating data on large scale
installations, the variability resulting from different
process type, specific installation cost factors, and varia-
tion in cost accounting procedures. In the figures for
annual costs cited in this report, the fixed charge portion
includes depreciation of capital equipment over 15 years on
a straight line basis. Operating costs include a charge for
parasitic power consumption.
4. Associated Environmental Factors
The disposal of waste products from stack gas cleaning
systems still remains a major problem with serious environ-
mental consequences. Based on a potential installation of
100,000 MW of flue gas desulfurization, calculations indicate
that 48 million tons per year of throwaway sludge would be
produced. This corresponds to a potential land requirement
of 160 square miles assuming a 20-year storage requirement
and ponding to a 10-foot depth. This should be compared to
a 50 square mile requirement for flyash disposal under the
same assumptions. In some rural plants, sludge materials
can be disposed of in a pond on the power plant site. In
urban applications the sludge can be transported for landfill,
but the transportation costs may be prohibitive in certain
situations. Although it is feasible to minimize potential
water pollution and land deterioration problems by closing
the scrubber liquor loop and by careful engineering of disposal
sites, it is essential that development and demonstration
efforts be accelerated in this area to obtain satisfactory
solutions to this problem before its full impact is felt in
the 1975-80 time period.
Due to the great difficulty of storing and marketing
large quantities of sulfuric acid under future supply/demand
constraints, it is estimated that only a relatively small
fraction of flue gas desulfurization systems will produce
saleable H2SO4. From an environmental viewpoint, the most
manageable sulfur product appears to be elemental sulfur,
since: (a) it can be economically stored for sale in
certain locations; (b) it would drastically reduce land
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requirements if treated as a throwaway product; and (c)
it is an insoluble and inert material with no apparent water
pollution potential. The major obstacles to use of elemental
sulfur producing control processes are the lack of demon-
strated technology and unfavorable economics, if treated
as a throwaway product.
5. Institutional Barriers
There are a number of institutional barriers in the
electric utility and control systems industries to the
accelerated application of SOX control systems. These
barriers can combine to delay the ordering, fabricating,
assembling, and placing into operation of SOX scrubbing systems.
Some of the most important are (a) the adequacy of the market
demand to encourage development of a supply industry; (b)
necessity to maintain adequate electrical reserve generation
margin; (c) lack of process chemistry expertise in the elec-
tric utility industry; and (d) fuel switching alternatives
where higher costs for low sulfur fuels can be passed through
to consumers by means of fuel adjustment clauses.
An important factor now restricting system installation is
the currently limited market demand for the SOX control sys-
tem. This lack of demand by the electric utilities and other
industries arises from a number of primary factors such as
lack of confidence in the ability of the vendors to perform
as promised, an anticipation that regulations may be altered
in the near future, potential difficulties in raising capital
and obtaining rate increases to cover expenses for pollution
abatement, and the lack of suitably trained personnel in the
industry to evaluate and operate these systems. With increased
demand pressure, scrubber systems probably could be constructed
at a hicfher rate than at present.
Elimination of these primary factors which are now limiting
market demand will require time to accomplish. Familiarity
with the technology is increasing but confidence in system
reliability depends critically on scrubber operating experience
during the next few months. A sudden surge of orders could
swamp the productive capacity of the control systems industry,
though, and scrubbers which might otherwise be brought on line
in 24-30 months may be delayed a year or more.
Nationally in the electric power industry, there is
certainly an upper limit to the generating capacity which
can be retrofitted each year because of the necessity to
maintain adequate reserve margins. While that quantity is
somewhat above present estimates of market demand or what
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the control system vendors can now supply, this factor may
preclude higher rates of installation. In particular,
there may be severe scheduling problems in retrofittinq
scrubbers in the middle central and middle southern parts
of the country where the large coal-fired utilities, already
under pressure because of delays in new generating equipment,
are concentrated.
There is little expertise in large-scale chemical process
technology within the electrical utility industry. Thus,
there may be serious operational problems once the scrubbers
are installed because of the lack of familiarity with the
operational details of the scrubbing system. The utilities
now depend almost completely on the control systems vendors
and engineering consultants for technical advice. However,
because of past experience, particularly with the dry lime-
stone injection/wet scrubbing systems, utilities are wary of
vendor claims.
There are several economic disincentives involved in
installing stack gas scrubbers. The utilities can meet the
SOX standards by converting coal-fired plants to low sulfur
oil or by securing low sulfur coal. Both of these options
have, in turn, broad implications for national economic and
environmental policies. Even with much higher costs for the
low sulfur fuels, many utilities are allowed to pass most of
these increased fuel costs directly and immediately on to
the consumer without regulatory commission action. On the
other hand, utilities must apply for rate increases to cover
the capital and operating expenses of the scrubbers.
In the construction industry, localized shortages of
pipefitters, boilermakers, and possibly other skilled workmen
may delay scrubber projects. If intense competition for
skilled metal-workers does develop because of construction
booms in refineries, waste treatment systems, etc., then it
is certain that scrubber installation schedules will be de-
layed, and installation costs will be escalated.
6. Forecasting of Utilization of Flue Gas
Desulfurization Systems
In the United States during the 1973-80 period, electric
utilities will probably continue the current pattern in
selecting wet scrubbing systems, with the majority of orders
probably for wet lime/limestone scrubbers producing a throw-
away sludge. There probably will be a limited number of orders
for regenerative processes using reagent liquors based on
magnesium, sodium, and other compounds.
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Forecasts based on SOCTAP estimates of the regulatory
enforcement pressures, utility demand, and supplier capa-
bilities indicate that as much as 20,000 MWe of generating
capacity could be equipped by SOx scrubbing systems by the
end of 1975 but more likely the capacity will be closer to
10,000 MWe. By the end of 1977 the equipped capacity may
be 48,000-80,000 MWe which would allow the use of high sul-
fur coal to supply 2§-40% of the utility heat required from
coal in that year. Again, realism dictates that the lower
end of the range would be the best guess because of the like-
lihood of near-term delays and the uncertainties in estimat-
ing the effect of interactions between the factors considered.
With steady growth in the control system industry based
on a firm market in the utility industry, at least 75% of the
coal-fired capacity conceivably could be equipped with stack
gas scrubbers by 1980. This could permit the utilization of
over 400 million tons of high sulfur coal in that year. Such
an estimate, however, does not take into account chemical coal
cleaning processes such as liquifaction and gasification
which may become available on a limited basis in the 1977-1980
timeframe.
Our forecast is based on the results of many discussions
with utilities, manufacturers, and others to attempt to identi-
fy and quantify those factors which might limit the utiliza-
tion of SOx control systems. These include consideration of
the technology, cost, environmental effects, factors affecting
utility demand, other institutional barriers, and the ability
of the industry to produce and install the systems.
Our estimates are the result of an intuitive and analyti-
cal blending of these factors. The concept of "choke point"
or limiting factor is an integral part of our assessment.
For example, if the technology is not available, a deluge of
orders by the utilities will not automatically result in
increased utilization. Given the technology and sufficient
orders, the "choke point" may be determined by considerations
such as financing, engineering design, scrubber production,
construction, or possibly the ability of the utilities to
phase in the operation of SOX control systems without risking
unduly low reserve margins. It is apparent also that the
choke point will change with time. Elimination of the con-
trolling 'thoke point? allows the utilization rate to increase
until a new factor is controlling. This new rate may or may
not represent a significant increase in utilization rate.
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An upper limit of 24,000 MWe and 80,000 MWe by the
end of 1975 and 1977, respectively, is forecast based on
the assumption that the "choke point!1 is supplier capability.
Orders for systems for 1975 must be placed within the next
6-9 months, with 24-30 months then required to brinq each
system on line. The lower limit, of 10,000 MWe and 48,000
MWe for 1975 and 1977, respectively, assumes the likeli-
hood of delays in excess of 6-9 months before utility
demand increases significantly. Thus, utility demand is
the initial "choke point." Factors affecting this demand
are many. The assumption that a combination of factors
and the resulting utility demand constitute the real
"choke point1 leads us to conclude that the lower estimates
are the more realistic.
B. Reconunendati.gns_
The momentum for utilization of stack gas cleaning
appears to be building and probably will continue at some
rate without the need for additional assistance from the
Federal government. We believe, however, that the rate of
utilization of these systems could be accelerated, if it
is deemed desirable, by implementing the following recom-
mendations. Consistent with the limited objectives of this
study, the recommendations are addressed only to stack gas
cleaning. This is not to imply, however, that alternatives
to stack gas cleaning are less desirable and should not be
encouraged.
1. A major factor which limits utility demand
appears to be a lack of up-to-date knowledge of
the status of SOX technology and other informa-
tion needed by the individual utility to decide
how to meet its local sulfur regulations and
how to plan a program to implement this decision.
We recommend the institution of an effective pro-
gram of SOX control technology transfer to be
carried out by one or more Federal agencies to
assist the utilities and industrial boiler opera-
tors in identifying potential technologies and
solving technical staffing problems associated
with the operation of the scrubbers. This
activity would cover not only information
dissemination on hardware but would address
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operations and manpower problems within the
utility/industry context. A possible model
might be the combination of a policy committee
under the Federal Council for Science and
Technology or the Council on Environmental Quality
and an operations office under EPA Control Systems
Division. This arrangement could go a long way
toward meeting the twin objectives of putting a
new face on the Federal government's attempts to
accelerate the application of SOX control techno-
logy while ensuring the required level of technical
expertise in the operational arm. It would also
have explicit responsibility for the dissemination
of information about foreign developments in SOX
control.
2. Accelerate R&D in critical areas of SOX
control technology. In particular, Federal R&D
efforts should be expanded to accelerate the
development of improved scrubber solid waste
management processes. It also is strongly recom-
mended that the Federal government continue
support of ongoing government sponsored programs
to develop SOX control processes. The need for
the development of advanced SOX control processes
is clearly recognized to expand the options avail-
able to industry and the Federal government, parti-
cularly processes with more environmentally accept-
able by-products. However, the committee was not
in unanimous agreement that programs for advanced
processes should be wholly or predominantly funded
by the Federal government.
3. Explore a variety of incentives to accelerate
the application of SOX control systems, and/or dis-
incentives for substitute or alternative pollution
control strategies. The following incentives and
disincentives might be considered:
(a) Modification of the fuel adjustment clause
provision now operable in many states to in-
hibit utilities from passing through to the
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consumers the high cost of low sulfur I iu-I
rather than installing SOx control systems
which would require public utility commission
action to increase the rate base. This
problem could be explored with the Nat ion.>1
Association of Regulatory Utility Commissions
(NARUC).
(b) Simplification of the procedures re-
quired by public utility commissions for
utility companies attempting to obtain rate
increases to cover the costs of pollution
abatement devices such as SOX scrubbers.
Removal of this disincentive is closely
coupled to changes in the fuel adjustment
clause and could also be explored with
NARUC.
(c) Institution of a grant-in-aid program
through EPA to assist in the purchase of SOX
control equipment. A variation of this
approach would be a low-interest loan program
in which a fraction of the loan would be for-
given when the scrubber system goes into
operation.
(d) Sulfur tax with a rebate clause so that
the utilities would pay a sulfur emission
charge until their scrubber goes into operation
and then taxes paid during the construction
and shakedown phase would be rebated. Al-
ternatively, a clause for suspension of the
tax during the period of construction and
shakedown phase could be considered.
(e) Residuals subsidy program under which a
base-level price would be established for
scrubber residuals such as sulfur, H2S04, and
CaSC>4 to encourage beneficiation of the scrubber
sludge to a potentially useful product, even
though that product may have to be stockpiled.
This could avoid premature commitment of large
areas of land to non-reclaimable sludge ponds.
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4. Encourage Labor and Commerce Departments to
determine national needs for skilled technical
manpower (boilermakers, pipefitters, etc.) for which
there may be intense competition among several
competing industries (SOX scrubbers, refineries,
etc.). Where potential shortages are indicated,
special programs to provide the manpower supply
and increase its productivity may be required.
5. Encourage interagency efforts to devise
policies (and propose legislation if necessary)
to provide special incentives for the use of low
sulfur fuel by small industrial boiler and area
sources. This would direct the low sulfur fuels
toward users for whom SOX control methods would
be prohibitively expensive. This would result
in a strategy which would influence fuel purchas-
ing patterns by inhibiting utilities and large
industries from tying up available low sulfur
fuel supplies by outbidding the small consumers
with long-term contracts.
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III. DESCRIPTION AND TECHNOLOGY STATUS OK
FLUE GAS DESULFURIZAT10N SYSTEMS
There are more than fifty SO2 flue gas desulfurizaLion
control processes, and their major variations. Of those,
only five are considered developed sufficiently to enable
reasonable estimation of expected performance and economics.
For the purposes of this discussion, four of these five
processes are considered sufficiently developed, with
acceptable S02 removal efficiencies, to potentially make a
significant contribution to the control of new or modified
power plants within the next five years. The dry limestone
injection process, although well characterized, has a
removal efficiency too low for most boiler control require-
ments .
The four processes which are considered sufficiently
developed to potentially desulfurize flue gas on a full-
scale commercial basis, within the next five years, are:
Wet lime/limestone scrubbing
Magnesium oxide scrubbing
Catalytic oxidation
Wet sodium-base scrubbing with regeneration (Wellman-
Lord Process)
An additional process, the double alkali process, is
also potentially important, and could be added to the above
list if process technology development is accelerated.
The following discussion describes and presents the
status of: wet lime/limestone systems, magnesium oxide
scrubbing, catalytic oxidation, the Wellman-Lord process,
double alkali, and dry limestone injection control processes.
A. Wet Lime/Limestone Systems
The great majority of full-size power plant desulfuriza-
tion systems in both the planning and operational phases
involve scrubbing with limestone or lime slurries. The
primary reasons for this are that these processes are more
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fully characterized than other first generation systems;
have relatively low capital and operating costs; and have
high potential removal efficiencies. However, along with
characterization comes familiarity with such process problems
as chemical scaling, erosion/corrosion, solid waste dis-
posal, and plume heating requirements.
Several methods have been developed for the use of
limestone and lime in a wet scrubbing process. The major
variations are schematically illustrated in Figure III-l.
In Method 1, Scrubber Addition of Limestone, the flue gas
is contacted with a slurry containing finely ground lime-
stone. The limestone is added directly to a portion of
scrubber effluent for recycle. Part of the scrubber dis-
charge goes to a settler (or a pond) where the solid product
is removed. Settler overflow can either be recycled as
shown or discharged to waste. The next method, Scrubber
Addition of Lime is similar to Method I except that the
limestone is first calcined to lime externally before
addition to the scrubber circuit; ordinarily lime is pur-
chased by the utility from lime suppliers. In the final
method, Boiler Injection, the limestone is calcined in the
boiler (as in the Dry Injection System) and carried to the
scrubber in the flue gas. Figure III-2 shows the Common-
wealth Edison Company's Will County Station - Unit No. 1.
This unit utilized limestone introduced in the scrubber
circuit and shows the major equipment items needed for a
typical full-size wet limestone installation.
In addition to being classified according to whether
lime or limestone is the reactant, the above processes are
further classified as cyclic or non-cyclic. Such a classi-
fication refers to whether the aqueous liquor loop is totally
recycled (cyclic operation) or totally purged (non-cyclic
operation) to a stream or reservoir, giving rise to possible
water pollution problems. In light of such potential water
pollution problems, the great majority of the full-size in-
stallations operate, or will operate, in a total or near-
total recycle mode. The ultimate disposition of the sludge
solids is generally in a large pond at the power plant site;
when land is not economically available, the sludge is
transported to the most economical surface disposition
area available.
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GAS TO STACK
STACK
GAS
SCRUBBER
CaCO,
PUMP
TANK
SETTLER
METHOD 1. SCRUBBER ADDITION OF LIMESTONE
CaS03+CaS04
TO WASTE
STACK ^
GAS W~
CaC03
CALCINER
GAS TO STACK
Ca(OH)2
SCRUBBER
CaO
PUMP
TANK
SETTLER
CaS03+CaS04
TO WASTE
METHOD 2. SCRUBBER ADDITION OF LIME
GAS TO STACK
CaC0
BOILER
CaO GAS
SCRUBBER
PUMP
TANK
SETTLER
METHOD 3. BOILER INJECTION
TO WASTE
Figure III-l. Major process variations for use of lime or limestone for
removal of S02 from stack gases.
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S
•H
•M
CO
X
o
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VI
•H
S
rt
0)
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The chemical reactions occurring in the above systems,
although seemingly simple, are neither well understood nor
universally agreed upon. The following chemical reactions
have been postulated for flue gas scrubbing with limestone
slurries and appear to be the most plausible on the basis
of experimental data available.
|S02(g)5± S02(aq)
SO^aq) + H05iHS05i.H +
|
Ca+4" +
|
CaCC>3 (s)^±CaCO3 (aq)
CaCC>3 (aq)^Ca++ + 003=
+ 1/2 • H20£CaS03'l/2 H2O(s)
C03= + H+ 5=St HC03-
H++ HC03"-±H2C03(aq)
fl The overall reaction is:
CaC03(s) + S02 (g) + 1/2 H20-*CaS03.l/2 H20(s) + C02 (g)
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There has been a considerable amount of bench model,
pilot plant, and prototype experimental activity in the
limestone wet scrubbing area. An extensive effort has been
expended on a variety of scrubber types, by a large number
of organizations, over the last 30 years. Over the last
several years, pilot plant effort has been, particularly
active and substantial advances have been made in wet lime-
stone technology. Scrubber types which have received the
most attention in recent years have been the venturi.
Turbulent Contact Absorber (TCA), Hydrofilter (flooded
marble bed), spray tower, and packed tower. Generally,
pilot plant results have indicated that under carefully
selected operating conditions, all of these scrubbers,
with the probable exception of the packed tower due to its
inherent plugging tendencies, can be operated with rela-
tively high SC>2 and particulate removal efficiencies
with acceptable reliability. Pilot plant testing has in-
dicated that, with relatively high liquid-to-gas ratios,
high solids content in the scrubber slurry, long residence
times in a delay tank following the scrubber, and a proper
choice of scrubber type, the desirable combination of good
removal efficiencies without excessive down-time can be
achieved.
For example, the results of both the Ontario-Hydro and
the Tennessee Valley Authority (TVA) pilot plant programs
indicate that good performance and reliability have been obtained
on a pilot-size scale. Ontario-Hydro was able to achieve
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SO removal efficiencies of 70-80 percent in its spray
tower, under reasonable operating conditions, with good
reliability; scaling or plugging was not a major problem.
TVA has been able to achieve high removal efficiencies foi
three scrubber systems: a venturi-rod (modified venturi)
spray tower, a three-stage TCA, and multi-grid tower. For'
the venturi-rod/spray unit, SCU removal efficiencies of
77 percent over a 354-hour test were achieved with only
20 hours of down-time. Particulate removal efficiency was
measured at from 98.9 percent to 99.3 percent. For the
TCA unit, S02 removal efficiencies of up to 92 percent
and a particulate removal efficiency of 98.3 percent have
been measured during a 172-hour test. Although the unit
showed no scaling or plugging tendencies, erosion of the
balls, grids, and nozzles was excessive; design modifications
are being considered to minimize this problem. For the
multi-grid scrubber, a 270-hour test yielded an S02 removal
efficiency of 85 percent with no scaling or plugging.
Particulate removal was about 98.9 percent. TVA reports
that demister operation has been troublesome, however, with
some solids buildup (CaSC>4 • 2H20) .
At the present time, at least six full-size scrubber
facilities have been constructed and have generated varying
amounts of operating data. An additional unit, the London
Power Fullham Plant, was constructed and tested in the late
1930's. This unit is considered the first commercial
application of wet limestone scrubbing of power plant flue
gas. It was operated from 1936 to 1939, yielding very high
S0_ and particulate removals, without substantial scaling
or plugging problems. In fact, many of the techniques used
to control scaling and plugging on this- unit have been
utilized successfully in recent years. However, the
facility was afflicted with corrosion and erosion problems
which led to considerable down-time and high maintenance
costs. The unit was taken off the line during the early
stages of World War II, when the stack plumes were considered
markers for enemy airmen. Before shutdown, a plant modifi-
cation decreased the removal efficiency to 90 percent, but
gave some promise of being able to remain in service for
much longer periods without repair. This unit is considered
to have been the first to indicate the feasibility of wet
limestone scrubbing for power plants on a commercial basis.
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In Japan, 156 MWe power plant of the Mitsui Aluminum
Company has been retrofitted with two dual-stage venturi
scrubber systems, each capable of handling 75 percent of
the full-load gas flow. The system has exhibited reliable,
trouble-free operation since being put on stream on March
29, 1972. The plant is presently burning 2 percent sulfur
coal and achieving 80 - 85 percent SC>2 removal from the
flue gas using carbide sludge (essentially calcium hydroxide)
as the alkaline absorbent. The unit passed performance
guarantee tests within four weeks of start-up which required
90 percent SC>2 removal and 90 percent flyash removal at a
specified gas flow rate. Presently, the unit is operating
at less stringent conditions, but with the aim of meeting
the Japanese regulatory codes. It should be noted that,
although the system is designed for total liquor recycle,
it did not operate in a totally closed-loop mode for at
least a portion of its operating lifetime. Appendix A fur-
ther describes this important unit which was recently visited
by SOCTAP members.
The AB Bahco system, which utilizes a two-stage inspi-
rating scrubber with lime as the reactant, is considered an
important operational scrubber facility despite its small
size (the equivalent of 25 MWe for the three units). The
units service three oil-fired boilers in a hospital
in Stockholm, Sweden. This system, considered among the
more successful of the wet lime scrubbers in operation, has
been routinely operated at 95-98% removal efficiencies.
After three months of service, the scrubber must be shutdown
and hard sulfate scale removed from the demister section.
The demisters have not been equipped with washing sprays,
a possible solution to the scaling. Recently, Cottrell
announced that it has licensed the Bahco process for use
in the United States. At the present time, they will accept
orders for scrubber facilities up to 40 MWe per module in
size.
In the United States, Combustion Engineering, Inc. has
constructed and operated three full-size scrubber facilities:
two in 1968 at existing coal-fired power plants (the 125
MWe Kansas Power & Light Lawrence Station No. 4 and the
140 MWe Union Electric Meramec No. 2), and the third, on
a new plant (the 420 MWe Kansas Power & Light Lawrence
Station No. 5). These units all employ boiler injection of
limestone followed by wet scrubbing in single-stage flooded-
bed scrubbers (method three of Figure IIJ-1). These plants were
expected to remove about 85% of the SC>2 from flue gas generated
using about 3.5% sulfur coal.
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Multiple problems including corrosion, plugging of
drain lines, spray nozzles, demister and reheater, lime dis-
tribution and mechanical failure of pumps and other
components were experienced during early stages of operation
of the 125 MWe KP&L Station No. 4. After incorporation of
several modifications, the system was able to operate for
extended periods with improved reliability even though the
scrubber was periodically taken off line for inspection and
repair and the plant boilers fired on natural gas at these times
During the first half of 1971, the unit operated with
SC>2 removal efficiencies of 50-65% and up to 90% for short
periods. In a three-day test period in March 1971,
efficiencies ranging from 52-87% (averaging 73%) were
achieved while firing 3.4% sulfur coal.
Problems were experienced at KP&L in early 1972 when
the larger (420 MWe) unit was added to the system. The
scrubber on the larger boiler is said to have caused over-
loading of the ponding system such that scaling occurred in
the scrubber beds of both units.
Another series of tests were conducted In February-March
1972, which Indicated that lower gas velocity, high L/Q ratio,
and high solids.recycle would improve the operation of the
facility. The scrubbing system has been recently modified
to achieve lower gas velocity, higher L/G and high recycle
of solids. The object of these revisions is to demonstrate
reliable operation of the system, probably with lower SC>2
removal than originally expected. The system with these
modifications was tested during October 1972, for approximately
two weeks. Based on results of operation during this short
period, KP&L management expects to obtain 75% SO2 removal
and 99+% particulate removal with this system in long-term
continuous operation. This program has been supported by
EPA-funded testing on the 11,000 CFM Combustion Engineering
pilot unit in Windsor, Connecticut.
The Union Electric unit was also tested in May-June
1971 with S02 removals similar to the 125 MWe unit. However,
mechanical equipment problems, mostly unrelated to limitations
in the process design, limited continuous operation to about
80 hours. Boiler pluggage was also a major problem with this
unit. Recently, Union Electric has announced abandonment of
this unit.
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The 420 MWe unit was initially tested in September
1971 during which maldistribution of gas flow to the six
scrubbers was noted. Gas flow control modifications have
since been made. The unit was started up again using
coal on November 28, 1971. Currently, information on SC>2
removal is not available for this unit. This unit is
currently being modified to achieve conditions suggested
by the February-March tests in Unit 4. Two additional
scrubbers are being installed in parallel to the existing
six scrubbers in order to lower the gas velocity.
In February 1972, the 175 MWe Commonwealth Edison Will
County Station - Unit No. 1 (Figure III-2) started up. This
unit has operated intermittently since start-up and has
generally achieved SC>2 removal efficiencies in the range
of 75-85%. Demister pluggage with a soft, mud-like substance
has been a problem; but with automatic demister washing
with make-up water via bottom sprays and other system modi-
fications, this problem appears to be controllable. There was
no hard scale noted anywhere in the system in operations to
date. Economic disposal of sludge from this system appears
to be a problem; however, Commonwealth Edison is presently
working on this problem with Chicago Flyash Company. One of
the first steps taken will be the installation of a sludge
treatment system to allow disposal of sludge with a lower
water content. None of the problems encountered thus far
in the Will County unit appear to be insurmountable. This
facility was also recently visited by SOCTAP members and
a more detailed description is presented in the appendix.
This system is the first full-scale installation in the
United States that uses limestone introduced into the scrubber
circuit. This system is representative of a trend in recent
years away from the boiler injection mode due to the possi-
bility of boiler pluggage and the tendency toward serious
scaling problems.
It should be noted that EPA is conducting a major test
program in the lime/limestone scrubbing area at the recently
built prototype facility at the TVA Shawnee steam plant near
Paducah, Kentucky. Bechtel Corporation is the prime con-
tractor for the test program for which TVA is supplying
operational and analytical personnel. The facility is very
versatile and will test limestone/lime scrubbing in venturi,
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turbulent contact absorber and flooded marble bed scrubbers.
The facility is equipped with extensive process instrumenta-
tion and sophisticated data acquisition and handling systems.
Test phases involving air-water and soda-ash, water, SO2
and flue gas, water, soda ash have been completed. Testing
with limestone is presently getting underway. As testing
progresses, the total body of knowledge in wet scrubbing
will be greatly increased.
B. Magnesium Oxide Scrubbing
In many respects,' the magnesium oxide (MgO) scrubbing
process is similar to lime (CaO) scrubbing. The principal
difference is that the spent magnesium sulfite and sulfate
salts are regenerated producing a concentrated stream of
10-15% S02 and regenerated MgO for reuse in the scrubber
loop. Since the reactant is recycled, it must be protected
from contamination by fly ash. It is, therefore, necessary
that the process be applied on an oil-fired boiler or that
the fly ash be sufficiently removed from the flue gas prior
to passing it into the MgO desulfurization process.
This process was first developed by the Grille Company
of Hamborn, Germany. In 1968, Grillo scaled up the small
pilot plant which it has operated for about one year to a
15,000 CFM scrubbing facility installed on an oil-fired
boiler of Union Kraft at Wesseling, Germany, The reactant
used was principally MgO with about 6% manganese dioxide.
Spent reactant from the scrubber was shipped from Wesseling
to Hamborn where it was calcined in a vertical kiln with
a carbon reducing agent to assist in the regeneration of
MgO. In Japan, the Mitsui Aluminum Company has tested
this system on a pilot-scale basis with generally encourag-
ing results. During the development program, Grillo adopted
the centralized reprocessing concept which suggests that
the superior economics associated with a large regeneration
facility will offset the cost of transporting spent reactant
to a centralized site and the regenerated reactant back to
the utility. This coneept is similar to and probably stems
from the custom smelting practices of certain nonferrous
smelting operators, of which Grillo is one.
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In the United States, the Chemico Corporation is
following a nearly identical approach to that of Grillo.
EPA and Boston Edison are cost-sharing the development
of an MgO scrubbing and regeneration process on a 150
MWe oil-fired unit at Boston Edison's Mystic Station.
The flow sheet for this process is schematically shown
in Figure III-3. This facility started up in April
1972 and has operated intermittently since then. Areas
of potential concern with the process, which will be
evaluated during the 12-month test program, include:
potential scaling and plugging problems, attainment of
90% design efficiency, potential erosion/corrosion pro-
blems, effectiveness of the regeneration step, and over-
all system reliability. The results of these tests will
be particularly important since there is only a limited
amount of information on this process based on prior
pilot plant testing by Chemico and Babcock & Wilcox.
Also, this demonstration represents the first time that
the individual steps of scrubbing, centrifuging, and
calcining have been operated on an integrated basis for
the Chemico system. The system has thus far in its
intermittent operation achieved 90+% SC>2 removal with
no apparent scrubber related problems; the major problem
area has been with the dryer's operational reliability.
In the EPA-Boston Edison demonstration, only the
equipment for absorption, centrifuging, and drying is
located at the power plant. Spent reactant is shipped
to the Essex Chemical Plant at Rumford, Rhode Island,
where it is calcined to produce SC>2 for making about
50 tons per day of 98% sulfuric acid. The SC>2 produced
during regeneration will provide feed for this plant's
total acid output.
A second full-scale magnesium oxide S02 removal
facility is planned for Potomac Electric and Power's
Dickerson No. 3 unit. Approximately 100 MWe of the
195 MWe of this unit will be processed. Since this
facility burns coal (3% sulfur, 8% ash), the scrubbing
facility consists of two separate venturi scrubbers.
The first removes fly ash particulates; the second
absorbs the SO^. Present plans are to use the afore-
mentioned calcination facility located at the Essex
Chtoical Plant. This facility is scheduled to start
up early in 1974.
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For both the Boston Edison and Potomac units, the
particulate-free, S02~containing flue gas from the
power plant enters the venturi absorber where it contacts
a dense spray of the slurry absorbing liquor. The ab-
sorbing liquor consists primarily of magnesium sulfite
(MgS03) , magnesium sulfate (MgSC>4) , and magnesium oxide
(MgO). Fresh MgO slurry is added as a makeup. A bleed
from the absorber goes to a centrifuge for separation
of the solids from the mother liquor. The mother liquor
is returned to the absorber system. The wet cake from
the centrifuge, containing water of hydration and surface
moisture, is dried in a direct-fired rotary kiln. Hot
drier exhaust qa.st.-:; pass to the stack where they provide
reheat for the flue gas from the absorber.
The anhydrous crystals leaving the drier, after
addition of carbon, are next reacted in a direct-fired
calciner to regenerate MgO arid release sulfur oxide.
The high operating temperature (about 1800-2000°F) is
needed to regenerate MgO from the relatively small
quantities of MgS04. 7H20 that form from oxidation of
MgS03 *6H20. The regenerated MgO produced is mixed
with make-up water and reused in the absorber system.
The calciner off-gases containing 15-16% SO2 are sent
to a conventional su If uric acid plant, for further pro-
cessing. Table IU-1 lists the chemical reactions
which have been postulated for the major steps of the
process. The appendix describes the status of the
Boston Edison unit, based on a visit by a SOCTAP member.
C. Catalytic Oxidation (Cat-Ox)
Monsanto has -leveloped a modified version of the
well-known contact i;jSC)4 process for removing SO2 from
power plant fine gas. Basically, the process consists
of passing the flue qas through a fixed catalyst bed
where S02, in -iv ;~ie.5ence of O;>, is converted to 803.
The 803 is thf,1 st sorhed in reci rculated H2S04 in an
absorption to'wt»
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Table III-l. CHEMISTRY OF MgO Sli'kRV PROCESS
ABSORPTION
MAIN REACTION
MgO *$02^6 H£0 -» Mg SOj • 6
SIDE REACTIONS
Mg S03+SG2 + H20 -» Mg (HSOa)2
Mg S04 • 7 H20
MgS03 + l/2 02^7 H20 ~* MgS04 • 7 H20
DRYING
MgS03-6H20 ^ MgSOa-hBHzO
M|S04 7 H20 ^ MgS04 *• I H20
H20(l) ^ H20(g)
REGENERATION
MgS03
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Besides being designed for the dilute SC>2 concentration
found in flue gas, the Cat-Ox process differs from tho con-
ventional contact process in two principal respects: first,
the flue gas entering the process must either already be at
a high enough temperature, about 850°F, for the conversion
of SOo to 803, or heat must be supplied. The heat of re-
action alone, because of the .low SC>2 concentration, is in-
sufficient to maintain the required temperature. Second,
SC^-containing ya.s (rlue gas) entering the system is not
dried prior to enieiing the converter.
For POVC.L j.ioM applications, Monsanto has proposed two
versions of the process: first, i.he "integrated system"
for use on new plants and second, the "reheat system" for
use on existing plants, These variations are shown in
Figures III-4 and ITJ«[>.
In the "integrated system-.," schematically depicted
in Figure III-4 hot flue gas at about 850°F is taken direct-
ly from the boilei and passed through an efficient dust
collection system (mechanical collectors plus an electro-
static precipitatcr) to remove at least 99.6% of the
particulates. The gas then flows through a converter where,
in contact with a vanadium pentoxide catalyst at about
850°F, oxidation of the SC>2 occurs. Flue gas from the
converter is next cooled in an economizer followed by an
air heater. By maintaining the operating temperature of
these units above the dew point of H^SO^, corrosion
problems are avoided. Sulfuric acid in the flue gas is
then condensed in a packed-bed absorber by direct contact
with acid recycled from an external cooler, producing an
80% acid product Acid mist and day ieiiu-iining dust in the
flue gas is then, i ..-moved in a highly efficient, fiber-type
mist eliminator -mn passed out the stack.
The "iehfri\ system" shown in Figure III-5 is similar
to the " i ntt:Mi 01 *••<< '-ystem." Howevei » the temperature of the
entering gas is lyrically about 325°F in this system, com-
pared to 8503F jn the "integrated system." Therefore, the
electrostatic precapitator need not be designed for such an
extreme temperature service. High efficiency dust removal
is still required, however. The low temperature of the en-
tering gas also necessitates raising the gas to reaction
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temperature before it enters the converter . This is done
by using the converter exhaust qases to prohe.it the incominq
gas. To supply the additional heat roquii^'i, hot gas from
the combustion of oil or gas is added ;ii ;{.<. t ly. With these
exceptions, the two systems at« >"=;••,;,; >[}y alike.
Monsanto tested the " i M. :-g '. oted ptocesG" on a 15 MWe
scale at Metropolitan t?._ ;. con • ,s Port. j,,nd ,.; t.tti on . These
tests, which cove tea a tvvo-yt-ar period from 1967 to 1969,
indicated the cap -,r; i i 1 1 ut r he m'<->.-"rbJ- *;> remove 85-90%
of the sulfui xii;-- '' '-.- , •, n a'.'/n •, ion, the information
required for 3caj >-•;[ •.. r tn - pi'-.e,^-: / •;-• ,>bt3 !.:,ed .
The princip,-,! t^chr.jd.i pK.-bieais -vjt,],
for power plant ap;pl icati on are us HOC i at 7< . Monsanto es
catalyst cl-;sninc' will be required at about
tervals. The ^9.6% collection efficiency r
precipitators is near the u,^..er limit of pr
equipment. The t-^chr.i>.-a 1 s tcresu of the r.r
to a large extern on how -.veil this critical
can be met. .,
the Cctt-Gx process
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requirement
This \> jc uc :'.-.-. ha.-, bee,1-; <>}! r , 'I- II line .; r- -'*>.' Conij.)ariy .
The $6,7 n. iliinr, ::ost oL ; h .- • : n onr, ti at i o". '.--,.; be shared
by EPA ar,d J i .1 inoi;; Povvi... , .,,t i, 1 —up .: ;j 1. 1 r- •• '"I1/ underway
and will he f.iilo ^ci h-y .-.. •;;: '•- \£»ar test prt- . :n .
We J iman -Loixi
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In th
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S02 in the f s ue -ja.- :s dbi>or,kif-d into a solution of sodium
sulfite, bic; ilfjte, c.Ad b.ilt \ie , converting some of the sul-
fite to bisulfite aeor.rd s uy to the following equation:
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Some of the absorbed S02 undergoes oxidation and shows
up in the solution as sulfate. The active scrubbing solution
is regenerated by evaporating water and SO- while crystalliz-
ing sodium sulfite in an evaporative crystallizer. This
step is represented by the reverse of the above reaction
and is promoted by heat input. The vapor product is cooled
to condense out all of the water. The pure gaseous S0?
can be further processed to liquid S02/ sulfur, or sulfuric
acid. Condensed water is used to redissolve the sulfite
solids for recycle to the scrubber. Sulfate formed in the
scrubber cannot be regenerated and is removed from the
system by direct purge of scrubbing solution or selective
crystallization of sodium sulfate. The purge can be treated
to transform sodium sulfite and sodium bisulfite to sodium
sulfate to eliminate an oxygen demand problem.
The specific advantage ot the WeiIman-Lcrd process is
the simplicity of its unit opei^ations. The main disadvantage
of the process is its sensitivity to buildup of contaminants
necessitating bleed. The major contaminants venerated in
the process are sodium sulfate, sodium thiosulfate, sodium
polythionates, and a small amount of elemental sulfur.
As stated previously, sulfate is generated by oxidation
of sulfite in the absorber. In the crystallizer, sulfites
are converted to sulfate, thionates, thiosulfates, and
sulfur by a disproportionation reaction which is promoted
by heat. There are several ways to control these undesir-
able reactions, the discussion of which is considered
beyond the scope of this paper.
A full-scale demonstration of the Wellman-Lord process
will be undertaken by Northern Indiana Public Service
Company at their D. H. Mitchell plant in Gary, Indiana,
with partial funding by EPA (approximately $4.25 million).
The system will be a retrofit to the 115 MWe boiler No. 11
and is designed for coal containing 3-1/2% sulfur and 11-1/2%
ash. The anticipated removal efficiency will be no less
than 90% in any case, and cleaned stack gas will contain
less than 200 ppm SO if the sulfur content of the coal is
less than 3-1/2%. Tne contact specifies that sodium make-
up shall not exceed 6.6 tons/day of sodium as Na2CC>3. This
plant will also demonstrate the technology for reduction of
SCU to elemental sulfur. Present plans are to start con-
struction of the unit, in January 1973 arid to start-up the
plant in July 1974.
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A very significant demonstration of Wol 1 man-Lot <1
technology is in J.ipan by the Mitsubishi Chemical Mactiinciy
(MKK) at the Japan Synthetic Rubber's Chiba Plant. This
unit treats a flue gas stream equivalent to about 75 MWe from
an oil-fired boiler containing 600-2000 ppm SC>2 and achieves
better than 90% removal of SC>2, which is converted to high
quality sulfuric acid. In general, operation has been
quite reliable, operating in excess of 9000 hours since
June 1971. During the past year, the scrubber has been
available almost 100% of the time the boiler has been in
operation. This may represent the longest successful
operation of any modern large scale SC>2 control process.
The main disadvantage of the system is the requirement to
bleed a waste liquor stream due to sulfate formation. For
the Chiba unit, this stream amounts to 1-1.5 tons/hour and
contains no sodium sulfite or pyrosul f i t.e, has a pH of
approximately 7 and a COD value under 200. It is estimated
that approximately 10% of the total incoming sulfur is bled
from the system; this corresponds to about 4% oxidation.
Recent developments by Sumitomo (Japan) have indicated these
numbers can probably be decreased by 55% by the use of an
oxidation retardant. SOCTAP members have visited this
facility and a trip summary describing the process in more
detail is included in the appendix.
E. Double Alkali Systems
There has been recent and intense interest in a new
class of throwaway flue gas desulfurization systems, double
alkali wet scrubbing technology. This process, which has
several variations, involves scrubbing flue gas with a
soluble alkali, such as sodium sulfite, and regenerating
the alkali with an insoluble alkali, such as lime, producing
an insoluble throwaway product, such as calcium sulfite.
The process has the potential advantage of soluble alkali
scrubbing without the potential scaling, plugging, and erosion
problems associated with slurry scrubbing.
Figure III-7 schematically depicts a double alkali
system. Flue gas entering the bottom of the absorber/scrubber
is contacted with a solution of Na-SO-^/NaHSC^ in the ab-
sorber. The liquor leaving the absorber becomes rich in
NaHSO3 as S02 is absorbed and reacts with the Na SO3. A
calcium hydroxide slurry is prepared in a mixing tank and
it is added to the caustisizer where it is mixed with the
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scrubber effluent. Regeneration occurs in the vessel and
the bisulfite is converted to the sulfite with the production
of calcium sulfite. Also, since some sodium sulfate forms
from oxidation of sulfite and bisulfite, lime must also re-
generate the sulfate by producing sodium hydroxide and
gypsum. The caustisizer product is pumped to a thickener in
which the precipitated calcium compounds are removed, and
the overflow liquor is pumped to a holding tank where make-up
Na2Co3, make-up water and wash water from the calcium salt
cake are mixed and returned to the scrubber. The following
are the chemical reactions postulated for this system:
Scrubber :
(a) Na2SO3 + S02 + H2O - * 2NaHSO3
Caustisizer :
NaHS03 + Ca(OH)2 - »NaOH+Ca3C>3 • 1/2H20 + 1/2H20
> 2!JaOH f CaSO[|
(d) NaOH + NaHS03
Another important variation to this process involves
use of both limestone, a less expensive alkali, and lime.
Limestone is used for the regeneration of the bisulfite,
and lime is used to regenerate the sulfate.
This process ha^i the potential advantage of performing
high efficiency particulate scrubbing and SO2 absorption
in one scrubber. This is feasible since sodium sulfite
solutions are quite effective absorption solutions and are
capable of yielding high SO- removal efficiencies in Venturis,
venturi_rocjs and similar scrubbers which are capable of
efficient particuJate removal but are not particularly
effective mass transfer devices.
It s"hould he noted that the driving force for reaction
(c) above is not great and SO ~/SO3 concentrations must be
maximized to increase t.he driving force. Most of the
variations of the double alkali process involve alternate ways
of treating the Na2SC>4 which is inevitably produced in the
absorption/scrubbing device. For example, use of ammonium
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sulfite scrubbing systems has been studied since the
thermodynamics for the regeneration of NII^SO^ is much more
favorable as compared to Na2SO4. However, due to the
volatility of ammonium compounds, serious fume problems
have been observed which, to date, have led to unacceptably
visible stack plumes. Another variation, developed in Japan,
involves reaction of a soluble sulf ate/sul f ite/bisulf ite
bleed stream with H2SC>4 and product calcium sulfite. Sodium
sulfate is converted to sodium bisulfite according to the
following reaction:
Na2S04+2CaS03- l/2h2O4H2S04+3H?u — »• 2NaHS03+2CaC04 •
Such systems allow the use of the less expensive limestone
for bisulfite regeneration.
To date, u^.iblc- alkali , .'/stems have been tested on a
pilot-scale bc'isis by several organizations. General Motors
and Chemico have run pi lot-hf-a ie tests on a process similar
to that depicted in Figure 111-7, and encouraging results
have been reported. Kureha and Showa Denko, in Japan, have
tested the system variation involving H-^SO^ addition de-
scribed above on a bench-scale and pilot-scale basis,
respectively. Double Alkali efforts to date have generally
indicated high S02 removal efficiencies (>9C%) , low sodium
make-up requirements and generally reliable operation.
EPA is in U'f- pro -ess •.! initiating a comprehensive
double alkali development program on a large pilot plant
to evaluate the various double alkali systems and to
optimize the most attractive schemes,
£' • PJ1Y_ JL-JL?'*5 y to?V£ _jn ject-i on
The dry L-imest i>n" jr. )ss in considered a
fairly well characterized control process with only limited
potential, d\>f- i i:" ,- i I/ i.<.; inherently low removal
efficiencies, i'ne j ^re-ess involves the injection of
pulverized 1 tui^t, tone -iiLoct ly into the power plant boiler
where it is calcined to lime and subsequently reacts at high
temperature with SC>2 anct excess oxygen in the boiler to
form calcium sulfate. The calcium sulfate is then removed
as a solid with the fly ash by mechanical collectors and
electros tat ic Hr ec i pita tor ,j ,
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Although recognized and investigated for many years,
the process had not been characterized adequately to enable
its confident full-scale utilization. For this reason, the
most comprehensive full-scale test program on the process
was initiated under a joint EPA-TVA project performed at
the Shawnee Station near Paducah, Kentucky. The program has
recently been completed. The process was installed on a
140 MWe boiler burning an average 2.7% sulfur, pulverized
coal.
The goal of the- Snawnee test piogram was to establish
the conditions for optimum system performance and obtain
comprehensive design and cost information. Results from
the comprehensive test effort have indicated that:
(a) SCU removal efficiencies are quite low; for most
limestones with the boiler operating at or near
full load only about 11% per unit of stoichiometry
can be expected with 95% confidence. This re-
moval can increase by a factor up to two if a
reactive limestone, such as marl, is available,
and/or if the boiler is operated near 50% load
conditions.
(b) Use of this process can lead to severe operating
problems. for example, during testing at
Shawnee, severe boiler reheater pluggage occurred
after only 6 d.iyt; of continuous testing. Union
Electiic has experienced similar pluggage problems
in their boiler during testing of their boiler-
injection/wet limestone system installed at their
Meramec No. j. Station. it should be noted, how-
ever, that such problems have not been severe at
a similar system installed at Kansas Power &
Light's L.-iwrenre Station No. 4 or at Detroit
Edison's St. Ciair NO. b Unit. Differences
associated wit.h boiler pluggage potential are
attribut i.-.i to specific boiler design features of
which tube spacing and temperature regime are
considered major parameters.
(c) Degraded electrostatic precipitator performance
resulting from higher dust loading of higher re-
sistivity particulate has been reported. Re-
ductions in efficiency ranging from 10% average to
about 25% were measured at Detroit Edison and
Shawnee. Test results from the latest precipitator
test program at Shawnee are not yet available.
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In light of the inherently low removal efficiencies,
and the potential for major reliability problems, it does
not appear that the dry limestone injection process will
play an important role in controlling SO,, emissions from
power plants. While the process may find some use for
particular situations, its application is expected to be
limited.
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IV. PERFORMANCE AND COST COMPARISONS OF FLUE GAS
DESULFURIZATION SYSTEMS
Any discussion or comparison of cost and performance
data relating to full-scale, commercial flue gas desulfuri-
zation systems must be prefaced with the warning that
generalized conclusions and figures are at best calculated
opinions or scaled-up projections derived from currently
incomplete data. At present there are too few installa-
tions and insufficient operating experience with any of
the processes to permit historical comparison. Available
information on the different processes is largely derived
from non-typical examples such as pilot plant experience
and experimental and prototype installations, and based
on a wide range of variables, so that they cannot be com-
pared in a precise manner. With commercial scale work on
most of the processes continuing, a basis for more accurately
assessing full-scale performance and installation and operat-
ing costs for different systems and specific applications
will be built up over the next several years.
A. General Considerations
An examination of the rationale for switching to low
sulfur fuels was outside of this Task Group's objectives.
However, an estimate ut the range of incremental operating
costs associated with the additional cost of low sulfur
fuel has been included in the summary table as a prelimi-
nary comparison with S02 removal processes,
Because S02 control processes are in an early stage
of development, it was necessary to generalize from the
scattered information available in order to obtain a
rational picture of relative performance and costs of SO^
removal processes.
B. New Versus Retrofit Installations
As far as S02 removal efficiency is concerned, there
seems to be little difference whether a particular S02 re-
covery system is added to an existing utility plant, or is
— 39 —
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planned, engineered, and constructed concurrently with
completely new power generating units. Operating per-
formance and direct operating costs may be slightly
affected by some of the design differences required for
retrofitting. The important difference, however, between
new and retrofit installations is the greatly increased
cost of construction and installation of retrofitted
equipment. This includes escalation for the requirements
of intercepting duct work,, and other special equipment;
new buildings or structural revisions and enlargement of
present structures; more difficult job locations, erec-
tion conditions and other site constraints; and extra-
ordinary interconnection and startup expenses. These
additional costs can increase the total investment to
several times the estimate for concurrently designed and
constructed facilities, and the upper limit would be what
the utility is willing to spend to keep from having to
convert to more costly low sulfur fuels, if he can get
them. Obviously, there are many present utility installa-
tions for which it will be impractical to retrofit. For
this SOCTAP study, retrofit costs were based on construc-
tion contractor's estimates for the typical or average
situation at most present utilities, generally represent-
ing a substantial increase in total cost over completely
new installations.
C. Throwaway Versus Saleable Product Systems
1. Throwaway Processea
In throwaway systems, the input reagents are not
ordinarily regenerated and recycled, and all of the end
product is considered waste material and discarded.
These systems, primarily the limestone, lime or the
double alkali scrubbing process, are generally less
expensive to purchase and build because of their simpler
technology. In a-id it ion, these throwaway processes
generally do not require the removal of particulate
matter (mainly fly ash) from the input gas prior to the
S02 removal stage. Consequently, any requirement for
electrostatic precipitators, or special particulate
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scrubbers is eliminated, as fly ash is adequately recovered
by the S02 scrubbers. For new utility plants, the elimina-
tion of particulate removal system reduces the total
out-of-pocket cost.
The operating costs for throwaway systems are highly
sensitive to the cost of the input additives, and the cost
of waste disposal. In some locations the delivered cost
of the required large volume of reagents may be prohibitive.
In some cases, the physical location of the utility, local
land use regulations, limited storage site area, or water
pollution potential may require excessive costs for secondary
pollution control, or for transportation of the wastes to
distant disposal areas.
Any of these factors may preclude the use of a throw-
away system in certain situations, despite any advantages
or desirability. Assuming moderate cost for reagents
delivered to the plant and nominal disposal costs related
to discharge into local settling ponds, the annual cost
for throwaway systems is generally less than for other
systems. In some cases where operating costs will be
high due to waste disposal costs, there is a possibility
that some offsetting benefit could be obtained if all or
part of the waste material could be further processed into
a non-polluting saleable product such as gypsum, concrete
aggregate, or solid land-fill material. This problem
requires further investigation since both cost and environ-
mental benefits may be realized. Currently, a practical
technology is not available, and it appears that market
availability is limited and economic benefit would be
marginal in most cases.
S02 removal efficiencies for throwaway processes are
comparable to other systems, and are generally adequate,
with the exception of the special process involving dry
limestone injection directly into the furnace. This last
process also has serious unsolved operating problems, and
has been generally abandoned as a practical method of SC>2
recovery.
2. Recovery Systems
For saleable products (recovery) systems, generally
the input reagent is regenerated and re-used; and the
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process converts the recovered SC>2 to a marketable by-
product such as sulfuric acid, liquid S02 or elemental
sulfur. The advantages of reducing the need for pur-
chasing, storing and handling large volumes of input
reagents, reducing or eliminating solid waste disposal
problems and a potential for supplementary income from
by-product sales, in many cases could result in lower
direct operating costs than for throwaway systems.
This savings must Le balanced against higher capital
investment cost. The increased technical complexity of
these recovery systems, plus the added costs for regen-
erating stages (particularly for off-site processing
plants) increases the initial investment cost from 20%
to 50% over a throwaway system. To be comparable to the
throwaway system, this estimate includes particulate
removal. In most of the recovery processes, particulate
removal is affected by an additional preliminary wet
scrubbing stage integrated into the SO-> removal process,
and the cost is included in the present SOCTAP study
figures. In certain cases where a separate precipitator
might be used, its cost would be roughly balanced by a
corresponding redaction in the SC>2 systems cost as a
result of eliminating the extra scrubbing stage.
The total annual cost, including annualized fixed
charges, for recovery systems (not including any off-set
from by-product sales) is generally higher, by at least
one-fourth, than !"• ;,: throwaway systems.
Despite theae higher ar.nualized coatsi tor many utility
situations, the elimination of excessive waste disposal
and secondary pollution conrroj costs, and/or the poten-
tial for recovering some of the costs through by-product
sales, make recovery systems highly attractive. These
benefits, however, <^ie stricsly dependent upon the market-
ability ot tr.e sulfur by-piociucts. If the by-products
cannot be sold (or yiven away), they pose transportation,
storage and <.ol '. -.'.f : ~"n uri blems and accompanying added
costs that couJ 1 •: c comparable to the disposal costs of
throwaway sy6tn..s The future economics of the marketing
by utilities of lai ye quantities of by-product sulfur or
sulfuric acid, in competition with potentially large low
cost supplies from petreleuro refineries, nonferrous smelt-
ers, and other sources is difficult to predict, and needs
much additional indepth study.
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D. Development of Comparable Cost Projections
The variety of estimates, opinions or guesses that
have been put forward as probable overall costs for in-
stallation and operation of different pollution control
systems show a wide range, depending upon the source.
There is often a considerable difference in judgment as
to exactly what costs should be charged to a process,
depending on whether it is a utility's estimate of total
out-of-pocket costs or a systems vendor's turnkey quotation.
In order to place capital or investment costs on a
reasonably common basis, the cost data and estimates avail-
able to date have been reconciled to represent the manufac-
turers' base costs for the particular SO2 scrubber system.
Auxiliary equipment is included only if it is unique to the
SC>2 removal technology. Limestone preparation and handling
equipment, for instance, would be included, but the cost of
modification to such items as main flues, stacks, or water
supply and water pollution control equipment are excluded.
Conversely, no credit is included in the SC>2 systems cost
for eliminating or reducing the requirement for specific
fly ash control equipment. To the base cost is added the
estimated costs for construction, erection, and integration
of that particular system with the power generating equip-
ment, generally averaging about 40% of base cost. An
additional increase is included for design, engineering,
and procurement costs attributable to the SC>2 removal sys-
tem. These costs were scaled to the requirements of a
typical coal-burning installation; and separate estimates
were established for both retrofitted systems on existing
utility plants and for systems constructed concurrently
with new generating units.
It was assumed that the typical plant size would be
200 MWe of generating capacity for retrofitted existing
plants, and 1000 MWe capacity for new power generating
plants. Total systems costs are expressed in terms of
dollars per kilowatt of generating capacity of the associ-
ated power gene1" i f J ng equipment.
Inve&ur.ent. cost a are given in two ranges; for each
system the lower figure is an average for concurrent con-
struction with new generating plants, and the higher figure
represents an average cost for retrofitting existing plants.
In either case, actual costs for particular installations
will vary according to furnace and boiler characteristics,
•43-
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_____ _ i —^r. — ^^B
sulfur and ash content of fuels, local pollution control
requirements, raw material storage and waste disposal
constraints, as well as the specific type of scrubber I
and other equipment selected. •
Presently available statistics on the direct operating V
costs for the different systems are less comparable than I
the reported capital cost estimates. The operating cost
is highly sensitive to the raw material and reagent costs m
and to waste disposal ,:osts, Even for the same S02 removal •
process, these costs can vary substantially from one parti-
cular installation to another. Estimates used in this _
study of probable operating costs for each process included •
only a nominal waste disposal cost where applicable, based •
on normal fluid discharge and ponding. A nominal range for
materials costs was used, rather than a maximum possible 0
range. Operating costs include a charge for parasitic power |
consumption.
The projected total annual cost, including annualized •
fixed charges for each process, is expressed in mills per
kilowatt-hour. These are presented as a single range from _
typical low to typical high cost operation based on average I
regional variation in reagent costs, and differences in ™
original capital costs, size, power requirements and operat-
ing results for individual installations with the same type flj
of system. Except as indicated, no credit was included for •
potential by-product sales.
For all cases, annual costs were figured on an assumed |
80% generating load factor, with fixed charges set at 18% of
capital cost. The 80% load factor used is high compared to
reported utility averages, but most of the SC>2 systems in-
stalled over tne near future are assumed to be on base-load
units with higher than average load factors. The levelized
capital charges of 18% include interest, return on investment,
taxes and insurance at typical levels for private utilities,
and depreciation on a 15-year straight line basis.
*•" C'c.-st arid^ Performance Comparisons
Table 1V~1 compares SC)2 removal techniques and probable
investment and annual costs for each of the particular con-
trol processes considered in this study. The figures have
been derived as indicated in the text. Specific comments on
each process follow,
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1. Low Sulfur Fuel
Switching to low sulfur fu^is w i I I involve some
"investment cost" in most instanced Boiler furnace
changes are necessary not ra.iy for switching to a differ-
ent type of fuel (coal to oil), but the differences in
heat content, ash content, and burning characteristics
between high and low .sulfi.r coals also usually require
extensive furnac*; ir.-jdj T'< .-ui. i :m , Costs would vary widely
from one situation to , .••,:, t h-a/, and no generalized estimate
has been attempted.
Dry Limes tone
Inj u c t ion
The strict interpretation of the term Dry Limestone
Injection applies to the process in which the limestone
and the SC>2 reaction takes place only in the combustion
and flue zones in the furnace, and the resulting materials
are removed froir- the stack gas in the dry state, without
any wet scrubbing stage. The investment costs given in-
clude $5 per kilowatt, for the part.iculate reir.oval equip-
ment assumed to be electrostatic preeipitators. The S02
removal efficiency is highly dependent upon the type of
limestone used and the t>oilei load condition.
Injection of dry limestone into the furnace, followed
by wet scrubbing, is a modification of the Wet Limestone
Scrubbing procen- and is eonsi "leri.d under that heading.
sts are vci
therefore o
rse-
Plant d
investrnen, r
is used, and
additional .'o-;t
if necessary, :
for storage and
lime. Annual o
cost of lime DW
greater amounts
costs. Ef f ten... t:_^ :>:- * ';
the 90% range, ^art t.v.; i
Only nominal waste di^po
many cases the cost of >
add significantly to the
1 < r;u ;. It,,!
ro^* '^ouire'int'r. c s , - nd resulting
y Si.i'itdr re-iyardlesy nf which reagent
•'?('. t-'-aied as ore :>••;.ress type. The
.;jt'---;- drying av>o -r,: s nd ing equipment,
. " ,.,.; -e ex'-ent b\ the higher costs
i t s>'iiit:ies roi the more reactive
'.:o;",ts are about the same, the higher
r .!„; the need for proportionately
and the limestone preparation
. irne reagent usually is higher, in
as i.one efficiency is around 80%.
.1 costs have been included. In
a. ing and transporting waste could
rejectee! annual cost.
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4. Magnesium Oxide Scrubbing
Investment costs will depend to some extent on whether
off-site recovery plants are used, or an integrated on-site
recovery stage is used. There are advantageous economies
of scale involved in large off-site recovery process plants,
if they are within reasonable transportation distance, and
can serve more than one facility and costs can be shared.
The costs reported in Table IV-1, however, reflect on-site
recovery and acid production. Credit for sulfur recovery
is based on the assumption that concentrated sulfuric acid
could be marketed at $7 per ton.
5. Monsanto Catalytic Oxidation
Since the end-product of this process is relatively
dilute sulfuric acid, credit for sulfur recovered is con-
siderably less than for other processes. A market value
of $4/ton for the 80% sulfuric acid is assumed.
6. Wellman-Lord
Credit for sulfur recovery based on $20 per ton for
elemental sulfur, or $7 per ton for concentrated acid, is
assumed.
7• Double Alkali Process
Relatively little information is available on costs
or performance of this process, and the proposed figures
are rough estimates only.
F. Specific Cost Examples
In the short tjme allowed for this study, two detailed
cost analyses were obtained. These should not be considered
typical applications but are included solely as examples of
detailed cost breakdowns. The first was TVA's engineering
analysis of calculated investment costs on its Widow's
Creek #8 plant, rated at 550 MWe. The total cost for the
retrofit limestone wet scrubber using a pulverized limestone
slurry as reagent was set at $35,000,000 _ 30%, equivalent
to about $64/KW. The design values were based on using
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12,000 BTU/lb coal. Parasitic power output used to run
the scrubber was set at 24.5 MWe, roughly 4.5%. Con-
struction was scheduled to start in July 1972 and end
in December 1973, 18 months. Detailed costs are shown
in Table IV-2.
In the second analysis, annual operating cost details
were calculated for a Cheitii co-Basic Mag-Ox Recycle Scrubber,
These costs were based on a scrubber for a 600 MWe oil-
fired boiler burning 2,5% sulfur oil at a load factor of
65%. SOX reduction was s?t at the equivalent of 0.3% S oil,
The investment ec><. c "01 this single stage Mag-Ox
scrubber was set by Chemico at $9 million ($15/KW) which
probably understates the full investment by the utility
for the design and erection of this facility. Recycled
MgO and by-product sulfuric acid are produced from the
scrubber wastes by a central processing plant off-site.
Five 600 MWe stations are p.tdicated in the design and
financing of a single piocess plant turning out 1.000 tons
of 98% sulfuric acid per day. The cost of the process
plant (an acid plant and a calcinei pltvt) is set at
$8,200,000; thus, the tot-.il closed system cost would be
5 x $9 million plus $8.2 million ot $53,2 million.
The annual operating cost detail supplied for the
Mag-Ox system by the Chemical Construction Corporation
is shown in the attached Table TV-3.
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TABLE IV-2
TVA WIDOW'S CREEK #8 - LIMESTONE WET SCRUBBER 550 MWE
I
Preliminary Construction and Facilities $ 445,000
I Yard Work $200,000
™ Unload $ Handle 40,000
Powerhouse Revisions 5,000
Miscellaneous Buildings 200,000
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Limestone Handling § Storage Facilities $1,890,000
Truck Rd (1 mile), Rail Track (1 1/4 miles)
Scales and Structures (2), Storage Area
(2 1/2 acres), Hopper with Car Shaker
(175 Ton Capacity), Conveyer System,
Storage Silo (7400 Tons Capacity),
Dust Control System, Air § Water
I Piping, Drainage, Bucket Elevator,
Front End Loader to Handle § Reclaim
Limestone
| Scrubber System $11,335,000 ($21/KW)
_ Foundations $ 235,000
• Piping System 1,335,000
• Structural Steel 1,200,000
Ball Mill 270,000
I Classifier 15,000
Scrubbers (4 Venturi - Rod) 3,500,000
Pumps, Motors, Drives 550,000
I Tanks 200,000
Draft Svstem (Due's, Reheaters, 3,795,000
— > ii:-.ul at ioii M neat i racing 23:.,0()U
• Disposal t, Recirculation System $1,910,000 ($3.5/KW)
I Disposal Area $1,300,000
Pumping Station § Pumps 155,000
Piping 415,000
•Water Intake § Skimmer 15,000
Concrete Trenches 25,000
Make-Up Water System $100,000
• Instrumentation $450,000
Electrical Work $1,000,000
Misc. Equipment, Local Communication System, Painting $46.000
SUBTOTAL $17,176,000
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TABLE IV-2 (CONT.)
Construction Facilities (10% Direct Costs)
TOTAL DIRECT CONSTRUCTION
Field General Expense
Allowance for Shakedown Modifications
Contingency Allowance (11% Total Cost)
TOTAL FIELD CONSTRUCTION
Misc. Engine Design § Mgt Overhead
Interest During Construction (8% per annum)
TOTAL PROJECT
ADD - R$D, CONSULTANTS, PILOT PLANTS
$1^724^000
'.$18,900,000 ($34/KW)
2,270,000
2,000,000
3,975.000
$27,145,000 ($49/KW)
5,865,000
2,200,000
$35,000,000
$ 1,000,000
No overtime provision; Material cost escalation = 5% per annum
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TABLE IV-3
CHEMICO-BASIC-MAG-OX RECYCLE SCRUBBER
Investment = $9 million
Operating Costs/Year:
Fixed Charges @ 201/yr
Maint. @ 4%/yr
Labor @ .5 man yrs - $10,000 each
Supervision @ 40% of labor
Power @ $0.01/KWH - 38x106 KWH/yr
Dryer Fuel - 100,000 BBL #6 oil @ $3/BBL
Water - ISOxlO6 coal/yr @ $0.25/1000 gal.
Scrubber Costs Yearly =
Acid Processing Plant: Processes MgSOs from 5-600 MW plants
Investment (Acid Plant + Calciner Plant) = $8,200,000
Annual Cost = $3,179,440 (101 amoritization, 4% interest)
Distributed to one 600 MW generating unit
= 201 x $3,179,440 -
$1.8 million
.360 million
.050 million
.020 million
.380 million
.300 million
.045 million
$2.995 million
Annual Scrubber + Processing Cost
Transportation Costs @ $5/ton (MgSOs out
= 26,000 ton/yr)
*TOTAL Mag-Ox SCRUBBING ANNUAL COSTS
NOTE: No credit for sale of acid.
TOTAL -
66,000 ton/yr;
$635,900
$3.630,900
in
460,000
* $4,090,900
The $4.1 million annual operating cost for a 600 MW plant operating at
651 load can be interpreted as follows:
$4.1 million/yr (6 x 105KW x 5694 hrs/yr)
* 1.2 mills/KWH
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V. ASSOCIATED ENVIRONMENTAL FACTORS
A. Quantification of the Problem
One of the major problems inherent in any flue gas
desulfurization system is the necessity to dispose of or
utilize large quantities of a sulfur product. The sulfur
compounds produced by such systems generally fall into two
major categories: throwaway or saleable products. To
date, most utilities have favored utilization of lime or
limestone scrubbing throwaway processes. Lime scrubbing
processes ordinarily produce sludges containing CaS03.1/2H2O,
Ca(OH)2, CaSO4.2H20 and CaC03; limestone sludges generally
contain CaS03.1/2H20, CaCOs, and CaSO4.2H20. For some coal
installations, where efficient particulate removal is not
installed upstream of the wet lime/limestone absorber, such
sludges can contain large quantities of coal ash. Most
systems designed to produce a saleable sulfur product at
the present time yield sulfuric acid, although elemental
sulfur, gypsum, and pure S02 are among the other potential
products.
Typical quantities of potential sulfur products com-
pared to fly ash production for a 1000 MWe coal-fired
boiler are presented in Table V-l. This table provides
rough comparisons between the production rate and storage
requirements for a typical throwaway sulfur product com-
pared to fly ash which is the normal disposable product
from a coal-fired plant.
It should be noted that only rough estimates for
specific volume were used to calculate potential storage
volumes required for 20 years of scrubber operation.
Depending on the process, lime sludges can be allowed to
settle in a storage pond to a 30-70% solids slurry, or
can be dewatered to close to a dry state by various de-
watering techniques. Table V-l also allows rough compari-
son between the potential production of sulfuric acid from
flue gas control systems and the total U.S. production
rates.
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The following are observations which can be made:
1. The production tonnages (dry basis) of throwaway
sulfur product are approximately 50 percent greater (dry)
than the fly ash normally produced; this leads to a
total (sludge plus ash) throwaway requirement about
2.5 times the normal coal ash disposal tonnage. This
indicates that production of the sludge throwaway pro-
duct aggravates an already existing problem, rather
than creates a totally new one. In general, the two
major techniques used for ash disposal, ponding in
large ash disposal ponds and transporting for landfill,
appear applicable to lime/limestone sludges.
2. Large storage volumes are required for the ultimate
disposition of sulfite sludges. For example, for a
1000 MWe unit over a 20-year lifetime, about 900-1100
acres (1.6 sq. miles) of disposal land would be required,
assuming a wet sludge (50 percent solids) ponded to a
10-foot depth. For 100,000 MWe, about 100,000 acres or
160 square miles (to a 10-foot depth) would be necessary
to dispose of the sulfur product. This should be com-
pared to a requirement of about 50 square miles for wet
ash (80 percent solids) associated with 100,000 MWe of
coal-fired capability.
3. Potentially large quantities of sulfuric acid can be
produced by certain flue gas desulfurization processes.
Such processes include: magnesium oxide scrubbing,
catalytic oxidation, and the Wellman-Lord system. Approxi-
mately 28 million tons per year of concentrated sulfuric
acid can be produced from 100,000 MWe of flue gas desul-
furization capability. This is close to the total annual
U.S. sulfuric acid production rate, which was 29.3 million
tons in 1971.
4. Elemental sulfur appears the most attractive product
in terms of production rates and potential storage volume.
About 89,000 tons/year of sulfur would be produced by a
1000 MWe unit per year; this leads to a potential storage
or disposal area of about 63 acres for a 1000 MWe unit
over a 20-year lifetime, assuming a 10-foot stacking
stack height.
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B- Throwaway Product Disposal
Several techniques have been proposed for disposing of
lar<|c quantities of t-hrowaway sulfur products. To date,
most of the operafinq lime or limestone scrubbing systems
have relied on disposal of the sludge materials in a disposal
pond on the power plant site. If sufficient land is
available, the pond is designed to eventually store liquid
sludge material over the lifetime of the power plant. Such
ponds are fed by a bleed stream from the scrubber circuit
which is pumped either directly to the pond or via a thickening
system (clarifier, filter, centrifuge) with the thickened
sludge pumped to the pond. The supernatant liquor from both
the dewatering system and the pond is usually returned to the
scrubber circuit.
Another important disposal technique used where land is
not available at the plant site involves maximum dewatering
of the throwaway bleed stream, using one of the many effective
combinations of clarifying,filtering or centrifuging equipment
available; the solid dewatered sludge is then transported,
generally by barge and/or truck to a suitable landfill site.
However, some sludge materials have been found difficult to
dewater mechanically. Since such sludge products, retaining
large quantities of liquor, are difficult to transport
and lead to eventual land use problems due to the instability
(nonsettling) of the wet sludges, chemical fixation processes
are being developed. These generally involve pozzolanic
(cementitious) chemical reactions requiring the presence of
lime. The reactions lead to the formation of a dry, solid,
and hopefully chemically inert material which is desirable
for landfill purposes.
The major problems associated with sludge disposal on
a large-scale basis are associated with interrelated environ-
mental and economic factors. Although throwaway sludge
materials are relatively insoluble, liquors in equilibrium
with sludge materials typically have dissolved solids contents
in the 3,000 to 15,000 ppm range; major constituents include
Ca++, SO=, Mg++ and SO^ . Although there are no finalized
Federal water pollution regulations and local regulations vary
considerably, it is certainly environmentally undesirable to
allow entry of substantial quantities of such liquors into
watercourses. For this reason, it is considered
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important for users of flue gas desulfurization systems
to operate in a closed or nearly-closed loop modo of
operation. For the disposal pond operation, this means
that all liquor entering the pond is recycled back to
the scrubber circuit; no sludge liquor is released to
any watercourse. Also, in order to avoid unintentional
seepage of liquor through the walls and floor of the dis-
posal pond into groundwaters, it may be necessary to
utilize a sealant material. Visits to the Mitsui-Miike
power plant in Japan and Commonwealth Edison's Will County
facility indicate that attempts have been made in both
installations to operate in a closed-loop mode. However,
in both facilities, seepage, run-off and other mechanisms
could be postulated which would allow liquor to be released
into watercourses, at least periodically. Careful civil
engineering of disposal ponds is needed to assure that
their design is consistent with closed loop operations. It
should be noted that ash ponds which have been utilized for
many years have similar water pollution problems; however,
there is little evidence that ash liquor contamination has
been of major concern to many utilities in the past. For
the landfill disposal technique, it is also necessary that
potential run-off will not lead to any significant water
pollution problem. For both ponding and landfill approaches
a detailed evaluation of the geologic and hydrologic
conditions of the disposal area is necessary to minimize
water pollution potential.
Another environmental concern is the ultimate condition
of the large land areas required for sludge disposal. Some
ponding installations have reported poor settling charac-
teristics of the sulfite sludge material, which could lead to
permanently somi-liquid slurry ponds which would be quite
difficult to reclaim for subsequent development, construction,
or other land use.
C. Sale of Sulfur Products
As stated earlier, sulfuric acid is the sulfur product
which has received the most attention as a flue gas desul-
furization saleable product, but the future market is uncertain,
Although sulfuric acid is a large volume chemical, Table
V-l indicates that each 1,000 MWe
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desulfurization system would produce about 278,000 tons per
year of concentrated acid; this represents about 1 percent
of the present total U.S. production rate. Since market-
ability of a relatively low-value chemical such as sulfuric
acid is highly dependent on transportation costs, it is
necessary that large acid producers be within about 100-150
miles of large users. By far the largest use for sulfuric
acid is for fertilizer production. Other important acid
uses include cellulosics applications (rayons, cellophane,
pulp and paper), petroleum alkylation and chemical production
(Ti02, HF, (NH4J2S04, etc.). At present, the states of
Florida, Louisiana, Texas, and Illinois consume close to
half of the U.S. total sulfuric acid output. Of these states
only the Illinois utilities normally burn large quantities
of high sulfur coal; and therefore would be the ones likely
to apply flue gas desulfurization systems that produce
saleable sulfuric acid.
However, other potential sources of reclaimed sulfur and
sulfuric acid will be major competitors in the marketplace.
By-product sour gas sulfur, in particular, has made large in-
roads in the sulfur/sulfuric acid market. Fuel desulfurization
and nonferrous smelters are other sources. Any new large
source of sulfur effectively impacts the sulfuric acid market,
since most sulfur produced is used for acid production.
Unfortunately, sulfuric acid production from power plant flue
gases cannot be adjusted to market demand for acid, since
these systems must operate continuously, which further com-
plicates their acid marketing.
Although an up-to-date and comprehensive market survey is
not available to assess the situation in detail, it appears
that only a relatively small fraction of the potential flue
gas desulfurization system users will be induced to produce
sulfuric acid, due to difficulty in marketing the acid. For
those systems that can market the acid, the resulting price
for H2S04 might be only $6 to $8 per ton or less. At such
prices, annualized operating costs for those systems, taking
credit for acid sale, will still be somewhat higher than
those of the throwaway systems.
As discussed earlier, elemental sulfur is probably the
most desirable sulfur product. As opposed to sulfuric acid,
sulfur can be economically stored for eventual sale. If
marketing is not possible, sulfur is probably the ideal
throwaway product since it is inert and insoluble, with much
smaller disposal site requirements than those for throwaway
processes. The major obstacles to elemental sulfur
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production appear to be (1) lack of demonstrated technology
and (2) potential economic penalties since operating costs
would be significantly higher than competing throwaway
systems if sulfur cannot be sold. However, a major step
has been taken in the initiation of the partially EPA-
sponsored NIPSCO Wellman-Lord unit which will produce
elemental sulfur. Allied Chemical technology, which utilizes
natural gas as a reductant, will convert the SO2 produced in
the Wellman-Lord evaporator-crystallizer to elemental sulfur.
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VI. INSTITUTIONAL BARRIERS TO THE
APPLICATION OF SULFUR OXIDE CONTROL SYSTEMS
Because the successful demonstration and subsequent
commercial application of SO control systems necessarily de-
pend on the electric utilities and the control system vendors
in the U.S., it is essential to recognize that serious im-
pediments in either of these industries to the general appli-
cation of stack gas scrubbers on coal-fired plants will retard,
or even obviate, the use of flue gas desulfurization as a
control strategy option.
A. Institutional Barriers in the
Electric Utility Industry
Application of sulfur oxide control technology will have
its greatest public health benefits when applied in the
electric utility industry. It is estimated that over 25
million tons of sulfur oxides are emitted in the United States
each year from coal-and oil-fired electric generating plants.
This represents 55% of all sulfur oxides emitted from man-
made sources. Electric power is growing rapidly, and is
capturing a relatively larger share of the energy market
so by the turn of the century 75% of sulfur oxides may be
produced by combustion in power plants. The abatement of
sulfur oxide pollution depends then critically on the ability
of the electric power industry to implement sulfur oxide
control technology or to find alternative sources of low-
sulfur fuel, either naturally occurring or chemically cleaned.
Barriers to the application of SOX control technology
can be associated with technological, economic, or environ-
mental factors. The technology may not be adequately and
reliably demonstrated as discussed above, or the investment
in the technology may be considered as too large to justify
in terms of the reduced risks to human health and property
or the secondary consequences of the technology such as solid
waste disposal may be considered as potentially more noxious
than the air pollution. However, even if all of those
barriers are overcome, application of SOX control technology
can be seriously impeded by barriers in the electric power
industry.
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An assessment of the nature and severity of those
barriers was obtained through a meeting of the SOCTAP
members with representatives of the electric power industry,
assembled by the Edison Electric Institute, and through
contacts between individual SOCTAP members and utility
personnel. The barriers which were identified are discussed
below:
1. Reserve Generating Capacity and Scheduling
of Retrofits
Reserve generating margins are required to meet customer
demand and still conduct essential periodic equipment main-
tenance and cover equipment malfunctions and failures. The
Federal Power Commission has stated that reserves of about 20%
of peak load are essential to avoid sporadic power curtail-
ments.
The electric power industry is organized into regional
power pools which provide an increased degree of reliability
through grid connections between individual utilities.
Assessment of the reserve generating capacity by the
Federal Power Commission for summer 1972, as shown in
Table VI-1, indicates that the reserve capacity in many
sections of the country was well below 20%. In addition, the
reserve capacity available during late June 1972 was con-
siderably below that anticipated for the summer peak period in
a survey conducted in late May 1972. This latter fact is an
indication of both the deterioration of reserve margin during
the peak load period because of equipment failures and un-
expected delays in bringing new equipment on line because
of technical and licensing problems.
The data in Table VI-1 indicate that the lowest reserve
margins were in the Southeast and West Central National Power
Survey Regions. Also faced with lower than desirable margins
were the Northeast and East Central Regions. These regions
with low reserve margins, as can be seen in Figure VI-1, fall
in a contiguous zone in the central and eastern part of the
country. Because 6f the widespread nature of the limited
reserve margins, the ability to transfer power from one region
to another has been significantly reduced. Even with some
inter-regional transfers, the maintenance of adequate reserve
margins throughout the eastern half of the nation has been
quite critical during the past three years. For a variety of
reasons, this situation will probably continue for the rest of
the decade.
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TABLE Vl-1
Generating Capacity and Reserve in the National
Power Survey Regions in Summer 1972
Formerly Expected as of
May 31, 1972
b
Net
ependable Capacity Available
esources**' for Reserves
1 1 of Esti-
mated Peak
NFS Region*
Northeast
East Central
Southeast
West Central
South Central
West
Contiguous U.S.j
MW
71,152
60,175
71,010
44,397
55,948
68,833
371,515
| Actual as of June 27, 1972
Net
Dependable
Resources**
Capacity Available
for Reserves
\ of Esti-
mated Peak
MW Summer Load MW MW Summer Load
10,788
, 9,471
7.071
4,631
9 371
13,223
i 54, 555
17.9
18.7
11.1
11.6
20.1
23.8
17.2
68,772 8,408 :
59,056 8,352 .
68,943 5,004 .
43,607 3,841
55,348
8,771
69,128 !l3,518 :
364,854 J47.894 .'
13.9
16.5
7.8
9.7
18.8
24.3
15.1
*National Power Survey (NPS) Regions are shown in Figure VI-1. In comparing
the NPS with the electrical Reliability Councils, the following identifica-
tions can be made: the Northeast Region corresponds roughly to the North-
east Power Coordinating Council and the Mid-Atlantic Area Coordination Group
combined; the East Central corresponds roughly to the East Central Area
Reliability Coordination Agreement; the Southeast corresponds roughly to the
Southeastern Electric Reliability Council; the West Central corresponds
roughly to the Mid-America Interpool Network and the Mid-Continent Area
Reliability Coordination Agreement combined; the South Central corresponds
roughly to the Southwest Power Pool and the Electrical Reliability Council
of Texas combined; and West corresponds to the Western Systems Coordination
Council.
**Includes net firm power purchases but does not include fossil plants on
line for testing. For nuclear plants, includes only megawatts actually being
operated under license limits.
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LEGEND
Power Supply Area
National Power Survey Region
FIGURE Vl-1-National Power Survey Regions
and Power Supply Areas
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The electric power industry has been characterized by
an extremely high rate of growth for the past two decades,
e.g., its 8-10% growth rate has been twice that of growth
in total energy utilization. These trends will in all like-
lihood continue throughout the remainder of this decade. In
Table VI-2 a recent forecast of the growth in the electric
power industry by Electrical World, September 15, 1972, is
summarized. The data show that the trend of vigorous growth
will probably continue and, although fossil-fuel plant addi-
tions will have a decreasing share of the total yearly addi-
tions, large blocks of new fossil capacity, on the order of
20 million Kw, will be brought on line annually in the late
1970's. Of this 20 million Kw average addition, approximately
55-65% is coal-fired capacity, with 5-15% of the coal-fired
capacity capable of dual-fuel operation, i.e., easy conversion
to oil- or gas-firing (Steam-Electric Plant Factors, 1971
Edition, National Coal Association).
Another factor which must be noted is that economies of
scale and technological developments have increased the size
of both fossil-fuel and nuclear plants significantly over the
past few years, the oil- and coal-fired plants going to 600-
800 MWe and nuclear plants to 1000-1200 MWe. This has meant
that, in many utility pools, larger reserve generating margins
must be maintained to cover the scheduled and unexpected out-
ages of the big plants. The construction lead times for
fossil-fuel plants are now 4-5 years and for nuclear 8-10
years. These long lead times tend to freeze the planning
schedules of the utilities and when delays occur there is
often little if anything the utilities can do to obtain alter-
native sources of power on short notice. The delays which
have been experienced in bringing many nuclear plants on line
also serve to erode the available reserve margin. In several
of the power pools, the status of nuclear capacity of 1000-
3000 MWe threatened by delays due to litigation over environ-
mental questions or technical problems has been the difference
between adequate and inadequate reserves. Nationwide, close
to 10,000 MWe of nuclear capacity originally scheduled for
1971-1972 has been delayed. Thus, even though a record 34,500
MWe of additional capacity will be brought on line by the end
of 1972, growth of 28,000 MWe in the non-coincidental annual
peak has resulted in a drop in the gross reserve margin. Un-
certainty about the status of delayed plants and possible
limitations on the crash-building of gas turbine and internal
combustion generation equipment to substitute for the delayed
plants certainly cloud the immediate future. Whether these
problems can be solved by the time that SOX control equipment
must be installed in great quantities remains to be seen.
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TABLE VI-2
Predicted Trends in the Electric Power Industry
(Electrical World, September 15, 1972)
Actual
1961
1962
1963
1964
1965
1966
1967
1968
1969
1970
1971
Fore-
cast
1972
1973
1974
1975
1976
1977
1978
1979
1980
1985
1990
Annual Non-
Co incidence
Peak
Millions Kw
141
152
161
175
187
204
214
239
258
275
294
322
353
381
414
447
482
517
556
593
820
1103
Capability
at Peak,
Millions Kw
185
199
211
217
230
242
259
280
301
328
353
386
425
470.
513
549
586
629
675
722
1009
1321
Gross
Margin,
% Peak
31.0
31.0
30.2
23.7
22.9
18.4
20.8
17.2
16.6
18.7
19.9
19.6
20.5
23.5
24.1
22.9
21.6
21.5
21.5
21.7
23.0
20.1
Net Total
Generating
additions
Millions Kw
12.7
10.4
18.7
11.7
13.8
11.7
21.4
21.8
22.3
27.7
26.3
34.4
43.2
46.2
40.2
33.6
38.8
45.2
47.9
45.1
59.0
72.0
Net Fossil
Generating
additions
Millions Kw
9.3
8.1
15.5
9.4
11.6
8.8
15.4
16.1
14.9
16.8
17.6
20.3
19.5
23.9
20.8
19.2
16.9
20.9
21.5
20.0
22.5
32.0
Total
Generation
Capital
Expend. ,
Billions $
2.2
1.8
1.8
1.9
2.0
2.6
3.6
4.4
5.6
7.0
9.2
10.1
10.4
9.6
9.8
10.3
11.7
12.4
13.3
14.5
15.6
20.2
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Across most of the country, electric power demand peaks
in the summer, and then again at a somewhat lower level in
the winter. Installation of scrubber equipment on existing
plants therefore would have to be scheduled for the off-peak
spring and fall periods. In a sample power pool investigated
- the Michigan pool composed of Detroit Edison and Consumers
Power - the amount of capacity which could be spared for
maintenance varied from about 100 MWe in winter to 1200 MWe
in spring out of 11,000 MWe pool capacity and zero in summer
to 1,500 MWe in fall out of 12,000 MWe pool capacity; i.e.,
10-13% of the capacity could be spared, and only during these
periods.
In a typical utility operation, each plant is rescheduled
for routine maintenance at least once a year, depending on the
age of the plant, i.e., older plants require more frequent main-
tenance. This maintenance may require 1-3 weeks, which from
all estimates would be too short a time to install even a
pre-assembled scrubbing system.
Once every 4-5 years, again depending on its vintage,
a plant is scheduled for major maintenance requiring 5-8 •
weeks. With careful scheduling, this time should be adequate
for the majority of retrofits. Thus, a power plant might be
available for installation of a scrubbing system once in
the 4-5 year cycle during the spring or fall maintenance period,
i.e., on the average, an upper limit of 20% of the power plant
capacity would be available for SOX control equipment instal-
lation each year. However, because an even smaller fraction
of the capacity can be spared for scheduled maintenance,
scrubbing installations would have to be carefully scheduled
and the installation time kept to a minimum in order to approach
scrubber installations on 20% of the system capacity in any one
year.
To put the point more clearly, the scrubber installation
time would have to be short enough during the 3-month spring
or fall period so that the utility could also complete the
maintenance scheduled on other boilers without exceeding the
limit of 10-15% margin for maintenance. Because of probable
stretch-outs early in the expansion of the control system
industry, it is likely that somewhat less than 20% of the
coal-fired capacity could be retrofitted each year and in
specific cases, such as the Michigan Power Pool and many
other largely coal-firing utility pools in the middle central
and middle south, no more than 10-13% of the capacity can be
retrofitted each year.
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2. Lack of Familiarity with Chemical Processing
Technology within the Electric Power Industry
Traditionally the electric utilities have concentrated
on what they do best - generating electrical power. Until
recently, state regulatory commissions have generally been
unsympathetic to proposed rate adjustments to allow utilities
to conduct R&D on new equipment and methods. Utilities
generally paid for R&D through higher prices on capital
equipment, the R&D having been performed by the manufacturers.
Consequently utility staffs have been composed largely of
mechanical engineers for the fuel-handling and boiler operations
and electrical power engineers for the generation and trans-
mission operations. Only in isolated instances have utilities
ventured into fuel cleaning or other activities which involve
large-scale chemical process technology. Flue gas desul-
furization confronts the utilities with massive, complicated
chemical processing plants, a challenge for which they are
neither adequately nor appropriately staffed.
The experience gained during the recent rapid growth
of nuclear electric power provides some insight. During the
late 1950's and early 1960's, only a few of the most progressive
utilities developed nuclear power divisions within their
organizations. The bulk of the utilities either were un-
receptive to suggestions that they begin staffing with nuclear
engineers on the grounds that nuclear power was "so far off"
that it would not enter into their 10-25 year planning acti-
vities or indicated that they would rely on consulting engi-
neering firms and the manufacturers to provide the required
expertise if it were ever needed. However, with the rush of
orders for nuclear units in the late 1960's and early 1970's,
many utilities suddenly attempted to build their in-house
nuclear capability for siting plants, preparing safety analysis
and environmental reports, etc., and found, not unexpectedly,
that the supply of appropriately trained engineers had been
depleted and that it would take 2-5 years to revamp and expand
graduate programs to meet their needs. Further, the utilities
found themselves competing with the manufacturers for what
manpower there was available.
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A somewhat similar pattern appears to be repeating
itself in the field of flue gas desulfurization. Most
utilities do not yet feel that they will be directly in-
volved in chemical processing, (either SOX control tech-
nology or chemical cleaning of fuels), ana their engineering
staffs have remained little changed. There is a general
feeling in the utilities that they can ultimately rely on the
vendors; yet there is general skepticism of the vendors' claims
at this time. If an early decision is made at the management
level that the utilities must turn to stack gas scrubbing as
an abatement strategy, there will be heavy demand for in-house
engineering talent to prepare specifications, review bids,
provide liaison during the construction and shakedown phases,
and assume responsibility for reliable operation of the
scrubbers. That type of manpower will probably be in a very
short supply.
On the operational side, the situation appears even more
discouraging. Visits by SOCTAP members to the most ambitious
SOX control projects-Commonwealth Edison's Will County plant
and Boston Edison's Mystic plant - revealed a low degree of
interest or involvement in the shakedown phase by the utilities
installing those two projects. While Babcock & Wilcox and
Chemico, respectively, have responsibility for bringing those
plants on line, the operational staff available from the
utilities for those projects are neither adequately nor ap-
propriately manned. Although both facilities have had a series
of unfortunate delays due largely to mechanical problems,
utility personnel have had little direct experience with their
scrubbers. Labor-management factors have also strongly affected
these two utilities' manning of their scrubber installations
and operation, representing yet another impediment to the
rapid application of flue gas cleaning technology.
3. Competing Fuel Supply/Environmental
Protection Strategies
Besides serious question of the electric power industry
toward the national and state sulfur oxide and nitrous oxide
standards, there is in many utilities genuine confusion as
to the best approach to be pursued. The options open to the
utilities are to commit capital resources to an uncertain and
expensive technology to remove SOX from the stack gases or to
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convert from coal to oil, hoping for a steady supply of
low sulfur oil at only reasonable price increases or to
contract for low sulfur coal, largely from Montana and .Wyo-
ming. While full discussion of these alternatives lies out-
side of the SOCTAP mandate, it is necessary to point out
several factors which serve as serious disincentives to rapid
growth of SOX control equipment.
The two low sulfur fuel alternatives do appear more
attractive to many utilities because they involve only small
capital investments and shift the environmental protection
strategy to an operating cost. In a number of states, utili-
ties are now able to pass on to the consumer most of the in-
cremental operating costs of higher-priced fuels by means of
"fuel adjustment" provisions. The fuel adjustment charges
may be passed directly to the consumer via the monthly bill
without further action by the regulatory commission. On the
other hand, increases in generating costs due to carrying
charges on or operating costs of capital equipment can be
compensated only by rate increases which require commission
action. Not only do the utilities claim that they must wait
for this compensation until the regulatory commissions act
but also they claim that -'they often have to "absorb" some of
the additional costs, particularly from nonproductive equip-
ment such as pollution abatement devices. This situation tends
to force utilities to secure as much low sulfur fuel as is
available and then wait to see what the Environmental Pro-
tection Agency or state agencies will do to enforce the
standards. In this regard, it should also be pointed out
that sulfur emissions tax would help only to the extent that
it might force utilities to install stack gas scrubbers on
those plants for which the utility could hot secure low sulfur
fuel.
While the probable dislocations in fuel supply resulting
from these factors raise many questions, one of the most
disturbing is the precipitous rush by the utilities to obtain
low sulfur coal contracts and thus to show "good faith" in
compliance insofar as the low sulfur coal is available.
Vigorous utility competition for low sulfur coal from new and
proposed mines in Wyoming and Montana has led to widespread
speculation in land and water rights, particularly in the
Powder River Basin. Much of the coal in this region lies under
land whose surface rights are privately owned but whose
mineral rights are either owned by the Federal government or
Indian tribes. Few mines are operating today but many appli-
cations for leasing public mineral rights are pending and
blocks of coal deposits owned by the railroad and other private
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interests, the states, and Indian tribes (off the reserva-
tions) are being unitized for exploitation. Acceptable re-
clamation of these semi-arid lands has yet to be demonstrated.
The sudden surge for development of these resources finds
both states and the responsible Federal agencies inadequately
prepared to cope with the array of immediate problems pre-
sented by the development let alone long-range cumulative
effects on the economic, physical, and social environment
of the region. Since stack gas cleaning represents a tech-
nological alternative in the near-term to such a culture-
and environment-shattering resource development, the full
implications of both options should be explored.
B. Institutional Barriers in the Control
Systems Industry
One of the major choke points limiting the growth of
stack gas scrubbing technology could be institutional con-
straints on the various design, construction, and material
supply organizations who will be called upon to expand their
efforts to meet the sizable demand forecasted for 1975-1980.
In order to obtain a scope of this problem the SOCTAP
members interviewed: (a) the engineering department of a
major utility...Southern Services, the people who must specify
the need for scrubbing on particular plants, prepare the
in-house documentation for technical and financial decision-
making, participate in the implementation process and sign-off
on the final product; (b) a major engineering-consultant
contractor...Bechtel who shares the engineering-design res-
ponsibilities with the in-house staff; participates in pre-
liminary development involving alternate process evaluation
and selection, preparation of bid plans and specifications,
hiring local construction and material sub-contractors, job
supervision and approval, and final start-up check-out runs;
(c) two of approximately fifteen* scrubbing system vendors...
Chemico and Combusion Engineering, who supply drawings, pilot
plant data, and the scrubber and its peripheral equipment; and
(d) the National Constructors Association...an organization
representing heavy construction contractors around the country.
The consensus of these sources is as fellows:
*Including:Babcock & Wilcox, Combustion Engineering, Chemico,
Peabody, Universal Oil Products (Procon), Krebs, Envirotech,
Zern, Monsanto, Enviroengineering, Joy, Research-Cottrell,
Wellman-Lord; North American Rockwell, Consolidated Coal.
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1. Utility Engineers
Although the institutional barriers within the electric
utilities to the rapid application of SOX control devices
were described in detail in the previous section, it is well
to reiterate one important point. Because the utilities do
not typically have chemical processing expertise on their
engineering staffs and because there will undoubtedly be a
shortage of experienced chemical engineers if and when
scrubbers are ordered in quantity, the utilities will have
to rely in large part on the manufacturers and consulting
engineers. This may result in d«lays in preparing detailed
specifications for the scrubbers and in deterioration of
performance once the scrubber operation is turned over to
the utility.
2. Consulting Engineers
The consulting engineers provide an interface between
the utilities and the scrubber vendors. These companies can
be divided into two groups - those who traditionally deal with
electric utilities on large construction jobs and those who
do not. For those with utility experience, the corporate
division handling scrubbers are significantly smaller than
divteLqoHS working on power plant design, either fossil fuel
or nuclear power. A typical scrubber system requires 20
men from the consultant's staff (engineers, designers, drafts-
men) plus 20 men from the scrubber vendor's staff. One of
the major consultants is currently working on 5 scrubber
systems. To expand further, the Scrubber Division would have
to borrow staff from the Power Division which is currently
working at capacity on nuclear plants.
For consultants without utility experience, it would
be necessary to create new divisions to build scrubbers. In
either case, a significant expansion of the demand for scrubbers
would cause an immediate shortage of experienced manpower
since all retrofit and many new scrubber systems will be
custom-made products.
3. Scrubber Vendors
Currently there are some fifteen vendors (see list above)
who are more or less established in the flue-gas scrubbing
business. A realistic assessment of the current capabilities
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of vendors indicates that there are three, possibly four,
who have sufficient experience and available manpower and
corporate backing to expand rapidly, i..e., within the coming
year. There are another three or four who are gaining
experience and could probably expand although at a slower
rate. The remainder of the vendors which have very limited
experience could possibly play an important role in the
late 1970's but their ability to design, fabricate, and
deliver an entire system is largely unproven. Finally,
new suppliers may be expected to enter the market with new
processes under license if the scrubber market develops
substantially.
At this time there are some 20 units committed or
underway. It takes two to two-and-a-half years to complete
a scrubber and about the same time to develop experienced,
competent engineer-designers. There will probably be in-
tense competition for experienced manpower if the market
. If :e Jot-s i apid j y ,.
Most vendors do not do their own fabrication. Thus,
there may be choke points at the level of component suppliers
or local fabrication shops. While no specific data were
obtained on this subject, several areas were mentioned by
those interviewed, including:
a. Pumps (lead time approx. 12 months)
b. Fans (long lead times)
c. Rubber-lined, pipes
d. Instrumentation (e.g. magnetic flow meters)
Almost everyone interviewed by the Interagency Task
Force predicted that the growth of scrubber installations
would be hindered by construction labor shortages in critical
skill areas...welders, pipe-fitters, electricians, boiler-
makers, and craftsmen who install the rubber liners in the
scrubbers. These shortages will be local in nature, reflecting
the constrained and declining membership of many local craft
unions, and the reduced willingness of skilled workers to
travel to find new work.
An EPA review of the construction industry shows the
following:
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a. Environmental standards will result in major
new demands on the construction industry for
the remainder of the decade. Besides stack
gas scrubbing facilities there will be sizable
growth in the demand for: Municipal sewage
treatment facilities indluding sewers, refinery
facilities for lead-free gasoline and low sulfur
fuel, thermal pollution reduction facilities for
power plants, industrial waste treatment facilities,
and new coal mining facilities. In addition there
will be a major new shipbuilding program and a
doubling of installed electrical generating capacity.
b. Shortages in process engineering talent will be
qualitative (due to lack of experience) rather
than quantitative.
c. Due to the difficulties in obtaining performance
bonding and sufficient working.capital the
contracting business is highly stratified, with
a few large firms handling the larger jobs. Thus,
as more large jobs come up for bids we can expect
fewer qualified bidders.
d. liabor strength is a local characteristic with over
10,500 union locals divided into more than thirty
different specialized trades. As a rule of thumb,
large non-residential work (over $500,000) in all
urban areas other than the Southeast and Southwest
is performed by unionized workers.
e. The skilled worker is no longer mobile in most
regions due to a reduction in the seasonaiity of
employment, union restrictions requiring work
permits to allow entry into other areas, fringe
benefits tied to local union contracts, and the
general immobility resulting from a higher personal
income.
f. Some of the craft unions show stagnant or declining
membership due to restrictive membership barriers.
The apprenticeship program for a Hoilermaker takes
four years although six months experience may be
sufficient to enable a man to handle most journeyman
tasks.
g. Unlike labor, basic materials (concrete, steel, cast
iron, plywood, electrical system components) rarely
create a check on industry capacity. Problems which
may occur relate to higher prices rather than a lack
of availability.
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h. Productivity in the construction industry has
not increased significantly in a decade and is
not likely to advance in the coming ten years.
Technological advance is sporadic. Pro-fabri-
cation may serve to create "captive" craftsmen,
further immobilizing skilled union laborers, but
it will not significantly reduce skilled labor
requirements on the site due to union work rules
and transportation constraints limiting the size
of pre-fabricHted parts.
i. Due to facttu , rel.ding construction activity
to seasonal and business cycles, many projects
are on-going at the same time and pace. Since
wages are fixed by local union contracts, the
workers tend to move between jobs on the basis
of available overtime. Thus, if pipe-fitters are
getting more oveitime on site #2 than on site #1
they can be expected to migrate even though there
is still work to be done on site #1. Thus, cost
estimates based on a 40-hour straight-time work
week will be underpriced.
j. New environmental standards have created an inelastic
demand for new construction which will probably
reach its peak in the middle of this decade. The
incremental figure for all such pollution control
construction during the decade is estimated not to
exceed four billion dollars (at 1967 prices),
representing an increaise of approximately 4 percent
over a haseline fiyae of about $1UO billion (1967
prices). The impact of this incremental demand will
be f c 1 v 'iirtinly -1S pJ'ire in^J oases,
k. In 1980, an incit.iiH-n t a 1 demand for $4 billion of
construction at 1967 prices would result in $2-4
billion of other construction being foregone because
of insuifiricn* supply to carry it cut, and in the
cost, of projects, constructed on schedule being raised
between $?,:-= and $5,2 billion (1967 prices). So the
"effect 1
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These conditions will cause contractors to
include large contingencies in their bids
for delays and overtime.
m. Of the $4 billion construction increment, the
"non-equipment elements of air pollution control
construction will not be significant."
The implications for scrubber installations in the
remainder of this decade are: higher costs and construction
delays with local labor factors determining their magnitudes.
It would appear to be safe to say that "institutional con-
straints" will limit scr-ibbui installation to the eirtent
that less than 10% of the potential demand can be met by 1975,
and that full demand can be met by 1980 only by extraordinary
circumstances of growth in the vendor industry and skilled
labor force.
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VII. FORECASTING SULFUR OXIDE
CONTKQL TECHNOLOGY
Recent trends in utility orders for flue gas desulfuri-
zation systems have been examined and forecasts for the
application of these systems in the period from 1975-1980
are presented. Implications of the projected expansion in
the use of SOX control technology are described.
A• %,'-_'''!I*-.- f.A'!r_Qds_ -i-JAr Orders for
f'lut/ Ga.'i Desulfurization Systems
By analyzing pi-^seut and planned flue desulfurization
systems in the United Spates, it is possible to roughly
ascertain trends i^ i he degree- of flue gas desulfurization
system utilization and the types of systems which are
presently favored by utilities. In Table VII-1 the full-size
desulfurization systems planned or operating in the
United States are compiled. Note that the table is arranged
in chronological sequence within category type; the facilities
completed earliest are listed first. Pa^ed on this
summary, the following observations can be made:
1. Presently, twenty-two flue gas desulfurization
systems are planned or in operation; sixteen are lime or
limestone scrubbing units; two are sodium-based; three are
magnesium oxide systems, and one is a catalytic oxidation
system. Eleven of the limestone systems utilize injection
of dry limestone into the furnace followed by either wet or
dry scrubbing; the remaining eleven lime/limestone systems
utilize only wet post-combustion scrubbing with a lime/
limestone slurry. Roi n the recent sales patterns and opinion
within the utility inoustiy indicate that few, if any, dry
limestone in. je.-t ion systems will be purchased in the future.
2. The gicat :ii-, ,or MY of the systems are installed
on coal-fired units; only two of the twenty-two are on oil-
fired units.
3. The g" -at maiority of the systems are retrofitted
onto existing boiler facilities; only five of the twenty-two
are systems for new boilers.
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Table VII-1.
PLANNED AND OPERATING FULL SIZE FLUE GAS DESULFURIZATION FACILITIES
IN THE UNITED STATES
UTILITY COMPANY/PLANT/NEW OR RETRO
LIMESTONE SCRUBBING
1. UNION ELECTRIC CO. (ST. LOUIS)/
MERAMEC NO. 2/RETRO
2. KANSAS POWER ft LIGHT/LAWRENCE
STATION NO. 4/RETRO
3. KANSAS POWER ft LIGHT/LAWRENCE
STATION NO. 5 NEW IN 1971
4. COMMONWEALTH EDISON (CHICAGO AREA)/
f ILL COUNTY STATION NO. I/RETRO
5. CITY OF KEY WEST/STOCK ISLANDVNEW
6. KANSAS CITY POWER & LIGHT/HAWTHORNE
STATION NO. 3/RETRO
7. KANSAS CITY POWER & LIGHT/HAWTHORNE
STATION NO. 4/RETRO
.8. LOUISVILLE GAS ft ELECTRIC CO./
PADDY'S RUN STATION N0.6/RETRO
?, KANSAS CITY POWER ft LIGHT/LA CYGNE
STATION/NEW
10. DETROIT EDISON CO./ST. CLAIR
STATION NO. 6/RETRO
11. ARIZONA PUBLIC SERVICE CO./CHOLLA
STATION/RETRO
12. UNION ELECTRIC COMPANY (ST. LOUIS)/
MERAMEC NO. I/RETRO
13. DUOUESNE LIGHT CO. (PITTSBURGH)/
PHILIPS STATION/RETRO
14. TENNESSEE VALLEY AUTHORITY ftiDOK'S
CREEK STATION NO. 8/RETRO
15. NORTHERN STATES PQtfER CO. (MINNESOTA)
SHERBURNE CO. STATION NO. 1 & Z/NEN
it SOUTHERN CALIFORNIA EDISON & OTHER
SOUTHWESTERN UTILITIES/NAVAJO/NEN
if. nlBWiDA TOWERm/REID GARDNER
STATION/RETRO
18. NORTHERN INDIANA PUBLIC SERVICE CO./
D.H. MITCHELL NO. 11 (WELLMAN-LORD
PROCESS)VRETRO
20. PHILADELPHIA ELECTRIC CO./EDOYSTONE 1/RFTRO
21. POTOMAC ELECTRIC & POWER (MARYLAND)/
DICKERSON NO. 3VRETRO
r ITAI YTIP. OXIDATION
22! (LliHolsTinfERywooD RIVERVRETRO
MEGAWATTS
140
125
430
175
37
130
130
70
820
180
115
140
100
550
1360
2-680
2250
3-750
250
115
150
120
100
100
STARTUP
SEPTEMBER
1968
DECEMBER
1968
NOVEMBER
1971
FEBRUARY
1972
OCTOBER
1972
LATE 1972
LATE 1972
NOVEMBER
1972
DECEMBER
1972
DECEMBER
1973
JANUARY
1973
SPRING
1973
SPRING
1973
APRIL
1975
MAY 1976
FIRST UNIT
1-UNIT MAR. 1976
3 UNIT MAR. 1977
MID 1973
JULY 1974
APRIL 1972
MID 1973
EARLY 1974
SEPT.-OCT.
1972
FUEL
3.0% S COAL
3.5% S COAL
3.5% S COAL
3.5% S COAL
2.75% S FUEL OIL
3.5% S COAL
3.5% S COAL
3.5 S COAL
5% S COAL
3.7%-3.8% S COAL
0.4%-1% S COAL
3.0% S COAL
2% S COAL
3.7% S COAL
0.8%-1.2% S COAL
0.3-0.8% S COAL
0.5%-1.0% S COAL
3.5% S COAL
2.5% S FUEL OIL
2.5% S COAL
10% S COAL
25%
•PARTIAL FUNDING BY THE ENVIRONMENTAL PROTECTION AGENCY
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4. The total megawatts represented by these units
is about 7,500 MWe, 3,600 MWe representing systems in-
stalled on new boilers.
5. Presently, about 3,400 MWe of control capability
is scheduled to be installed as of the end of 1974, which
includes 950 MWe utilizing dry limestone injection. Since
any additional commitments would require from two to three
years for design and construction, it is not expected tnat
the actual total capacity will be much greater than that
already scheduled for 1974. The corresponding number for
1975 is about 4,000 MWe. This amount could be increased
substantially only if utilities make decisions to install
such systems between now and about mid-1973.
6. The utilities to date have committed capital
expenditures for flue gas desulfurization systems of
approximately $330 million.
B. Forecasting Applications of
Flue Gas Desulfurization Systems
Based on the results of many discussions with utilities,
manufacturers, and others, an attempt has been made to pre-
dict potential growth patterns for the application of sulfur
dioxide control systems in the electric power industry.
With many uncertainties in regulatory strategy, utility
management policy, operations experience in SOX control
demonstration plants, and the capability of the control
system vendors to deliver reliable products, these forecasts
can at best be considered as rough estimates of optimistic
schedules for application of stack gas cleaning equipment
to central station generating plants.
It is impossible to characterize these forecasts in
a simple way, other than to say that they result from the
intuitive and analytical blending of many factors: pressures
from New Source Performance Standards and the State Implemen-
tation Plans; the realities faced in the electric power
industry today, including delays in nuclear capacity and
fossil fuel shortages; and the uneven progress of equipment
manufacturers in developing SOX control devices.
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Two forecasts are presented in Tables VII-2 and
VII-3 to illustrate possible trends in the application
of SOX control equipment in the electric power industry.
Some of the guidelines used in constructing these pro-
jections are described here. The modeling was simplified
by considering only coal-fired central station electric
plants. There are several limitations implicit in this
assumption which should be mentioned. Many smaller coal-
fired plants may be converted to oil-firing, and a number
of midwestern coal-fired plants may begin burning low
sulfur Western coal instead of high sulfur coals. An
offsetting factor may be the installation of SOX control
equipment on oil-fired boilers, depending on increasing
costs of low sulfur oil.
New and retrofit SOX control equipment installations
were considered separately. It was assumed that, because
of the New Source Performance Standards and the State
Implementation Plans, all new coal-fired plants would be
equipped, if possible, with SOX control devices. In the
forecasts, this annual demand was satisfied first. The
rest of the estimated capacity of the control system ven-
dors was applied to retrofitting existing coal-fired
plants.
The pacing factors or "choke points" in these projec-
tions are two-fold: the ability of the control system
vendors to convince the utilities that they have developed
reliable systems and the ability of the vendors to initiate
quickly many new projects, to bring those systems on line
with minimum delay and adverse publicity, and to continue
to take on new projects with negligible choke effects. In
both of the projections, the potential for delays due to
shortages in engineering and skilled construction manpower
and for delays in acquiring material and equipment was
recognized.
For purposes of simplicity, the manufacturers were
grouped three categories: Vendor A group included 3 to
4 major manufacturers which have considerable experience
with SOX control and have reasonably large engineering
staff; Vendor B group included 4 to 5 manufacturers with
some experience in SOX control and with extensive experience
in some phase of air pollution control or chemical pro-
cessing; and Vendor C group included all other manufacturers,
including such organizations as TVA which engineers its
own scrubber systems.
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TABLE VII-2
FORECAST OF SULFUR OXIDE CONTROL EQUIPMENT ON ELECTRIC
POWER STATION, 1975-1980
-OPTIMISTIC SCENAFIO-
Number of Scrubbers Brought- on Line
Vendor
Type
A
B
C
Install .
Totals
Capacity
Totals,
MWe
Total Cap. ,
MWe
Cumulative,
MWe
Type l15iru2
Install. i 974
New
Retro
New
Retro
New
Retro
New
Retro
New 860
Retro 1570
,„ 4 jU
2500
197H 1976
4
ib 16
,- '-, 2 5
1 ~ 25
b 10
16 16
46 60
12,000 12,000
9,500 12,000
2i,5Uu 24,000
24,000 48,000
1977
14
45
2
35
20
16
100
12,000
20, 000
32,000
80, 000
1978
16
45
2
35
30
20
110
15,000
22,000
37,000
117,000
1979
16
59
2
45
40
20
144
15,000
29,000
44,000
161,000
1980
16
59
2
45
50
20
154
15,000
31,000
46,000
207,000
Average size of new plants assumed to be 750MW; retrofitted plants
assumed to be 200 MW.
>
Plants using dry J >;v;•_ t r
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FORECAST OF SULFUR OXIDE CONTROL EQUIPMENT ON
ELECTRIC POWER STATION, 1075-1980
-ONE YEAR DELAY SCENARIO-
Vonclor Typo Thru? Number of Scrubbers Brought on Lino
Type
A
Install. 1974
New
Retro
New
Retro
New
Retro
New
Retro
1975 1976
5 U4
10 15
5 10
r' i
r ) ••
If- 2i<
1977
16
25
25
10
16
60
1978
14
45
2
35
20
100
1979
16
45
2
35
2
30
20
110
198i
16
59
2
45
2
40
20
144
Install. New
Totals
Capacity New H6u 3750 8,2.0 12,OoO 12,000 15,000 15,000
Totals, MWe Retro 1570 3600 r>,6oO 12,003 ,'0,000 22,000 29,000
Tot. Capacity, 2430 7150 13,850 24,000 J2,0uu 37,000 44,000
MWe
Cumulative, 2500 i0,000 24,000 48,000 80,000 117,000 161,000
MWe
Average size of now plants assumed to be 750 MW; retrofitted plants
assumed to be 200 MW.
2
Plants using dry limestone imortion not included in compilation
or in projection.
This number includes TVA ' ^ ^u ,' MW Widow'b CreeK Fl.Hit
4
This number includes Nort.'it-. <. n ;M .ttes Power1 , 14uO MWe Sherburne Co.
Plant.
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The first forecast given in Table VII-2 describes
what we considered an "optimistic" scenario for the
application of SOX control devices. Critical to this
forecast is the ability, particularly of the major manu-
facturers, to expand rapidly during 1973-1974 so that
they can handle 40 or more projects at the same time.
Also critical is the requirement that utilities will
have to order the scrubbers scheduled for operation in
1975 within the next six to nine months since the time
needed to specify, fabricate, and assemble a scrubber
is 24-30 months.
The second forecast given in Table VII-3 is more
realistic than the first forecast, in that it assumes
the likelihood of delays in excess of six to nine months
before utilities begin placing substantial orders. Some
of the reasons for such delays have been described above,
but probably include evidence of long-term reliable opera-
tion with Chemico's Mag-Ox scrubber in Boston or Babcock
and Wilcox's limestone scrubber near Chicago. This second
forecast assumes that the 62 scrubber units scheduled for
1975 (under the optimistic scenario) would not be completed
until the end of 1976. Twenty-three units were assumed to
come on line in 1975 and 39 units in 1976. Thus, the
postulated expansion of the scrubber application would be
delayed by one year.
The cumulative sulfur oxide control capacity predicted
in these two forecasts is presented graphically in Figure
VII-1. From these two curves, one can see that the elec-
trical generating capacity out-fitted with SOX control
equipment may be, between 10,000 and 24,000 MWe in 1975
and between 48,000 and 80,000 MWe in 1977. While it may
be possible to use only an incremental 25-60 million tons
of high sulfur coal because of the limited availability
of SOX control devices in 1975, the amount of high sulfur
coal which could be used in 1977 may grow to 120-200
million tons.
Although projections for the use of coal during the
coming decade also vary widely, it is instructive to com-
pare the quantities of high sulfur coal which could be
used with the availability of SOX control devices pre-
dicted in these Iwo scenarios. In Table VII-4 total steam
electric coal requirements are projected and compared to
the quantities of high sulfur coal made usable with SOX
control technology. From this table, one can see that,
in the first "optimistic" scenario, the market for SOX
control equipment; would probably soften after 1977 because
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cumulative
scrubber,
install.,
MWe
220
260
180
160
140
120
80
60
40
20
0
Optimist ic
Scenario
-+
One-year delay
Scenario
74 75 76 77 78 79
YEAR
80
FIGURE VII-1
FORECASTS OF CUMULATIVE STACK GAS SCRUBBER
INSTALLATIONS
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TABLE VII-4
Comparison of High .c:uJ fur Coal Usable with SOX
Control Technology t-o Total Consumption in Steam
F, lec-t t ] c PI :ir;i <-.
JX. UVI.V
Hi qh ;-u , : ..
-..' i 1 1» 5OX
Cc
1975
1977
1980
?al Consul 'i
lO^To:
440
485
545
i
Maximum
High Sulfur Coal
Used with SOX
Control-Seen.2
KJ^tons %Usable
26
120
410
6
25
75
Consumption of coal for r.team electric i.-i^ms assumed to
grow 6% per year fror '„•;-> million tons ir !c)";0 through 1975,
drop to 5% in 19'f>-lcr? ?. rv,,1 then -I? r.j ^.- 4r - in 1978-1980.
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of the rapidly diminishing market, the higher installation
costs in the remaining smaller and older boilers and the
competition from low sulfur coal and oil conversions for
the remaining plants. It appears, however, that the mar-
ket in the second "realistic" scenario would probably
remain reasonably firm beyond 1977 with diminished "over-
shoot" capability in the control systems industry as the
retrofit market would decrease appreciably in size only
in the early 1980's. These estimates, however, do not take
into account chemical coal-cleaning processes such as
liquefaction and gasification which may become available
on a limited basis in the 1977-1980 time frame.
The question of maintaining adequate, reserve generating
capacity is a complex one, as described in Chapter VI.
Referring to Table VI-2, one can see that, on an overall
national basis, even a 10% maintenance margin might allow
as much as 40,000 MWe to be available for SOX scrubbing
system retrofit installations in 1975. SOX control for
new plants can be installed while the boiler is being con-
structed and does not require a maintenance outage for
installation. Only existing units will have to be retro-
fitted and brought on line during the spring and fall
maintenance periods at a rate not to exceed the available
maintenance margin of 40,000 MWe. For both scenarios, the
projected additions of retrofitted systems are well within
this limitation.
On the other hand, in the middle central and middle
south sections of the Nation, many utilities are equipped
only to burn coal, thus the Nation's coal-fired capacity
is concentrated in that area and the bulk of the burden
of retrofitting may fall on those utilities. Because of
the limited ability to shift large blocks of electrical
power except within power pools (as pointed out in Chapter
VI), there will probably be localized problems in these
geographical areas in bringing retrofitted SOX control
equipment on line, just as the problems of bringing nuclear
plants on line will probably continue to exacerbate the
reserve margin difficulties. The application of SOX con-
trol equipment, i.e., the slope of the cumulative capacity
curves as shown in Figure VTI-1 will decrease.
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An analysis of the direct cost r ! a sulfur oxide
control program such is incorporated in the "realistic"
scenario is given in Table VII- :>,
In summary, we feel thai d ,», extrapoJat: /:N of the current status
of stack gas clea/.u)'.) snd does n<>t atterapt to evaluate
all possible alt^n-;• i-'os for ;-"Ox pollution abatement.
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STA'iUS RiX.i;-'S uN IMPORTANT MAJOP
SGX HCRTjhHING FACILlTII.r
IN THE UNITED STATES AND ^/-PAN
VISITED riY SOCTAP MEMBKK.S
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Process; Magnesium Oxide Scrubbing with Thermal Regeneration
Process Supplier: Chemical Construction Corporation (Chemico)
Constructor;cKemical Construction Corporation
System Location; Boston Edison's Mystic Station in
Boston, Massachusetts
Conclusions and Analysis of Significance .
In April 1972, the shakedown period began for the Mag-Ox
scrubbing system on a 150 MW oil-fired boiler at Boston
Edison's Mystic Station. The venturi scrubber has operated
intermittently since then due to mechanical difficulties.
During operation, the scrubber has achieved SOj removal
efficiencies in excess ot 90% with no apparent scrubber-
related problems. The major problem has been with the
design and operation of the MgS03 crystal dryer. Redesign
of the dryer and a change of fuel to a low viscosity oil
appear to be resolving these problems. Other problems with
centrifuging the sulfite crystals from the scrubbing liquor
and properly calcining the sulfite to regenerate MgO appear
to be manageable. If new problems are not confronted, the
scrubber system should begin long-term test runs in the near
future.
This project is quite important because it will be the
first time the individual steps of scrubbing, centrifuging,
and calcining on an integrated basis for the Chemico process
have been combined. Partially funded by EPA, the project
involves not only the scrubber, centrifuge, and dryer at the
Boston Edison plant but also the calcining and acid plant at
Essex Chemical Company in Rumford, Rhode Island.
The process has not yei. oeen demonstrated on a coal-fired
plant, however, a full-scale Mag-Ox scrubber is planned for
Potomac Electric and Power's Dickerson Plant. Approximately
100 MW of the 195 MW of Dickerson Unit 3 will oe processed.
Since the plant burns coal '3% S, 8% ash), the scrubbing
facility will use one venturi scrubber to remove the particu-
late and a second to remove the SO2. The scrubber is scheduled
to start up in early 1974 ar.'i to use the calcining plant at
Essex Chemical.
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Process ; Limestone Scrubbing with Throwaway Product
Process Supplier; Babcock & Wilcox
Constructor ; Babcock & Wilcox
System Location: Commonwealth Edi . >wi, c'o.'s Will County
Station in Romeo" i i 1 ••• , Illinois
Conclusions and Analys.i -\J2f_
In February, i'llJ, the 175 M\v Commonwealth Edison
Will County Station l.'nif No. 1 .started up. The system con-
sists of two iclent i- . i parallel we i limestone scrubbing
systems, each con;.; . -, > •> , •. i a venturi for particulate
removal, followed in series by a *.urbu"Jent contact
absorber (TCA) foi sr>^ absorption, T.iis unit has operated
intermittent 1\ since .->t.trt-up and ii,..?-. generally achieved
SO2 removal ef f i c j enc; i es in the range oi 75-85%. Demister
pluggage with a soft, nr^tiike substance has been a problem;
but with automatic demister washing with make-up water via
bottom sprays, this problem area may lend itself to control.
Additional droplet disengagement space upstream of the
demister may also help alleviate the problem.
Economic disposal of sludge from this system appears to
be a problem; howe^e* , Commonwealth Edison is presently
working on this h. . -,\ \ < c, v/ith Chicagii F'lyash Company. One
of the first <- teps taken will be the installation of a
sludge t:eatiin.nt \.>U;>>, to allow disposal of sludge with a
lower watei '-< •, i ^y fvom the boiler injection mode due to
the possibili'v -. .; /,. .jj.-.-t pluggaqe • >.V ' - i> -, . This facility is considered very
important for the;- ^e ierai U.S. control situation, since the
Will County unit is typical of many coal-fired retrofit
situations. Despite the demister, mechanical and sludge
disposal problems, it appears likely that the system will be
made to operate reliably with adequate disposal of sludge
material, in the near future.
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Process; Lime Scrubbing with Throwaway Product
Process Supplier; Chemical Construction Corporation (Chemiro)
Constructor: Mitsui Miike Machinery Co.
System Location; Miike Power Station, Omuta Works, Mitsui
Aluminum Co., (near Omuta, Japan)
Conclusions and Analysis ni SijjnJJ:'ic_cii.c_e;
The SOX control system on the Miike Power Station of
Mitsui Aluminum Company, Ltd., located near Omuta in
Kyushu has exhibited reliable, essentially trouble-free opera-
tion since March 29, 1972, After its performance passed the
guarantee tests in late Apj.il, the control system has been
operated under less stringent, conditions just adequate to
meet the current Japanese SO., standarur... r\io serious chemical
or mechanical problems havf been detected in the two-stage
venturi scrubbinn .syster.
The sludge An the- d i ;;., .-,; pond app^-ir« to be settling
quite well, in fact,, nnurr. :>«•:>? ter than >:.x • i ' °nced at
U.S. facilities. ULtartu.^ .Disposal of the tnrowaway product,
a major problem : n the I . •>. , remains r opeu question.
It should be not*, i •
this system to date it v.>;
United States air polluti
design ground rules £01 th
to those of man;. • v ji !
furization systems. The
commonality: us** of exist
efficient electrostatic •
moderately-large size boi
throwaway product, arid uv
The unit takes on add.it::-
was designed based on L , -S
similar unit, us iruj <:,.\i> ±
being construct^' ' r. "• ''.e
Phillips StatKM;, '-i-li ^. t
1973.
It shou id ?,r ..,., , . •
Mitsui unit hat- no^ yet !
some question r^-iac . .u:-j :
performance to Liif• •> l;, ,
different de^ica- ...rj-if.^i >
let concentrations, ^;; :; ,
and much Mche> i)..' " : '
u
1 a
i
tc
>•;
5.he rc-iiible pertormance of
;} s i gn i f i ^ an re t o the
ontrol program, since the
spanese unit are quite similar
ur il 11 i er, r^q , r ing desul-
owing are iinorq the areas of
coal-fiit-d boiler, moderately
pi tator .•-••, installation on
(156 Mw), production of a
bility of ca 1 >:• i uai hydroxide.
signi f iranofe -since the system
chnology \Chemioo) and a
.ydroxide on a coal boiler, is
for Duquesne Light Company's
up scheduled during spring
lability of the
Also, there is
r apolating Mitsui
substantially
• higher 862 in-
'-q boiler loads,
., ; Icmg-tei
";n demon st r
*'? >al idi ti
.u -j.,1 i cat i o •
: o ; , such ::
. ' : ', h fi i c. e \ \
U! Tr:
•-it.ed
< ' ' c -
1 b W i
u, • m
\' ,"t T
; 1
.-' t
^ V,
' i'v
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Process; Soluble Sodium Scrubbing with Thermal Regeneration
(Wellman-Lord Process)
Process Supplier; Wellman Power Gas
Constructor: Mitsubishi Chemical Machinery (MKK)
System Location; Japan Synthetic Rubber
(near Chiba, Japan)
Conclusions and Analysis of Signif i.c ance ;
Successful reliable ojciation ol: the Wellman-Lord SOX
control process at Chiba for greater 1 v,c.n 9,000 hours for the
last year and a half .is considered quite significant for the
U.S. SOX control situafuu This process has been demonstrated
to reliably remove in t :•• icier r-i 90 percent of the inlet flue
gas on a 75 Mw oil-iaifi • ilei. It appears that the process
should be applicable to coal- fired boilers if fly ash removal
equipment is installed upstream of the absorber. A Northern
Indiana Power Service Co. (NIPSCO) unit, partially funded by
EPA, will evaluate such systems on a coal-fired boiler. Cost
studies indicate that capital and operating costs for a Wellman-
Lord system in the U.S. on a coal-fired boiler are not a great
deal higher than those for wet lime/limestone or magnesium oxide
scrubbing systems, which are generally considered the least
expensive of the flue gas desulfurization systems.
The major problem witn the process is the requirement for
a bleed to remove contaminants, primarily Na^SO.^. Present infor-
mation indicates about 10 percent of the total incoming sulfur
is lost as soluble Ndot-.4 T^is is undesirable from an environ-
mental viewpoint, .-. inct Cut. uro Federal regulations for waste
streams will probaMy prohibit such discharge; also, sodium
make-up costs are quite significant. However, based on an oxi-
dation retardant identified by Pumitomo, such Josses might be
reduced by 55 perct-iu. CM HIM techniques for decreasing or
eliminating this discharge- will probably have to be considered
for U.S. applications,
• Another potential pr^.r I tjrr. with this and all the other con-
centrated S02 producing plot-esses is the requirement to sell
large quantities ol lrw-v-.^ue sulfur product. Although there
• is little doubt that H;.SCS , ,.m be marketed in the U.S. in certain
• localities (near F^SO^j' users) . it does not appear that such pro-
duction can be absorbed by users if a large percentage of U.S.
I electrical utilities would produce acid. However, elemental
sulfur, which will be ptoduced in the NIPSCO unit, is another
potential product which is both storable and potentially sale-
Iable; this could ultimately be the most desirable end product
of all, including the ihrowaway sludges associated with lime/
limestone processes.
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Process; Lime Scrubbing with Gypsum Production
Process Supplier: Mitsubishi Heavy Industries - Japanese
Engineering Consulting Co.
Constructor: Mitsubishi Heavy Industries
System Location: Amagasaki Power Plant
(near Osaka, Japan)
Conclusions and Analvs':- •..'. -.. ; ua i f j . ••
!-,insai Electric
The Mitsub i :-.n i . JT-X
the Amagasaki power pS-i
i ./«.
oxi
reliable, trouble
three-month peric.
its demonstrated
high-purity gyp^-,.
CaSOs • 1/2H20.
over the last eJ i
relative to rh. .- VIM it wM
United States ;. itu.it", on 1s
low-sulfur res;
to the scrubbe-
control or; bo : ;
let concert, rat i
greater than. 20
scrubbing ay^t- . ,; r.-:
other re! ;<•'-;'• , • • ;\- in
Also, ut L li .-rat . •-., *• '. i,..-
United States ;•.•-, a i ' ne >•.
Chemico and We • ;.tu;u. • ..or ,
they are U.S. based com].
."••'-gypsum <^o,., ront i ol system on
t'L r'ansai Lii'-tiic has exhibited
:!:•; i-'ji, foi ^f.i'rciKinicit-el y a
(••'j, 1972 ri;is process with
•hnolociy . .i ,r- production of
HjC;) irs- > i •; ;-; ludge-rich in
i .: techno L-M \ hc-s been demonstrated
,'-r Liiiis: iJvp^.-j!- system treating
• •. KoY'^~! r-'' 1 ; • •' Nippon Kokan
', . '-alcixijTi -•.. ; . ,te for throwaway
I'.OL^ easily ; '-rod, either by
i altering ope.1 at. • oas . This can
sements for 'liudge disposal ponds
reclaiming of such ponds. For
c r. Ludge is transported for
i «n be reduced since a drier (lower
handled and transported to the
; t here ,
.i'a"ko ext
iuai
of
! S
:: i:-
oi ! j
3P.I\ V-i
r -i >:i> x '• ;
!.f> a a
] i a
! '' fpre -
, s gh - s
, - . - 1 r u .1 i
! t;
Me
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2 J1
r t?5 t=tin factors
<> • ."it " ons to the
• -MW boiler burns
,'(s Concentration
u j .itilities require
- i or oil with in-
. &y;-. leas generally
•:i Lerice has jiititcated lime
;-rone to sfftlir\g, plugging and
it Itiqhcr ;.;ile! SO-, concentrations,
: iruhishi • t - Inoi' .gy in the
. i i 11 i '"a" t ;cxft>xi r ed to use of
-h no logy, for exaitiple, since
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Process: EPA Prototype Test Facility - Limestone and Lime
Scrubbing with Throwaway Product
Major Contractor; Bechtel Corporation
Constructor; Tennessee Valley Authority (TVA)
System Location; TVA's Shawnee Steam Plant near Paducah,
Kentucky
Conclusions and Analysis of Significance;
The EPA prototype test facility consists of three
parallel scrubber systems, each capable of treating 30,000
acfm (lOMw) of flue gas, which are integrated into the
flue gas ductwork of an existing coal-fired boiler. Bechtel,
as the prime contractor, has designed the facility and has
overall responsibility for the test program, whereas TVA
has constructed and is operating the system. This facility
was designed for maximum flexibility; it can evaluate four
scrubber types, lime or limestone as the scrubbing medium,
various solids handling systems, and a variety of flow
configurations and a range of test conditions. The facility
has a high degree of instrumentation for control and re-
cording of data over a wide range of operating conditions.
Since the facility started up during April, 1972, it
has generated important data during air-water and sodium
carbonate testing. Recently, testing has been initiated
using limestone slurries. It is expected that such lime-
stone and subsequent lime testing will supply information
important to the design and/or operation of present and
future facilities utilizing a wet limestone or lime
scrubbing process. Such information will include: a
comparison of performance and reliability for various
scrubber types, evaluation of lime versus limestone for
effectiveness, a comparison of solid disposal techniques,
and determination of optimum operating conditions for
maximum removal efficiency and reliability.
-93-
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i R':3:.-.roi Trlsivfu? Fsrfc, a.irtn Carolina 27711
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!!tr;S/5'/'r»0.',D February 23, 1C-73
KAsft
tloa r--rj contact i-;- if you r;-:vo «ny ^u^tic^s.
1. r.--rj (;r . * rccc-.'rr 3i cr o1.1^ :}?)
pcrlo-.:.
2. !J-/iO (IT N = p-Cr'-^r 31 P- -ll^:: 3D)
S'? '-/HI -:ufr)lv to .f-:\'!t'~* o'>'; ':ut-2 in 1. ??.'<* nrcpnr^tl(••'"• of
SC~K; in*\'.'i r" 'ortc-.
I T - 1
Str-tcs :.u:t uavG cc:-.^lctGf« cat?, sutislssio.i io RD
RO r.usl: hava coriplcted data suhnission tr, i«".r.3.
"frf*i"*iTj"i3f *^f*"/*.'^c*** T */ ' ^f * ^*i/i ft 0"^ i r\v* <" ri "*'* i ^**ii*it*i f> v*vt ^^ v***^^ o y*i^ r*."i t^'7" r* 7^'v*»
Wv*t4'1*li*l ti *-* V. ' - —> ^" ' * I>- . 11 I J * t t /i sJ t \f t '••-'"•TOi.t'Ut^t I*1 I — -1 «5 i U. i-Jw I "j ^ t h*
7. R + i:-r-
:"U":;. i ., ; ".;TP c : r-.-.racio.i t nuMinhw a-;, . .-iry stS'cl'tics for
'-'Torflr--' r>v--r1 (;•:!, eccor-il-.j tc tl -.:- f:Jlc; ."in-" sc-'iO iul.i:
G. A'.'-;i:-r-: 1 - ['irot CY qjarcc.-r nir q^alUy rl.vta
b. •|3V'.'.:-'>or 1 - Second CY quarter air nv'^ity data
C, rp'r.sr- 1
t!i CY
^il^.^lnns fl.j>t..i ?,!!• -iry, ~r^ -nrml n1r ii'slity nnl:1 sur^r
U.t wo(fl
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cvory aUt: ^ossiMr; t.o hn.vc all "old" air •yj.illtv flat?., first
scr.nsrvvp.l r^r-orf. , sir! first, steer;:!, and tnird ouartcrly reports
to t!A03 !>y J'jna 15, VJ73.
flp,2 proMc'i nrv ihi^rfnr-"! tnt'i minterir.rscn of Ihn proposed
schedule, R * 120, is t:>,c- sorlotr, rl.ort'"-^ of crr-ujf-rr tiro for il-V
cosino. Tl.is ratter is no-' h^inrj Ktisdieu in dnuan.
;o sufi^'-GT; c;i::t VOM rV-r FY 74 h'.:=-'^:;t nrr?n~r-r-?nts for use of
l tcl^n'^nn service for <"••':*( tina an.! tr-criS^iittina c'atn to
•."i "V! O'l - .'! I> C ; 'i 1
you ncvo questions, pleAr>:j contact inn directly.
All of t'v? C'^i^.^ioi irvT.t^r1' rn".^*"?ct'i^l "
t.ccc.::~"'t ' •: i •'..;T-' :•(-:•".; .-..r ';.: i . ' tr.-i-v to;ji:i I.-oiii t;:j c.roa
conyrrr.ion an.J ^vst-'-'.i conv.-rsi^n cor-tr^ctfjal efforts. Please net
vc-;:r rr;r--;r, tc- hin vithi.i t'-: r^xt rrvcr.il ',:.::.•:':•;.
cc: G. J. 'Jehls
,1. C. Hoses, Jr.
A. A. SKV'rakor, or.
1. -,. n . •-. . ,-j ,.
U-.. -i . i .« . i' . .v»l I J
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UNITED STATES ENVIRONMENTAL PROTtCTIOiN AGENCY
Office of Air Quality Planning and Standards
Research Triangle Park, North Carolina 27711
SUBJECT: Review Schedule with Milestones for DATE: February 23, 1!
Transportation Control Plans
FROM: B. J. Steigerwald, Director
Office of Air Quality Planning and Standards
TO: Air and Water Program Directors
Regions I-X
States are required to submit transportation control plans on
April 15, 1973. In order to comply with the requirements of the Clean
Air Act and the Court, EPA must publish approval/disapproval notices
for transportation control plans in the Federal Register not later than
June 15, 1973. This has resulted in a very tight schedule for the
review, approval/disapproval and promulgation where necessary. The
schedule does not allow for any postponement of the publication dates
of June 15 and August 15 as appropriate. To assure that adequate
progress is being made towards achieving this requirement the following
schedule with appropriate milestones is transmitted. A detailed
discussion and tracking chart is attached for your information.
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Key milestones:
1. March
2.< April 15, 1973
3.< April 16, 1973
4. April 16, 1973
5. April 16., 1973
6. April 20, 1973
7. May 7, 1973
8. May 15, 1973
9. May 21, 1973
10. May 22, 1973
11. June 4, 1973
Plan'review starts upon »eceipt of draft
SIP; copies are sent to reviewers
States hold public hearings on SIP
Regions finish review and assessment of
public hearing transcript content
Plans received by regions
Regions begin to prepare for EPA promultjatii
in regions where no plan was submitted"
Reviewers receive SIPs
Regions receive review comments from EPA
reviewers, public, and interested parties
Regions make approval/disapproval recommen-
dations
LUPB forwards coordinated regional office
draft F.R..inputs to OAWP
OAWP forwards approval/disapproval recommen
dations and EPA p/oposed plans to EPA
Steering Committee
Final Interagency review comments are
received by OAWP
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EPA Form 1320.6 (Rev. 6-72)
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12. June 6, 1973
13. June 10, 1973
14. June 15, 1973
15. July;25, 1973
16. August 1, 1973
17. August 15, 1973
OAWP makes final approval/disapproval
decisions ,. 1
Regional Offices schedule public hearings
on EPA proposed plans
Federal Register notice of SIP approval is
published
Federal Register notice of hearings and EPA
developed plans for disapproved or inadequate
SIP is published
Regions hold public hearings on EPA plans
OAWP receives Regions' and LUPB's public
hearing assessments
EPA promulgates EPA plans
. Steigerwal
Director
Air Quality Planning
and Standards
Attachments (3)
cc: Region?.! transportation representatives
Reviewers
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ATTACHMENT I
/
Review Procedure for
State Transportation Control Plans
Plan review will start with the receipt by the Regions of the
draft SIPs which will be used for the States' public hearings. Copies
of draft SIPs shall be sent to the attached list of reviewers upon
receipt. Subsequent to the States' public hearings, to be held prior to
April 15, the regional staff shall commence review of the hearing transcripts
and assess their import. If needed, contractor assistance will be available
to aid Regions in this task. This information shall be retained and used
by the Regions as input to their eventual approval/disapproval recommendation
for SIPs.
As final transportation control plans are received the Regions will
send copies directly to the attached list of reviewers. It is anticipated
that the reviewers will return comments directly to the appropriate
regional office not later than May 7, with a copy sent directly to the
Office of Air Quality Planning and Standards, Land Use Planning Branch. All
reviews must be completed by Mav 7, including those for late plan submittals.
The Ren-'ons will formulate their recommendation to approve or disapprove
the plan by May 15. OAQPS will assist the regional offices to assure that
uniform policies will be followed in the ten regions involved in the
review procedure. Guidelines of Federal Register notices will also be
prepared during the period up to May 15 by the regional office. The OAQPS
will provide assistance to the regions prior to May 15 through contract
assistance with TRW. During this time period TRW will review the transpor-
tation strategies suomitted. Their review will aid OAQPS in the analysis of
' the1 ifflplementatioTrs-ehcdule and theHmpct"of~"ttie-conti'ol "measures-proposed.
No later than May 15 the Regions should have drafted appropriate
Federal Register notices including where necessary preliminary EPA proposals.
The Regions shoulu also prepare input which would be useabje in the
preamble and briefing memo for the approval/disapproval no'tice. This will
be du in the Office of Air Quality Planning and Standards, Land Use
Planning Branch by May 16. One Federal Register issuance for all plans
WOU]C| be the mos.|. appropriate approach. OAQPS will coordinate input from
the regional offices in regard to the preamble and briefing memo in order
to draft these items in a manner that would reflect the nationwide impact
and implications of the transportation control plans. Additional assistance
from TRW under the aforementioned contract will be utilized at this time
to describe specific features of transportation control strategies which
will serve as input for the briefing memo and the premable. These items
will be forwarded to Headquarters, OAWP, by May 21. The EPA Steering
Committee shall have this input for review by"May 22. Final interagency
review should be completed by June 4. It is emphasized that throughout
the procedure starting in March, key-Federal agencies, especially the -•
Department of Transportation, will have been brought on-board to review
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the plans. Other Federal agencies will be apprised of the status of
the plans and hence it is felt that this final interagency review will
serve as an update. ' •
June 15, 1973, 1s the date for publication of the EPA approval/dis-
approval notice in the Federal Register. If disapproved, EPA must •
promulgate a plan within two months or August 15, 1973. Throughout the |
review period OAQPS will work closely with regional offices and the scates
Involved in the review of the plans. They will follow closely the inter- m
change of information between the states and the regional offices in order I
to minimize plan disapproval. It is anticipated that through close liaison
with the states disapproval notices can be minimized. Throughout the
period of January 15 through August 15 the TRW contract assistance will •
also be available to provide on-call technical assistance to EPA and trie "
states in.the evaluation, interpretation, and corre:tion of various
transportation control measures. They will also assist in preparation of •
transportation control strategies that EPA must propose. •
%
The Land Use Planning Branch will report bi-weekly on the status of •
the transportation control plans to Headquarters. If it appears that jj
additional assistance is necessary in the regional office, the OAQPS will
be available to give either direct technical support to the regional «
office or support through the assignment of additional task orders to •
the appropriate contractor. Tasks in excess of those anticipated in the
new task order should be paid from the appropriate region's BOA funds, _
It Is important that a decision be reached quickly in the event a ™
plan ic not turned in. If it becomes apparent that the plan is to be
more than a few days late, Immediate action should be taken by the . •
regional office to prepare a transportation control plan. It is recommended m
that the region adhere to a time schedule for preparing drafts of appropriate
plans that will assure the drafts being sent to Headquarters on May 22, •
with Steering Committee review on May 22. If it becomes apparent that a |
large number of plans need to be promulgated, many mor? so than presently
expected, additional funding would be required for contractor assistance. _
It would not be possible for the OAQPS to expend a large^man-effort in the •
promulgation of EPA plans. It is anticipated that most of 'the regional
offices will be capable with contractor assistance to prepare any plans
that were necessary. However, technical assistance would be available to a •
limited extent in plan preparation. • •
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SOME ASPECTS OF EMISSION CONTROL
• IN THE
BY-PRODUCT COKE INDUSTRY
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George B. Crane
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ENVIRONMENTAL PROTECTION AGENCY
Office of Air Quality Planning and Standards
Engineering Srr^ioes Branch
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• Introduction
B This document has been issued as an aid to enforcement personnel of
Region V and should be useful to other EPA engineers. It constitutes
• , partial coverage of control of air pollution from by-product coke ovens.
The subjects covered are: (1) coke quenching and the effect of foul
I water on air and water pollution emissions, and (2) coke plant control
_ equipment manufacturers and their capabilities to install necessary
control systems.
B Subject (2) was investigated by telephone contacts with vendors.
• In most cases, company literature was available in time to be considered
in the report. Some company contacts were uncertain about the existence
• of control applications within the United States. Otherwise subject (2)
Identifies all significant coke plant control equipment manufacturers located
' in the U. S. or licensed to do business here, along with the controls
• installed or contracted, and date of startup if now under construction. The
summary of U. S. control is current as of February 1973.
Although coke quenching is described in subject (1), the available quenching
I controls are identified and located as described in subject (2). The
ordinary quench tower is not covered in this document.
It was not possible in the time available to estimate the number of ovens that
| a vendor could rehabilitate or the number of control systems that he could
install within a given time. However, the vendors' U. S. control
• installations have been identified to indicate their capabilities.
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Coke Quenching
If a coke oven contains 13 tons of coke, and if this is pushed into a car |
and quenched from 2200 to 400°F using 4,000 gallons of water at ambient «
temperature, about 14,000 pounds or 40 percent of the water will be
evaporated. This will generate about 370,000 cubic feet of steam. I
Quenching is done by water sprays in approximately 2 minutes.
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Measurements on actual quench towers by U. S. Steel show that the vapor
velocity and temperature reach a maximum of about 36 feet per second £
2
-(ft/sec) and 160°F, respectively, early in the quench. During the
remainder of the quench, there is a nearly linear drop to about 32 ft/sec
and 150°F. A volume of about 900,000 cubic feet of steam and air are
discharged from the tower during each quench. The air rushes into the
bottom of the quench tower as the hot steam and gases flow upward and out
the top. The gas velocity was measured-by dividing the cross section of
the quench tower into 16 equal area zones and taking pitot tube traverses.
Temperature was also measured in each zone.
Liquid entrainment by the above steam-air mixture should commence at a
gas velocity approaching 10 ft/sec and indeed, considerable mechanical
carry-over of quench water is always observed. There is a distribution
of particle sizes and the coarse drops fall out near the quench tower.
The net result is that more than 40 percent of the quench water is carried
out; the total amount released is that vaporized plus that mechanically
carried out. The latter may amount to 5 - 10 percent of the quench water
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• Tato of Chemicals 1n Quench Water
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m It has been common practice for coke makers to quench v/ith waste water
from coke oven by-product recovery plants. Coking coals contain varying
I . amounts of chemically combined nitrogen, sulfur, and chlorine. These are
largely volatilized in the coke oven as organic compounds and occur in the
I waste waters from the by-product recovery plant. The chlorine shows up
M as a chloride, and part of the sulfur appears as sulfate. It is costly to
remove these from the water waste. Many organic compounds also appear in
tt the water waste, to a degree depending on their degree of separation in
the by-product recovery plant. These organic chemicals can be removed by
m proper treatment of the water waste. Ammonia can occur in the free form
m (NH4OH) and in the fixed or chemically combined form (NH^CI and NH^SC^).
If lime is added by operation of the "fixed still" in the recovery
I plant, CaCl2 and CaSO^ will be in solution, the latter to the extent of
its solubility of about 2 grams/liter.
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It is evident that many chemical compounds can be present in the v/aste
J water sent to quench. Because of the highly transient phenomena and the
short time intervals involved, and because of the three-phase quenching
• system, one cannot calculate the chemical emissions due to quenching, neither
• adiabatic flash nor isothermal flash assumptions will give an accurate
picture of the situation. A rough estimate would simply say that if 40
J percent of the quench water is evaporated and 10 percent is mechanically
carried out, then 50 percent of the chemicals are evolved - perhaps somewhat
• greater for low boilers and somewhat less for the high boilers.
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T.FVISFD: 2/20/73
Table 1 gives the standard raw waste level of a coke plant, defined as
the quantity pf chemicals in the raw waste before any treatment. Obviously,
the range can be enormous, and for this reason, subsequent values that
;
I discuss may not agree with the averages of Table 1. The BOD5 item
is obtained by a standard test using v?aste-consuming bacteria and is a
measure of total organic matter that can be thus consumed. The figure
3.5 pounds represents an oxygen demand to convert to COp and H^O by bacterial
oxidation.
Table 2 shows the total coke plant effluent with the best available
treatment, i.e., the highest degree of treatment that has been reliably
achieved in an actual treatment.facility within the steel industry. This
degree of treatment may be costly for some segments of the steel industry.
Ammonia in the solution is stripped out in the "free still." Ammonia is
liberated from sulfate and chloride salts by treatment with lime and stripping
in the "fixed still." All waste streams are combined in the biological
treatment or "bug" plant. Cooling towers are employed to reduce the volume
of water to be treated. The cooling tower blowdown is sent to the biological
plant to dilute the still waste.
Table 3 shows the major waste components in an actual coke plant and their
total estimated daily flow after specified treatment. This treatment was
not the oest available. The free and fixed ammonia stills were to operate
with addition of lime to effect a 90-percent removal of ammonia. This
seems like low removal but it corresponds to 0.00016 mol fraction
(100 parts per million by weight) in the still bottoms. The combined flows of
550 gpm were to go to a trickling filter for an assumed phenol removal of
'". " /•• , .'u:]t. It ;!,i :"..!•./. ;...' • - ' • <.-
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1
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1 Table 1. STANDARD RAN LIQUID WASTE
-3
LOAD COKE MANUFACTURING"3
• • (Basis = 1 ton dry coal coked)
1 Parameters Range
~~
Water flow, gal 1400 - 4200
1
Phenol, mg/liter 5-35
| lb 0.125 - 0.875
• Cyanide, nig/liter 0.10 - 155
lb 0.0025 - 3.88
1
NH3, nig/liter 1.0 - 78
| lb 0.025 - 1.95
• BOD5, ing/liter 7 - 600
Ib - 0.175 - 15
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Average
3000
22
0.55
12
0.30
14
0.35
150
3.5
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REVISED: 2/2IV/3
Table 2. TOTAL COKE PLANT LIQUID
WITH BEST AVAILABLE TREATMENT
(Basis s 1 ton dry coal coked)
Water flow, gal
Phenol, Ib
Cyanide, Ib
Ammonia, Ib
BOD5, Ib
500
0.002
0.003
0.020
0.045
any effect on chlorides or sul fates. Oxidation of sul fides increases
the amount of sul fate.
Properly designed and operated bug plants can effect much greater phenol
removal than 60 percent. Recoveries of 90 to 95 percent can also
be made by liquid extraction, by operating on phenol -containing streams
early in the process before they are diluted with other aqueous wastes.
Whenever bug plants are used, some parallel standby or other provision
must be made for continuity of phenol removal if the phenol-consuming
bacteria are killed by shock loads, poisons, or other process irregularities.
From the data above, it is evident that economical treatment of coke
plant aqueous wastes may still leave sufficient amounts of phenols and
organics that the water is unacceptable for use in quenching. More important,
perhaps, is the fact ttiat the treatments mentioned do not remove inorganic
salts. Table 3 indicates that there are about 29,000 Ib/day of calcium
chloride and sulfate in the treated waste. In quenching with this
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I
Component
H~0 gpm
Phenols
Ammoni a
Sulfide
jSulfaue
/
Cyani de
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Cyanatcs
Chlorides
Calcium
Table 3. PROPOSED TREATMENT FOR LIQUID WASTE
FROM AN ACTUAL COKE PLANT4
(Basis = 8600 tons/day dry coal coked)
Haste. Ib/day
Before treatment
540
4,000
13,400
3,200
4,400
1,000
2,200
10,000
_
After treatment
550
.1,600
1,340
250
5,240
150
1,700
10,000
13, POO
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they are also carried out in the 5'to 10 weight-percent portion of
qucnchwater leaving as droplets, The material settling to the ground
1s washed to the rivers by rain. The same 1s true of organlcs. Also,
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a significant amount of material - especially these inorganic salts -
remains on the cooled coke. They are transferred to the blast furnace and are
more or less volatilized out of the cool top, going to the blast furnace gas
washer. This is a water washer to remove particulates from the blast
furnace gas. Volatilized organics and inorganics (CaCl2> etc.) go Into
the wash water and eventually to disposal whence they find their way into .
streams. Sulfates which do not volatilize are reduced to sulfides and
enter the blast furnace slag. On weathering, part of this slag sulfide
can be released to air as H^S.
In summary, coke quenching mainly redistributes most of the pollutants
which are originally in the quench water. A portion goes to air, part
goes to ground and thence to watercourses, part goes to blast furnace
slag and thence to air. Both air and water pollution result.
Estimated Air Pollutant Emissions During Quenching
A United Nations study gives some quench emissions based upon experiments
with aqueous wastes from byproduct coke plants. In one case, the volume
of steam was known and samples - Including condensate - were analyzed. In
the other case, a material balance was made or, the quench water. These
data are from Europe, and the quench water composition probably differs
from that In many U. S. plants. Nevertheless, I have worked the emission
figures over onto the bases of Table 3, which is 8600 tons/day of dry
coal coked. The results are shown in Table 4 and represent air emissions
8
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from a 11. S. plant coking B600 tons/day of coal 1f the quench water and
other conditions were comparable to pages 17 and 30 in reference 6.
From the same study, the probable performance of the U. S. plant with
respect to parti culates might be:
P articulate Tb/day.
Grit
No control 1,100
Control 260
Droplets
No control 22,000
Control 2,200
This amounts to about 75 percent control on grit and 90 percent control
on aqueous droplets. The study data are based on:
a. Area deposition measurements, and
b. Collection on greased plates above the quench tower.
Table 4 and the above values are all based on extrapolation of European
estimates, but they give the best estimates of which I am aware, based
on any published data. Measurements 'In the United States are needed.
.
y
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Pollutant
Table 4. AIR EMISSIONS WHEN QUENCHING
WITH COKE PLANT WASTE WATER IN U. S.
(Basis = 8600 tons/day dry coal coked)
Emissions, lb/daya
Phenol
Naphthalene
NH3
H2S
HCN
Tar
Cl-
Page 17
2100
360
1500
1000
120
120
360
Page 30
820
820
2000
4
50
960
^Assuming conditions are equivalent to those in reference 6, pages 17 and 30.
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•REVISED: 3/12/73
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• United States Suppliers of Coke Ovens and
Associated Emission Control Equipment
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Time requirements for building a grassroots coking facility, including
• by-product recovery plant and associated air and water pollution controls,
may be assessed by the actual requi rements for the 87 oven battery at
I Brown's Island, Weirton Steel Division of National Steel Corporation.
The time used was:
1. Scope of work, specifications and request for bids 3 months
| 2. Bid response and evaluation of bids 4 months
m 3. Company decision to build 3 months
4. Select 2 contractors (engineer and construct)
I and award contracts 9 months
5. Construct facilities 27 months
I Total 46 months
I Extensive repair, alteration or construction of coke oven facilities in
the United States is limited by the availability of silica brick, now
• available from only two U. S. sources, Harbison Walker and General Refractories,
• With en average projected demand of over 50,000 tons/year, the 42,000 ton/yr
U. S. manufacturing capacity is about 10,000 tons/yr deficient. Little
J . if any import from Europe, or even from Japan, seems possible. The silica
brick shortage is due to loss of the silica brick market by the disappearance
" of open hearth furnace users, and from retirement of skilled brick-shrtpe
• mold makers, who are not being replaced.
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y \REVISED: 3/12/73
Koppcrs Company Inc.
Koppers Company is the largest United States supplier of coke ovens
and by-product coke oven gas plants as well as associated air and
water pollution control equipment. The company is reported to have
built about 70 percent of the total U. S. coking capacity. During
World War I and II, Koppers had the capacity to build about a dozen
batteries at one time, although, this activity would not be entirely
simultaneous. There would be some staggering.
The following sections describe Koppers1 activities and capabilities and
do not constitute an exhaustive coverage. Only emission control methods
are identified; the reader may find descriptions and drawings in many
q
other sources.
1. EPA - AISI smokeless charging concept; gravity feed Tarry car
on a battery with single collecting main. Jones & Laughlin Steel
Corporation, Hazelwood, Pennsylvania; Granite City Steel Company,
Granite City, Illinois (latter for 1973 startup).
Further developments in EPA - AISI smokeless charging with a screw-
feed larry car plus other mechanical refinements, on ovens with 2
collecting mains. Donner Hanna Coke Corporation, Buffalo, Kew York;
Bethlehem Steel Company, Burns Harbor, Indiana; Colorado Fuel and,
Iron Corporation, Pueblo, Colorado. Weirton Steel Division of National
Steel Corporation. (Target date for startup - in spite of explosion
at site of ovens - is now June 1973. )
Retrofit of EPA - AISI concept on existing larry car at Ford Motor
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REVISED: 3/12/73
hydraulic controls by overheating clue to limitations on physical
location suggest the unsatisfactory nature of this type of retrofit.
I 2. Pipeline charging. Building 56 new 20-foot ovens with capacities
Q of 2500 tons per day of coke. Inland Steel Company, Indiana Harbor;
* , Indiana (1974 startup).
9 3. Smoke transfer pipe. Supplemental suction is created to pull
• the emissions from the oven being charged into an adjacent,Oven,
where, under oven suctions, they are collected by the oven gas collecting
• main. Jones & Laughlin Steel Corporation.
I 4. Emission control during pushing. Traveling quench car hood, directing
to a smoke collection main and scrubber. Ford Motor Company, Dearborn,
| Michigan.
I b. Emission control during pushing. Coke side hood extending
for the total length of the battery with overhead exhauster main
• going to water scrubber. Inland Steel Company, Indiana Harbor, Indiana.
| 6. Control of pushing emissions by "one spot" transfer car and
f smoke scrubber on gas cleaning locomotive system. WelrtOR Steel
Division, Weirton, West Virginia (1973 startup).
• 7. Continuous controlled quenching from a closed coke receiving hopper.
• Weirton Steel Division of National Steel, V.'airton, Heft Virginia
(1973 startup). ' ; ' ,
8. Koppers vacuum carbonate process for removal of mlfur ffojn
• '"',"i!;P PVC !"i r>":<;. "!!-!<• prOC01"'* •"' ' ' "-"v»v* <••• "•?• G? MCP^ffnlfe df ft-^
from coke oven gas, and there 'is no water pollution
13
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3/1,7/73
It operates 1n conjunction with a Claus sulfur recovery plant. The
only installation currently operating is at Donner llanna Coke,
Buffalo, New York. One at the Heirton Steel Division of National
Steel Corporation is scheduled for startup in June 1973. Other
installations have been built by other firms than Koppers.
9. Ammonia destruction process. This removes NFL ion from aqueous
waste by stripping out as NH^, followed by incineration to form N2
and HpO. Weirton Steel, Weirton, West Virginia (1973 startup);
Inland Steel Company, Indiana Harbor, Indiana (1973 startup).
10. Biological treatment. This process removes phenols and certain
other organics from coke plant aqueous wastes. A biological oxidation
occurs. Koppers claims 99 percent phenol removal is possible. They
also estimate 75 to 85 percent removal of CN. Among the plants
having this system is Weirton Steel, Weirton, West Virginia (1973
startup).
Wilputte Corporation
Wilputte is another old-line firm that has been building coke ovens in the
United States since early in the century. Until 1970, it was owned by
Semet Solvay, a subsidiary of Allied Chemical Corporation. It is now
owned jointly by Salem Corporation of Pittsburgh and Gibbons Brothers
Ltd. of England.
Wilputte is a fully integrated engineering and contracting firm specializing
in design and construction of coke ovens, coke oven machinery, and by-product
-. i . !•: c- ".-•.. :.-.?.
Since 1966, over 1200 large-capacity coke ovens have been completed.
14
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_ Among Wilputte's services to industry are:
a. Planning studies and capital budgeting for coke production
• requirements.
| b. Coke plant facility studies and survey reports for pollution
_ abatement.
c. Coke oven battery inspection.
d. Project management and field supervision for coke oven
| battery rehabilitation.
• e. Preventive maintenance programs.
• The following sections describe Wilputte's pollution control capabilities.
• 1. Automotive lid lifter and programmed charging, for most
existing coal charging cars. One now operating at Great Lakes
I Steel Division, Detroit, Michigan.
I 2. Smoke transfer pipe. A supplemental suction is created to
pull the emissions from the oven being charged into an adjacent
| oven, where, under oven suction, they are collected by th* oven
g gas collecting main. This has been tested only at the Dormer Hanna
works.
• 3. Mobile rotary continuous quencher. Prototype operated at
• Clairton plant of U. S. Steel. Wilputte says this quencher can
be built for existing battery installations.
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REVISED: 2/28/73
4. Pipeline charging. Semet Solvay Division of Allied Chemical,
Detroit, Michigan. Battery of 70 ovens.. Startup 1973. Scmet
Solvay Division prototype at Ironton, Ohio. Completed in 1970.
Another is being built for Alabama By-Products Corporation for startup
in late 1973. It will service 78 ovens.
5. Ammonia destruction. No installations to date, but Wilputte is
bidding on several units.
6. Vacuum carbonate coke oven gas desulfurization, with Claus
process to recover elemental sulfur. Clalrton unit of U. S. Steel
is operating. Several were built but not now operating, including
units for Republic Steel at Chicago and Warren, Ohio.
7. Phenol recovery. Light oil extraction process. About a dozen
units built within past 25 years. Also solvent extraction process
licensed by Jones & Laughlin Steel Corporation.
Coaltek Associates (Division of Allied Chemical Corporation)
Pipeline charging. As of February 1973, Coaltek has licensed all coke
oven builders in the world, except one, to construct pipeline chargers.
After licensing, their services to the contractor include monitoring
of process flow sheets, P and I diagrams, plant layout, specifications,
and other general guidance.
Table 5 shows the U. S. installations of pipeline charging built and
building. According to Coaltek, several studies concerning other
,o- !•'.: -iii,'.,' .<. ' ... .:.: :c. : • . V, ,; :: ,
confidence that industry has in pipeline charging.
16
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Table 5. U. S. PIPELINE CHARGING
INSTALLATIONS LICENSED BY COALTEK
Company
Ovens
Number Status
Number of
6-1nch
pipelines
Semet Solvay,
Ironton, Ohio
Semet Solvay,
Detroit
Inland Steel,
E. Chicago
Alabama By-
Products,
Birmingham
24
70
56
Existing
New
Pre'rieaters
Number Tons/hr
of coal
each
40
80
100
Startup
78
Existing
80
1970
1973
February 1974
March 1974
Coaltek claims that their process can readily be installed on batteries
built within the past 6 years; they say such ovens have the charging
pipeline entrances built in. They also Insist,.outside statements to
the contrary notwithstanding, that pipeline charging can be Installed on
most existing ovens, although it cannot be jusitifed for ovens more
than about 20 years old.
17
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Arthur G. McKee
McKce is a large engineering and construction firm which has joined with
Dr. C. Otto and Company of West Germany and Otto Construction Company of
New York to provide design, engineering, and construction services for
coke and coke by-product plants. McKee has designed numerous major
facilities for metals processing and for petroleum, chemicals, and
minerals processing.
Otto has operated in Germany for over a century and has built about
65,000 coke ovens throughout the world during that time. For the U. S.,
available information shows the followinq Otto construction: 85 ovens
in 1969 for Great Lakes Division, National Steel, Detroit; 63 ovens in
1959 for U. S. Steel at Fairfield, Alabama.
Pollution control offerings include the following:
1. Coaltek pipeline charging.
2. Otto quench car hood on the coke side. The hood covers the entire
length of the quench car track. The hood is compartmented for five
ovens per compartment and a stationary wet scrubber.
3. Three-stage movable quenching machine. For new batteries.
4. Dry coke cooling system. Pushed coke is cooled by inert gas
and auxiliary quenching.
5. Miscellaneous designs for sulfur removal from coke oven gas, for
ammonia destruction, and for phenol removal from waste water.
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Ihcro Is little Information about items 3 and 4 above. Further Invostiration
is warranted.
^ In operational responsibility, Otto handles electrical, instrumentation,
• and ordinary materials handling systems. McKee supervises construction
and Otto supervises startup.
The Iron and Steel Division of McKee has responsibility for coke plants.
I This office is in Cleveland and has about 1000 men; however, this office
also contains the Petroleum Refining and Chemical Divisions.
I
M J. E. Allen and Associates
— This company is involved in a hooded-car quench system. The first unit
• ' was developed jointly by the above; Interlake Inc. Technical Center,
• Chicago; Hanby-Allen Pollution Control Systems, Inc. (HALCON), Chicago;
and Aronetics Division of Thermotics, Inc., Houston.
Two specially equipped'cars are coupled together. The hooded quench
• car is intended to capture emissions from pushing. These are drawn
into the cleaning system on the trailer by the draft induced by a two-
• phase jet scrubber.
J A test of the unit was made in Houston using a smoke bomb. The unit has
^ been shipped to the Interlake plant, Chicago, where the first test will be
* made on actual coke ovens in April 1973.
I
Mitsubishi Chemical Industries Ltd.
i-iilsuuisiii started in I(JJ4 as a prouuccr 01 coke and tar products, but is
• now a combination of business enterprises including metal production, petroleum,
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chemical1.,, nuclear equipment, construction i qui|'.v.?rit, <,;id several others.
Mitsubishi has devolop"(i some rather olirctivp coke own controls which
seem to be available ior licencing with the UniU'H .cilni':s, hut I hove few
details. They do, hcv:evor, have a liaison office in New York at 277 Park
Avenue. The emission controls described by Mitsubishi .ire as follows:
1. Smokeless charging. Charging car with Movable but unspecified
dust collector system to prevent emissions from charging hole and
ascension pipe. According to color photographs sent by Mitsubishi,
control is excellent.
2. Smokeless pushing. A hood is attached to a coke guide to
cover the quenching car. This hood attached to a suction duct
extending the length of the battery, at a sport in the duct
depending on the oven being pushed. Gases and dust go to a
nearby scrubber. Clean gas goes to stack. Color photographs
sent by Mitsubishi indicate excellent emission control. Great Lakes
Steel Division, National Steel, Detroit, Michigan. Startup 2njd quarter
of 1973.
American Waegner-Biro Company, Inc.
Dry coke quenching was developed in Europe m?ny years ai;o and used to a
limited extent where .coal was costly and air pollution was not tolerated.
I have references to about four plants in Europe for coke capacities in
the 500 to 900 tons psr day range. A few plants in Switzerland, by other
makers, arc also applying this principle to coke or to other products.
'., •• - \* , ,- t . : ... --:,, ,.'.U . '. . , . ... ' -. , .-•-•'. ..'. ......
the direct cooling iirSiiiUiii and uLi.uincs> y.cuCij- h^wt-u ui Jiy piucesiJ.
20
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™ - ' REVISED: 3/12/73
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M Heat is then recovered from the hot exit gas by indirect hoat exchange
to water, forming useful steam.
• The Waagiuer-Biro dry coke quenching system has not been tried in the
• United States. Some critics contend there is a serious dust problem
with the product, calling for wetting and increased water to the blast
• furnaces. Others think that it can eventually become important because
of the saving of heat from the pushed coke.
To illustrate the heat savings available by gas cooling and steam
| generation, the savings may be calculated as a percentage of the heat
£ used in firing the coke ovens themselves. The heat saved by dry cooling
of coke from, say 1832° to 572°F, amounts to nearly 18 percent of that
I used to fire the ovens. The overall heat transfer efficiency was taken as
85 percent.
I
m Tailor and Company, Inc.
This company 1n Bettendorf, Iowa, is developing a pneumatic preheated coal, oven
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injection process, including a locking, self-cleaning oven charge port. The
process seems complex and, to my knowledge^it has not vet been
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REVISED: 3/12/73
1. Crane, G. B. to Megonnell, W. H. Trip Report: Fairfield Works of
U. S. Steel Corporation at Birmingham, Alabama. October 7, 1971.
/'
2. Fuller-ton, R. H. Impingement Baffles to Reduce Emissions from Coke
Quenching. JAPCA V7: 12, 807 - 809 (1967).
3. Industry Profile StuJy on Blast Furnace and Basic Steel Products.
Contract 68-01-0006. Water Quality Office, Environmental
Protection Agency. December 1971.
4. Crane, G. B. to Megonnell, W. H. Meeting Report: U. S. Steel and OAP
Personnel at Raleigh, December 29, 1971.
5. Crane, G. B. to Cuffe, S. T. Trip Report: Meeting with United
States Steel Personnel at Department of Justice, Washington, D. C.
November 2, 1971.
6. United Nations Study ST/ECE Coal 26, pp. 17 and 30.
7. Personal communication, Norman Plafcs, CSD, OAQPS, EPA.
8. Personal communication, Edward Gibbs, Marketing Manager, Koppers
Company.
9. Edgar, W. D. Coke Oven Air Emissions Abatement. Iron and Steel
Engineer., pp. 86 - 94 (October 1972).
10. Brochure, Sulzer Dry Coke Cooling, Sulzer Brothers Limited,
Winterthur (Switzerland).
22
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GUIDELINE SERIES
OAQPS NO. 1.2-002
GUIDANCE FOR WRITING OF
TRANSPORTATION CONTROL PLANS
5OC
VS. ENVIRONMENTAL PROTECTION AGENCY
Office of Air Quality Planning and Standards
Research Triangle Park, North Carolina
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UNITED STATES ENVIRONMENTAL PROTECTION AGENCY
Office of Air Quality Planning and Standards
Research Triangle Park, North Carolina 27711
rajECT: Transportation Controls DATE: March 12, 1973
FROM-. Ronald A. Vonezia, Chief , /
Land Use Planning Branch A m
TO: Air and Water Program Directors
Regions I-X
At the Kansas City regional meeting on February 9, 1973, it was
indicated that the OAQPS would assist the Regions with guidance in
the preparation of transportation control plans that must be proposed
and promulgated by EPA.
A review of the SIP task schedule sent to you on February 23
points out the extremely short time period available for the prepara-
tion of EPA plans after a decision is made as to whether or not the
State plan is acceptable. To fully think out, prepare, review, and
announce on June 15 an EPA plan proposal with only one month lead
time is very difficult. To assure adequate preparation and review of
EPA proposed plans, the following is recommended.
The regional offices should prepare a contingency EPA proposal
for transportation controls in each Region requiring these controls
to meet NAAQS by 1975. OAQPS 1.2-002, "Guidance for Writing Transpor-
tation Plans," is provided to assist the Regions in writing the plans.
This information should serve only as a guide. EPA policy on use
of gasoline rationing and the extent to which states will be required
to enforce EPA promulgated regulations are not yet finalized. There-
fore, to the extent sample regulations imply a particular enforcement
policy or a preferred strategy, they should be considered preliminary
until further policy guidance is recommended.
Included is a list of items that should be included in the pream-
ble. It is important that all these points be covered for the prepara-
tion of a comprehensive preamble. Preambles for Regions' proposals
will be coordinated by the Land Use Planning Branch for the single
preamble to cover all EPA plans proposed on June 15. The Land Use
Planning Branch is developing an additional listing of strategies and
priorities which can be used in EPA plans, and will attempt to
identify preferred strategies that would be most appropriate for EPA
proposal and promulgation in each Region.
*
Close attention should be given to the memorandum "Enforceability
of Transportation Control Strategies," 3-2-73, Shutler to Regional Air
and Water Programs Division Directors. Mr. Graham prepared an excellent
analysis of the potential for state and/or Federal enforcement. It is
intended that the sample plan be modified to suit each particular
Region using Mr. Graham's work and the preferred strategies from the
EPA Form 1320-6 (Rev. 6-72)
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Land Use Planning Branch. This information will be available
March 20. At that time the Region should review the proposal,
determine if it suits regional needs and prepare an outline of the
"back-up" EPA plan for each AQCR. This will be held in reserve to
finalize as an EPA proposal if states do not submit an adequate plan.
Mr. Frick, of OGC, is preparing a document on the basis for ex-
tensions to meet the NAAQS. It is expected it will be available by
March 20.
The following policy issue papers are now in preparation by the
Land Use Planning Branch for consideration by the Administrator.
These issues will become an integral part of EPA policy to achieve
transportation controls.
1. Should an EPA promulgated plan make maximum use of
gasoline rationing? How much rationing can be
effected without severe community impact?
2. Should EPA write regulations to force the states to
act or should EPA act directly?
It is anticipated that we will be able to discuss these issues
in some depth at the March 20 meeting. A decision will be reached
as soon as possible.
An evaluation report must be prepared for transportation and or
land use plans that are received from the States. The Land Use
Planning Branch has prepared a checklist (OAQPS 1.2-003) which can be
used in the evaluation of the plans and serve as the basis of writing
the evaluation report. A copy of this report should be sent to the
Land Use Planning Branch no later than May 15, 1973.
For your review of the State plans, your attention is called to
the following references:
1. "Requirements for Preparation, Adoption and Submittal of
Implementation Plans." (36 FR 15486) August 14, 1971.
2. "Criteria for Review of Transportation Control Measures."
OD/OAQPS January 30, 1973.
3. "Proposed Transportation Control Measures." (38 FR 1464)
January 12, 1973.
If you have further questions on transportation controls, please
contact the Land Use Planning Branch (919) 688-8291 or 8270.
Attachments
OAQPS 1.2-002
OAQPS 1.2-003
cc: Transportation representatives
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• March 12, 1973
I
£ OAQPS NO. 1.2-002
• Guidance for Writing of
Transportation Control Plans
This appendix includes the following sections:
I
I. Items to be Included in the Preamble
• II. Suggested Wording for Opening of Preamble
III. Sample Wording for Possible Regulations
• IV. Current Studies and Guidelines Applicable to Plan Preparation
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• I. Items to be included in Preamble
• The preamble to the control regulations should contain the following
im items:
1. Percent pollutant reduction required: a statement as to the
I percent reduction required of oxidants or carbon monoxide
to meet the national primary ambient air quality standard
I by May 31, 1975.
a 2. Background: a brief description of the history and legislation
leading to the requirement for EPA to promulgate a control plan,
I (See Section II). Also a description of the topography and
meteorology of the region in question and a statement describing
| the reason (health basis) for the NAAWS. Describe the base air
M quality data and compare it with the national standards.
3. Transportation and/or land use control alternates: describe the
I control strategies available for the region in question such
as (a) stationary source controls (restrictions on organic solvent
| use, gasoline vapor recovery systems for service stations, a
• change in the substance used for degreasing operations, and a
vapor recovery system that prevents evaporation of solvents from
• dry cleaning operations;) (b) hardware type mobile source controls
(inspection and maintenance, retrofit and fuel conversion,
• evaporative controls to prevent evaporation of gasoline during
• the filling of the gas tank; (c) reduction of vehicle miles
traveled (increased use of mass transit, increased car pooling,
I gasoline rationing, increasing cost of motor vehicle use, limiting
the number of automobiles registered, land use controls or a
' combination of these.) I
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4. The specific transportation and/or land use control strategy
proposed to meet NAAQS by May 31, 1975.
5. Include a table summarizing the effect of each element of the
proposed strategy as is shown on page 2196 of the January 22,
1973 proposed plan for Los Angeles, 38 FR (2194).
For the following items see the January 22, 1973 Federal Register:
6. Discuss legal and administrative procedures to implement the
plan.
7. Include compliance schedules.
8. Discuss surveillance and monitoring procedures.
9. Economic and social impact of the (name of Region) transportation
and/or land use plan.
10. Direct costs to the public.
11. Effect on the economic fabric of the community.
12. Tax revenue implications.
f
13. Summary of impacts.
14. EPA efforts to mitigate the effects of proposed regulations
15. The need for mass transit (if applicable).
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II. Suggested Wording for Opening of Preamble
ENVIRONMENTAL PROTECTION AGENCY
• [40 CFR Part 52]
Approval and Promulgation of Implementation Plans
• Notice of Proposed Rule Making
I
On May 31, 1972 (37 FR 10842), pursuant to section 110 of the Clean
| Air Act and 40 CFR Part 51, the Administrator approved, with specific
• exceptions, State plans for implementation of the national ambient air
quality standards. On this date, the Governor of
• was advised that in order to complete the requirements of § 51.11 (b)
and 51.14, a transportation and/or land use control strategy was to be
| submitted to the Administrator by February 15, 1973.
On January 31, 1973, the United States Court of Appeals for the
District of Columbia Circuit found that the Administrator did not conform
• to the strict requirements of the Clean Air Act of 1970 in permitting
several states to delay submission of transportation control portions
I of their implementation plans until February 15, 1973, and in granting
m extensions until mid-1977 for attainment of the national primary ambient
air standard without following the procedures established in Section
I 110 (3) 42 V.S.C. § 1857 c-5 (e). Accordingly the court ordered that the
Administrator rescind the extension granted the states for implementation
• of the transportation and/or land use control portion of their imple-
• mentation plans. The affected states were required to submit a control plan
by April 15, 1973. The plan was to show attainment of the national ambient
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air quality standards for oxidant and/or carbon monoxide as expeditiously
as possible but no later than May 31, 1975.
On this day the Administrator approved, with specific exceptions,
transportation and/or land use control plans submitted in response to
the January 31, 1973 court order. This proposal results from the failure
of the State of to submit an acceptable control
plan for the attainment and maintenance of the national primary ambient
air quality standard for oxidants and/or carbon monoxide.
III. Sample Wording for Possible Regulations
The following sample regulations should be modified to fit the AQCR
in question. This also induces the paragraph numbering system. Example
regulations follow the format shown in (38 FR 2194) dated January 22, 1973.
a. The preferred approach to be used by EPA in promulgating regula-
tions such as those on gasoline rationing (Section II f) have not
been finalized. Therefore these regulations and the strategy
implied by their use may be revised as EPA policy on preferred
strategies arid enforcement are further developed.
b. Subpart (name of state)
Section is amended by adding paragraphs
through , as follows: § 52 control strategy and
regulations: Photochemical oxidants and/or carbon monoxide,
AQCR.
Regulation for control of evaporative emissions.
(1) For purposes of this paragraph:
(i) "Evaporative control device" means a device installed on a
motor vehicle to prevent the escape of gasoline vapor from
the gasoline tank and carburetor.
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™ (ii) "Registered" as applied to a motor vehicle, means that such
• motor vehicle, is duly licensed
for general operation on public roads or highways by the
| appropriate agency of the Federal Government or by the State.
^ (2) This regulation is applicable in those portions of
Counties contained within the Metropolitan
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Air Quality Control Region (AQCR) in the State of
The requirement of this regulation shall be effective
commencing up to _ •
_ (3) Prior to (date) _ , an evaporative control device of at
least 85 percent efficiency which is approved by the
I Administrator shall be properly installed, in good working
order, and in operation on all registered light-duty
| gasoline-powered vehicles of model years 1966 through 1969
m and all registered heavy-duty gasoline vehicles of model
years 1966 through 1972. Approved evaporative control
• - devices shall be installed on a schedule determined by the
Administrator.
• (4) After (date) , the following shall apply in the areas
• specified in paragraph (b) (2), of this section:
(i) The State of _ shall not register light-duty
• vehicles which do not comply with the provisions of
paragraph (b) (3) of this section.
• (ii) No owner of light-duty vehicles shall operate or allow
• the operation of such vehicles which do not comply with
the provisions of paragraph (b) (3) of this section.
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c. Regulation for gaseous fuel conversion.
(1) For purposes of this paragraph:
(i) "Fleet vehicle" means any one of ten (10) or more light-and
heavy-duty vehicles operated by the same person (s) or
business and used principally in connection with the same
occupation or related occupations.
(ii) "Gaseous fuel" means liquified or pressurized petroleum
or natural gaseo which are used as fuel for light-duty
vehicles.
(2) This regulation is applicable in those portions of
Counties contained within the Metropolitan Air
Quality Control Region (AQCR) in the State of ,
The requirements of this regulation shall be effective
commencing on (date) .
(3) All registered gasoline-powered fleet vehicles of model years
prior to 1975 shall be equipped for and operated on gaseous
fuel by the effective date of this regulation. Conversion of
such fleet vehicles for use of gaseous fuel shall be on a
schedule determined by the Administrator.
(A) After (date) , the following shall apply in the areas
specified in paragraph (c) (2) of this section:
(i) The State of shall not register vehicles
which do not comply with the provisions of paragraph
(b) (3) of this section.
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| (ii) No owner of fleet vehicles shall operate or allow the
_ ' operation of such vehicles which do not comply with the
provisions of paragraph (c) (3) of this section.
I d. Regulation for yearly inspection and maintenance.
(1) For purposes of this paragraph:
| "Inspection and maintenance" means a program to reduce
•I emissions from in-use vehicles through identifying vehicles
that need emissions control related maintenance and requiring
• that maintenance be performed.
(2) This regulation is applicable in those sections of
• Counties contained within the Air Quality
• Control Region (AQCR) in the State of . The
requirements of this regulation shall be effective commencing
• °n (date)
(3) All registered gasoline-powered light- and heavy duty vehicles
• shall be inspected annually for emissions and, as necessary,
• maintained by the owner in order to pass the inspection. This
shall be done by personnel, facilities and procedures which shall
• be proposed and promulgated by the Administrator.
(4) After (date) , the following shall apply in the areas
^ specified in paragraph (d) (2) of this section:
• (i) The State of shall not register light-duty
vehicles which do not comply with the provisions of
• paragraph (d) (3) of this section and procedures promul-
gated pursuant thereto.
™ (ii) No owner of light-duty vehicles shall operate or allow
• the operation of such vehicles which do not comply with
the provisions of paragraph (d) (3) of this section.
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Regulation for oxidizing catalyst.
(1) For purposes of this paragraph:
"Oxidizing catalyst" means a device installed in the exhaust
system of the vehicle that utilizes a catalyst and, if
necessary, an air pump to reduce emissions of hydrocarbons and
carbon monoxide from that vehicle.
(2) This regulation is applicable in those sections of
Counties contained within the AQCR in the state
of . The requirements of this regulation shall
be effective commencing on (date) .
(3) All registered gasoline-powered light- and heavy duty motor
vshicles of model years 1966 through 1974, shall be equipped
with an appropriate oxidizing catalyst exhaust retrofit in
accordance with paragraph (e) (2) of this section, approved
by the Administrator.
(4) After, , the following shall apply.in the areas
specified in paragraph (e) (2) of this section:
(i) The State of shall not register light-
duty vehicles which do not comply with the provisions
of paragraph (e) (3) of this section.
(ii) No owner of light-duty vehicles shall operate or allow
the operation of such vehicles which do not comply with
the provisions of paragraph (e) (3) of this section.
f. Regulation for purchase of gasoline.
(1) For purposes of this paragraph:
(i) "Control period" means a portion of a calendar year in which
gasoline sales are regulated.
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(11) "Retail outlet" means any service station, filling station,
garage, store or other place of business at which gasoline
<• is transferred directly to consumers in the regular course
| of business.
'• (2) This regulation is applicable in those portions of
|_ Counties contained within the Air Quality Control
'• Region (AQCR) in the State of . The
• requirements of this regulation shall be in effect commencing
j ^*
(date) and shall remain in effect through (date)
The regulation shall be effective in the same control periods
,_ during each calendar year thereafter, until such time as the
Administrator determines the regulation to be no longer
:• necessary for the attainment and maintenance of the national
standard for photochemical oxidants (hydrocarbons and/or
i | carbon monoxide.)
:• (3) During the control periods, as specified in paragraph (f)
(2) of this sections the sale of gasoline to retail outlets
• and to the owners and operators of motor vehicles shall be
S controlled by directions of the Administrator, EPA.
.I (4) The amount of gasoline to be controlled shall be determined
/
1• by the Administrator no later than 30 days prior to the
effective date of a control period. This determination shall
• be based on the hydrocarbon emission reduction required for
the attainment and maintenance of the national standard for
• photochemical oxidants and/or carbon monoxide in the AQCR.
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g. Volatile organic compound loading facilities.
(1) This regulation is applicable in those portions of
Counties contained within the
Air Quality Control Region (AQCR) in the State of
. The requirement of paragraph (g) (2) of
this section shall be effective commencing
(2) No person shall load or allow the loading of volatile organic
compounds having a vapor pressure of 1.5 pounds per square
inch absolute or greater, under actual storage conditions,
into any tank truck or trailer, railroad tank car, loco:mctive,
aircraft, stationary storage tank with a capacity greater
than 5 gallons from any loading facility unless such tank or
loading facility is equipped with a vapor collection and
disposal system, or its equivalent, properly installed, in
good working order, and in operation. Loading shall be
accomplished in such a manner that all displaced vapor and air
will be vented only to the vapor disposal system. A. means
shall be provided to prevent liquid organic compound drainage
from the loading device when it is removed from the hatch, or
to accomplish complete drainage before such removal. The
vapor disposal portion of the system shall consist of one
of the following:
(i) An absorber system or condensation system with a minimum
recovery efficiency of 90 percent by weight of all the
volatile organic compound vapors and gases entering such
disposal system.
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• (11) A vapor handling system which directs all vapors to a
fuel gas system.
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(111) Other equipment of at least 90 percent efficiency,
• provided plans for such equipment are submitted to and
approved by the Air Pollution Control Officer.
• Intermediate storage vessels may be used prior to disposal
of vapors under paragraph (g) (2) (1) , (ii) , or (ill) ,
• provided they are so designed as to prevent release of
• vapors at any time during use.
(3) Notwithstanding paragraph (g) (2) of this section, no person
• loading or allowing the loading of the above specified
compounds in the above. specified storage vessels from the
I above specified loading facilities, any of which were in
V existence on the effective date of this regulation, or in
the procers of being installed for use on said effective date,
• shall be subject to the provisions of paragraph (g) (2)
of this section until (date) . Provided however,
Jj that such person is hereby required to file on or before
_ (date) a compliance schedule with the Administrator
showing how the person will bring this operation into
I compliance with paragraph (g) (2) of this section on or
before (date) . Failure to file such compliance
| schedule or abide by its items shall render the
m prohibition contained in paragraph (g) (2) of this section
immediately applicable to such person on _ (date) _ ,
• or on the date of said person's failure to abide by said
compliance schedule, whichever is later.
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h. Control of drycleanlng solvent evaporation.
(1) For the purposes of this paragraph:
"Drycleaning operation" means that process by which an
organic solvent is used in the commercial cleaning of
garments and other fabric materials.
(2) This regulation is applicable in those portions of
Counties contained within the
Air Quality Control Region (AQCR) in the State of
. The requirements of this regulation shall
be effective commencing on (date) .
(3) No person shall operate a drycleaning operation unless the
uncontrolled organic emissions from such operation have
been reduced at least 85 percent.
(4) Drycleaning operations emitting less than three (3) pounds
per hour and less than 15 pounds per day are exempt from
this regulation.
(5) If incineration is used as a control technique, 90 percent
or more of the carbon in the organic compounds being
incinerated must be oxidized to carbon dioxide.
i. Decreasing operations.
(1) For the purpose of this paragraph:
"Degreasing" means the operation of using an organic solvent
as a surface cleaning agent prior to fabricating, surface
coating, electroplating or any other process.
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* (2) This regulation is applicable in those portions of
I Counties contained within the Air Quality
Control Region (AQCR) in the State of
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| The requirements of this regulation shall be effective
_ commencing on (date) .
(3) No person shall use trichloroethylene (TCE) degreaser as a
• degreasing solvent.
j. Organic Solvent Usage.
| Contact the Land Use Planning Branch for additional information
« on this subject. Work is currently being done to revise
Appendix "B" of the August 14, 1971, Federal Register. 36 F.R.
• (15486.)
IV. Current Studies and Guidelines Applicable to Plan Preparations
The EPA has published the following studies and guidelines:
a. "Prediction of the Effects of Transportation Controls on Air
• Quality in Major Metropolitan Areas" and "Evaluating Controls
to Reduce Motor Vehicle Emissions in Major Metropolitan Areas,"
| November 1972. Both of these documents are generally known as
« the "Six Cities Study."
b. "Transportation Controls to Reduce Motor Vehicle Emissions in
• . Major Metropolitan Areas," December, 1972. This document is a
summary of 14 cities that were studied with the view of
• recommending specific transportation control strategies.
• Separate reports for each of the 14 cities will also be
available alo.ig with the Six Cities Study and the document
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listed in b above from the Office of Technical Information and
Publications, Research Triangle Park, North Carolina 27711.
c. "Control Strategies for In-Use Vehicles," November, 1972. This
report is available from EPA, Mobile Source Pollution Control
Programs, 401 M St.S.W., Washington, D.C. 20460.
d. "Proposed Transportation Control Plans," Federal Register
(38 FR 1464) January 12, 1973.
e. "An Air Pollution Impact Methodology for Airports and
Attendant Land Use," dated January, 1973. Copies available
from Land Use Planning Branch, EPA, Research Triangle Park,
North Carolina 2771.1.
f. "Criteria for a Review of Transportation Control Measures"
OD/OAQPS Memo, January 30, 1973.
g. "An Interim Report on Motor Vehicle Emission Estimation" Kircher
and Armstrong, October, 1972 and available from the Land Use
Planning Branch, EPA, Research Triangle Park, North Carolina 27711.
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GUIDELINE SERIES
OAQPS NO. 1.2-003
CHECKLIST FOR EVALUATION OF
TRANSPORTATION PLANS
DOC
US. ENVIRONMENTAL PROTECTION AGENCY
Office of Air Quality Planning and Standards
Research Triangle Park, North Carolina
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UNITED STATES ENVIRONMENTAL PROTECTION AGENCY
Office of Air Quality Planning and Standards
Research Triangle Park, North Carolina 27711
SUBJECT: Transportation Controls
DATE: March 12, 1973
FROM: Ronald A. Venezia, Chief .-> .,
Land Use Planning Branch *• l
TO: Air and Water Program Directors
Regions I-X
At the Kansas City regional meeting on February 9, 1973, it was
indicated that the OAQPS would assist the Regions with guidance in
the preparation of transportation control plans that must be proposed
and promulgated by EPA.
A review of the SIP task schedule sent to you on February 23
points out the extremely short time period available for the prepara-
tion of EPA plans after a decision is made as to whether or not the
State plan is acceptable. To fully think out, prepare, review, and
announce on June 15 an EPA plan proposal with only one month lead
time is very difficult. To assure adequate preparation and review of
EPA proposed plans, the following is recommended.
The regional offices should prepare a contingency EPA proposal
for transportation controls in each Region requiring these controls
to meet NAAQS by 1975. OAQPS 1.2-002, "Guidance for Writing Transpor-
tation Plans," is provided to assist the Regions in writing the plans.
This information should serve only as a guide. EPA policy on use
of gasoline rationing and the extent to which states will be required
to enforce EPA promulgated regulations are not yet finalized. There-
fore, to the extent sample regulations imply a particular enforcement
policy or a preferred strategy, they should be considered preliminary
until further policy guidance is recommended.
Included is a list of items that should be included in the pream-
ble. It is important that all these points be covered for the prepara-
tion of a comprehensive preamble. Preambles for Regions' proposals
will be coordinated by the Land Use Planning Branch for the single
preamble to cover all EPA plans proposed on June 15. The Land Use
Planning Branch is developing an additional listing of strategies and
priorities which can be used in EPA plans, and will attempt to
identify preferred strategies that would be most appropriate for EPA
proposal and promulgation in each Region.
Close attention should be given to the memorandum "Enforceability
of Transportation Control Strategies," 3-2-73, Shutler to Regional Air
and Water Programs Division Directors. Mr. Graham prepared an excellent
analysis of the potential for state and/or Federal enforcement. It is
intended that the sample plan be modified to suit each particular
Region using Mr. Graham's work and the preferred strategies from the
EPA Form 1320-6 (Rev. 6-72)
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Land Use Planning Branch. This information will be available
March 20. At that time the Region should review the proposal,
determine if it suits regional needs and prepare an outline of the
"back-up" EPA plan for each AQCR. This will be held in reserve to
finalize as an EPA proposal if states do not submit an adequate plan.
Mr. Frick, of OGC, is preparing a document on the basis for ex-
tensions to meet the NAAQS. It is expected it will be available by
March 20.
The following policy issue papers are now in preparation by the
Land Use Planning Branch for consideration by the Administrator.
These issues will become an integral part of EPA policy to achieve
transportation controls.
1. Should an EPA promulgated plan make maximum use of
gasoline rationing? How much rationing can be
effected without severe community impact?
2. Should EPA write regulations to force the states to
act or should EPA act directly?
It is anticipated that we will be able to discuss these issues
in some depth at the March 20 meeting. A decision will be reached
as soon as possible.
An evaluation report must be prepared for transportation and or
land use plans that are received from the States. The Land Use
Planning Branch has prepared a checklist (OAQPS 1.2-003) which can be
used in the evaluation of the plans and serve as the basis of writing
the evaluation report. A copy of this report should be sent to the
Land Use Planning Branch no later than May 15, 1973.
For your review of the S.tate plans, your attention is called to
the following references:
1. "Requirements for Preparation, Adoption and Submittal of
Implementation Plans." (36 FR 15486) August 14, 1971.
2. "Criteria for Review of Transportation Control Measures."
OD/OAQPS January 30, 1973.
3. "Proposed Transportation Control Measures." (38 FR 1464)
January 12, 1973.
If you have further questions on transportation controls, please
contact the Land Use Planning Branch (919) 688-8291 or 8270.
Attachments
OAQPS 1.2-002
OAQPS 1.2-003
cc: Transportation representatives
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• OAQPS NO. 1.2-003
- CHECKLIST FOR EVALUATION OF
' TRANSPORTATION PLANS
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March 12, 1973
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3/12/7J
APPENDIX B
Checklist for Evaluation of Plans
INTRODUCTION
The following check list for use in review of State Air
Quality Implementation Plans was compiled and edited from infor-
mation available from the following sources:
Federal Register, Volume 36, Number 228 (11/25/71)
Sierra Club v. Ruckelshaus, U.S. District Court, D.C.,
Number 1031-72 (6/2/72)
Federal Register, Volume 38, Number 8 (1/12/73)
Natural Resources Defense Council, Inc., et al. v.
Environmental Protection Agency, U.S. Ct. Appeals, D.C.,
Number 1522-72, et al. (1/31/73)
« Federal Register, Volume 38, Number 21 (2/1/73)
The check list retains the Code of Federal Regulations
article numbering system and part and subpart headings. Where
reference is made within a check list item to appendices or
articles not presented in the check list that inforamtion will
be found in the November 25, 1971, Federal Register unless
noted otherwise.
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Subpart B - Plan Content and
Requirements
§ 51.10 General requirements.
(b) Each plan implementing a pri-
mary standard shall provide for the
attainment of such standard as ex-
peditiously as practicable, but in no
case, except as otherwise provided by
Gv.bpnrt C of this part, later than
May 31, 1975. The projected date of
attainment of such standard shall be
specified in the plan.
(c) Each plan implementing a sec-
ondary standard shall provide for the
attainment of such standard by a speci-
fied date, which shall be within a rea-
sonable time after the date of the
Administrator's approval of such plan.
(d) The plan for each region shall
have adequate provisions to insure that
pollutant emissions within such region
will not interfere with attainment and
maintenance of any national standard
in any portion of an interstate region
or in any other region
(e) Each plan shall provide for pub-
lac availability of emission date re-
ported by source owners or operators or
otherwise obtained by a State or local
agency. Such emission data shall be
correlated with applicable emission
limitations or other measures. As
used in this paragraph, "correlated"
means presented in such a manner as to
show the relationship between measured
or estimated amounts of emissions and
the amounts of such emissions allow-
able under the applicable emission
limitations or other measures.
Not
Applicable
9
rH
a FM
•H
r-l
T3 (0
-H
0 M
O O
Covered in
Transportation Plan
Missing
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§ 51.11 Legal authority.
(a) Each plan shall show that the
State has legal authority to carry out
the plan, including authority to:
(1) Adopt emission standards and
limitations and any other measures
necessary for attainment and main-
tenance of national standards.
(2) Enforce applicable laws, regu-
lations, and standards, and seek
injunctive relief.
(3) Abate pollutant emissions on
an emergency basis to prevent sub-
stantial endangerment to the health
of persons, i.e., authority compare-
able to that available to the Admin-
istrator under section 303 of the Act.
(4) Prevent construction, modifica-
tion, or operation of any stationary
source at any location where emissions
from such source will prevent the
attainment or maintenance of a national
standard.
(5) Obtain information necessary to
determine whether air pollution sources
are in compliance with applicable laws,
regulations, and standards, including
authority to require recordkeeping and
to make inspections and conduct tests
of air pollution sources.
(6) Require owners or operators of
stationary sources to install, main-
tain, and use emission monitoring
devices and to make periodic reports
to the State on the nature and amounts
of emissions from such stationary
sources; also authority for the State
to make such data available to the
public as reported and as correlated
with any applicable emission standards
or limitations.
Not
Applicable
Covered in
Original Plan
Covered in
Transportation Pis
Missing
3
Remarks
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(b) Where a plan sets forth a control
strategy that provides for application
of (1) inspection and testing of motor
vehicles and/or other transportation
control measures or (2) land use
measures other than those referred to
in § 51.11 (a) (4), such plan shall set
forth the State's timetable for obtain-
ing such legal authority as may be
necessary to carry out such measures.
(c) The provisions of law or regula-
tion which the State determines provide
the authorities required under the sec-
tion shall be specifically identified,
and copies of such laws or regulations
shall be submitted with the plan.
(d) (1) Except as otherwise provided
by paragraph (b) of this section, the
plan shall show that the legal authori-
ties specified in this section are
available to the State at the time of
submission of the plan.
(2) Legal authority adequate to
fulfill the requirements of paragraph
(a) (5) and (6) of this 'section may be
delegated to the State pursuant to
section 114 of the Act.
(e) A State governmental agency other
than the State air pollution control
agency may be assigned responsibility for
carrying out a portion of a plan: Pro-
vided, That such plan demonstrates, to
the Administrator's satisfaction, that
such State governmental agency has the
legal authority necessary to carry out
such portion of the plan or, pursuant
to paragraph (b) of this section, has a
timetable for obtaining such authority.
(f) The State may authorize a local
agency to carry out a plan, or portion
thereof, within such local agency's
jurisdiction: Provided, That such plan
demonstrates, to the Administrator's
satisfaction, that such local agency has
the legal authority necessary to implement
such plan, or portion thereof, and further:
Not Applicable
Covered in
Original Plan
Covered in
Transportation Plan
Missing
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Provided, That such auth'
not relieve the State of
under the Act for carryL
or portion thereof.
§ 51.12 Control strategy
(a) In any region wlv
(measured or estimated)
of a pollutant exceed tb
by an applicable nation
plan shall set forth a
which shall provide I
emission reduction necu.
ment and maintenance of
standard, including the
sion reduction necessar-
sion increased that can
expected to result from
of population, industri,
vehicle traffic, or oth,
cause or contribute to '<
(b) In any region w.i
estimated ambient level:
are below the levels sp.
plicable secondary star
shall set forth a contr
shall be adequate to pi
pollution levels from I
deteriorated.
(d) For purposes of
trol strategy, data del-
men ts of existing ambJc
pollutant may be adjust
extent to which occasic.
accidental phenomena, <
forest fires, industri.
demonstrably affected
levels during the measu
,hall
Uity
i plan
•els
;>ecified
s the
.tegy
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tain-
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•mis-
emis-
be
",rowth
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hat may
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which
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§ 51.14 Control strategy: Carbon mon-
oxide, hydrocarbons, photo-
chemical oxidants, and nitrogen
dioxide.
(a) Priority I Regions. (1) Each plan
f c r a region classified Priority I with
respect to carbon monoxide, photochemical
oxidants, or nitrogen dioxide shall set
forth a control strategy which shall
provide for the degree of emission reduc-
tion necessary for attainment and main-
tenance of the national standard for each
such pollutant after consideration of the
emission reductions that will result from
the application of Federal motor vehicle
emission standards promulgated pursuant
to section 202 of the Act.
(2) Unless specific data are available
for a region, a State shall assume that
such Federal motor vehicle emission
standards will result in the emission
reductions shown in Appendix I to this
part. If specific data are vised, such
data must be submitted in the plan for
such region. (Refer to F.R.)
(3) The plan shall contain:
(i) A description of enforcement
methods including, but not limited to
procedures for monitoring compliance
with the selected traffic control measures,
procedures for handling violations, and a
designation of enforcement responsibili-
ties (j.e., air pollution control agency,
State police.)
(ii) Proposed or adopted rules and
regulations pertaining to the selected
transportation control measures.
(iii) A description of administra-
tive procedures to be used in imple-
menting all selected transportation
control measures.
Not Applicable
Covered in
Original Plan
Covered in
Transportation Plan
Missing
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(iv) A schedule designating dates by
which legal authority necessary to imple-
ment the plan will be obtained, other
significant steps in the implementation
of the plan will be achieved, and each
control measure will be implemented.
(h) Control strategy development. In
a region in which attainment and main-
tenance of a national standard will
require emission reductions in addition
to those which will result from applica-
tion of the Federal motor vehicle emis-
sion standards, the control strategy
c^'iall provide for application or such
oi:ier meaiujj es as may be necessary for
attainment and maintenance of such
national standard.
(c) Adequacy of control strategy (1)
The plan shall demonstrate, by means of
a proportional model or diffusion/photo
chemical model or other procedure which
is adequate and appropriate, that the
control strategy included in each plan
for a region classified as priority I
is adequate for attainment and mainte-
nance of the national standard (r) to
which such control strategy applies.
Control measures shall not result in an
increase in the concent ration of any
pollutant. The plan shall include
provisions as necessary to prevent such
increases in concentrations as a result
of traffic increases that may be stim-
ulated by transportation control
measures.
(2) With respect to control of
carbon monoxide and nitrogen oxides, the
proportional model which may be used
for purposes of this paragraph is described
in § 51.13 (e) (2): Provided, With
respect to the national standard for
nitrogen dioxide, that the degree of air
quality improvement indicated to be
necessary by the proportional model will
be achieved by a corresponding degree of
reduction of total nitrogen oxides
emissions from stationary and mobile
sources. (Refer to F.R.)
Not Applicable
Covered in
Original Plan
Covered in
Transportation PI;
Missing
7
Remarks
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(3) In any region where the degree
of nitrogen oxides emission reduction
necessary for attainment and mainte-
nance of the national standard for
nitrogen dioxide is greater than that
which can be achieved by the applica-
tion of (i) the Federal motor vehicle
^mission standards promulgated under
section 202 of the Act, (ii) reason-
ably available control technology to
nitrogen oxides sources, and (iii) any
transportation control measures which
may be necessary for attainment and
maintenance of the national standards
for carbon monoxide and photochemical
oxidants, the plan shall provide for
the degree of hydrocarbon emission
reduction attainable through the appli-
cation of reasonably available control
technology. In any such region, a
control strategy which provides for
such hydrocarbon emission reduction
shall be deemed adequate for attain-
ment of the national standard for
nitrogen dioxide.
(4) With respect to hydrocarbons and
photochemical oxidants, it may be assumed
that (i) there is no background concen-
tration of photochemical oxidants and
(ii) the degree of total hydrocarbon
emission reduction necessary for attain-
ment and maintenance of the national
standard for photochemical oxidants will
also be adequate for attainment of the
national standard for hydrocarbons. The
proportional model to be used to deter-
mine the necessary hydrocarbon emission
reduction is set forth in Appendix J to
this part. (Refer to F.R.)
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(5) The plan shall show that the con-
trol strategy including transportation
control measures will result in the degree
of emissions reduction indicated to be
necessary by a proportional model, diffu-
sion model , or other procedure which is
adequate and appropriate. The plan shall
contain a .'•ummary of the computations,
assumptions, and judgments used to deter-
nii-v.- the i;,.-.riions reductions that will
iesu.lt fro;:1 application of the control
strategy to each point source, and each
group of area sources. Su>-h summary shall
In-- inrlu'l'd i"i a table similar to that
• • .,. .; \up i x '"> L . 'Vis part. The
(> ' an ai.;.o t.i.all Contain a summary oi the
data, computations, assumptions, and
judgments used to develop any transporta-
tion control measures that are a part of
the control strategy. Such a summary
shall as a minimum contain the material
described in Appendix M to this part. The
detailed computations and data shall be
retained by the State and made available
for inspection by the Administrator at his
request. (Refer tr F.R. F. 36, No. 228
and F.R. V. 38, No. 8.)
(6) If a diffusion/photochemical model is
used, the plan shall include a description
of such model.
(d) Emission data. Emission data on
carbon monoxide, hydrocarbons, and ni-
trogen oxides shall be submitted in
accordance with the requirements of
§ 51.13 (f). (Refer to F.R.)
(a', Air 4jaiity data. Data showing
existing air quality levels shall be
presented in accordance with this
section:
(1) For Priority I regions, data on
carbon monoxide, nitrogen dioxide, and
photochemical oxidants shall, as a mini-
mum, include the results of measurements
made during a period of approximately
3 months in accordance with the
following procedures.
Not Applicable
Covered in
Original Plan
Covered in
Transportation
Missing
Remarks
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(2) For Priority I regions, only avail-
able air quality data for hydrocarbons
must be submitted.
(4) Air quality data required by this
subparagraph shall be submitted in the
form similar to that shown in Appendix
H to this part. (Refer to F.R.)
(f) Motor vehicle emission factors.
The States required to submit .transpor-
tation control plans must, except as
noted below, use current emission factors
and methodology to calculate emissions
from gasoline powered motor vehicles.
The current emission factors and method-
ology are presented in "Compilation of
Air Pollutant Emission Factors," EPA
report No. AP-42, revised semiannually,
and in superseding EPA interim reports.
These are available from the EPA, Office
of Air Quality Planning and Standards,
Research Triangle Park, N.C. 27711. If
emissions other than those presented in
the EPA report are used, the substantiat-
ing justification must be submitted with
the transportation control measures.
(g) Air Quality baseline. The concen-
trations of carbon monoxide and photo-
chemical oxidants set forth in the State
plan as approved and promulgated on
May 31, 1972 (37 FR 10842) (40 CFR
Part 52) may and should be used as the
air quality baselines for computation of
the emissions reductions through trans-
portation control measures required to
meet national standards. More recent air
quality data may be used where adequate
and appropriate. However, such data must
be compatible with the emissions inven-
tory for the region involved and justifi-
cation submitted for the appropriateness
of its use. Revised air quality data
should be submitted to the appropriate EPA
regional office at the earliest possible
date for evaluation and approval to
preclude plan disapproval resulting from
the use of faulty air quality data.
Not Applicable
Covered in
Original Plan
Covered in 1
Transportation 1
plissing j
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|(h) Transportation control strategies.
Information and requirements for States
which are considering transportation
M control measures involving inspection,
• maintenance and retrofit of in-use motor
vehicles are presented in Appendix N to
this part. (Refer to F.R. V. 38, No. 8)
§ 51.15 Compliance schedules.
(a) (J ) Except as otherwise provided
ir, subp.iragraph (2) of thi 3 paragraph,
each plan shall contain legally enforce-
Iable compliance schedules setting forth
the dales by which all ,-;t at.ii.nary and
mobile sources or categories jf such
1 sources must be in compliance with any
applicable portions of the control
strategy set forth in such plan.
§(2) A plan may provide that a legally
enforceable compliance schedule will be
negotiated with the owner or operator of
Ian individual source following submittal
of the plan. Such compliance schedule
shall be submitted to the Administrator
as early as possible but in no case later
• than the prescribed date for submittal of
• the first semiannual report required by
§ 51.7. Unless disapproved by the Ad-
Iministrator, such compliance schedule
shall be part of the applicable plan.
(b) O) Any compliance schedule de-
IKigned *••> provide for attainment and
ma i ati-'i'in i- <>t a pi imary standard shall
provide for compliance with applicable
I portions of the control strategy as ex-
peditiously as practicable and in no
case, except as otherwise provided by
1 Sub part C of this part, later than
May 31, 1973.
(2) Any compliance schedule designed
fto provide for attainment and mainte-
nance of a secondary standard shall
provide for compliance with applicable
^ portions of the control strategy in a
• reasonable time and in no case later
• than the date specified for attainment
of such secondary standard pursuant to
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(c) Any compliance schedule extend-
ing over a period of 18 or more months
from the date of its adoption, but in
no case later than May 31, 1975, shall
provide for periodic increments of pro-
gress toward compliance by any affected
source (s) or categories of sources.
(d) Except as otherwise provided by
Subpart C of this part, neither the State
agency nor a local agency shall grant
any variance of, or exception to, any
compliance schedule included in an ap-
plicable plan if such variance or excep-
tion will prevent, or interfere with,
attainment or maintenance of a national
standard within the time (s) specified
pursuant to § 51.10 (b) and (c).
§ 51.16 Prevention of air pollution
emergency episodes.
(a) For the purpose of preventing air
pollution emergency episodes, each plan
for a Priority L region shall include a
contingency plan which shall, as a mini-
mum, provide for taking any emission
control actions necessary to prevent am-
bient pollutant concentrations at any lo-
cation in such region from reaching levels
which would constitute imminent and sub-
stantial endangerment to the health of
persons, which levels shall be prescribed
by the Administrator.
(b) Each contingency plan shall (1)
specify two or more stages of episode
criteria sucn as those set forth in Ap-
pendix L to this part, or their equiva-
lent (2) provide for public announcement
whoiK'Vor ir.y ep i >ode stage, has been de-
termined to exi^t, and (3) specify emis-
sion control actions to be taken at each
episode stage, including, but not neces-
sarily limited to, actions such as those
set forth in Appendix I to this part or
their equivalent. (Refer to F.R.)
Not Applicable 1
Covered in 1
Original Plan I
Covered in 1
Transportation Plaj
Missing
12
Remarks
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|(d) To the maximum extcmL practi-
cable, emission control actions taken
pursuant to a contingency plan shall be
1 consistent with the extent of any air
pollution episode, e.g., if a single
source is determined to be responsible
for the occurrence of any episode stage,
• tnen the emission control action steps
™ applicable to such source, shall be taken.
_ (e) Each contingency plan for a Pri-
• or it y I region shall provide for:
* (1) Daily acquisition of forecasts of
atmospheric stagnation conditions or
1 during any episode stage and updating
of such forecasts at least every 12 hours.
(2) Inspection of sources to ascertain
• compliance with applicable emission
B control action requirements.
„ (3) Communications procedures for
• transmitting status reports and orders
* as to emission control actions to be
taken during an episode stage, including
1 procedures for contact with public offi-
cials, major emission sources, public-
health, safety, and emergency agencies
Iand news media.
(f) In the event that the requirements
of paragraphs (e) of this section have
•not been fully met by the prescribed date
for submitting a plan, a description of
the steps under consideration and a time-
1 table shall provide for meeting all re-
quirements of paragraphs (c) and (e) of
this section within 1 year after such
prescribed d?te. A description of interim
• actions that will be taken to control
™ emissions during any episode stage which
occurs during such 1-year period shall be
M included.
* (g) Each pJan for a Priority II region
shall include a contingency plan meeting,
Ias a minimum, the requirements of sub-
paragraphs (1) and (2) of paragraph (b)
^f this section.
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Not Applicable I
Covered in
Original Plan
Covered in 1
Transportation Plaij
Missing
13
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•
§ 51.17 Air quality surveillance.
(a) (1) The plan shall provide for the
establishment of an air quality surveill-
ance system which shall be completed and
in operation as expeditiously as practi-
cable, but not later than May 31, 1974
and which shall meet, as a minimum, the
following requirements.
(2) At least one sampling site must
be located in the area of estimated max-
imum pollutant concentrations.
(b) The plan shall include a descrip-
tion of the existing and proposed air
quality surveillance system, which shall
set forth:
(1) The basis for the design of the
surveillance system, selection of sam-
plers, and sampling sites.
(2) The locations of the samplers by
Universal Transverse Mercator (UTM)
grid coordinates or the equivalent. Any
EPA monitoring station may be designated
as a sampler location.
(3) The sampling schedules.
(4) The methods of sampling and
analysis.
(5) The method of data handling and
analysis procedures.
(6) The timetable for the installation
of any additional equipment needed to
complete the system.
(c) The plan shall provide for moni-
toring of air quality during any air
pollution emergency episode stage. The
stations selected for use during such
periods must be in operation within 6
months after the date of the Administra-
tor's approval of the plan and be capa-
ble of indicating when pollutant concen-
trations have reached, or are approaching,
any episode criteria established pursuant
to § 51.16.
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£ § 51.18 Kc-vJi!W of now sources and
modifications.
(a) Each plan shall set forth legally
enforceable procedures that will be used
to implement the authority described in
I§ 51.11 (a) (4), which procedures shall
be adequate to enable the State to deter-
mine whether construction or modification
Iof stationary sources w'.ll result in
violations of applicable portions of the
control strategy or will interfere with
•attainment or maintenance of a national
standard.
(b) Such procedures shall provide for
Ithe submission, by the owner or operator
of a new stationary source, or existing
source which is to be modified, of such
M information on the nature and amounts
1 of emissions, locations, design, construc-
~ tion, and operation of such sources as may
be necessary to permit the State agency
Ito make the determination referred to in
paragraph (a) of this section.
— (c) Such procedures rh^ll also include
• means of disapproving such construction
™ or modification if it will result in a vio-
lation of applicable portions of the con-
Itrol strategy or will interfere with attain-
ment or maintenance of a national standard.
(d) Such procedures shall provide that
1 approval of any construction or modifica-
tion shall not affect the responsibility
of the owner or operator to comply with
1 applicable portions of the control strategy.
"
§ 51.19 Source surveillance.
1.
Each plan shall provide for moni-
toring the status of compliance with any
rules and regulations which set forth
• any portion of the control strategy.
9 Specifically, each plan shall, as a mini-
mum, provide for:
I
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Not Applicable
Covered in
Original Plan
Covered in
Transportation Plan
i —
Missing
15
Remarks
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(a) Legally enforceable procedures for
requiring owners or operators of sta-
tionary sources to maintain records of,
and periodically report to the State in-
formation on, the nature and amount of
emissions from such stationary sources
and/or such othe information as may be
necessary to enable the State to deter-
mine whether such sources are in com-
pliance with applicable portions of the
control strategy.
(b) Periodic testing and inspection of
stationary sources.
(c) Establishment of a system for
detecting violations of any rules and
regulations through the enforcement of
appropriate visible emission limitations
and for investigating complaints.
(d) Procedures for obtaining and
maintaining data on actual emissions
reductions achieved as a result of im-
plementing transportation control
measures. In the case of measures in-
volving inspection, maintenance, or
retrofit, these data shall include the
results of an emission karveillance
program designed to determine actual
average per vehicle emissions reductions
attributable to inspection, maintenance
and/or retrofit. In the case of
measures based on traffic flow changes
or reductions in vehicle use, the data
shall include observed changes in vehicle
miles traveled (VMT) and average speeds.
The data shall be maintained in such a
way as to facilitate comparison of the
planned and actual efficacy of the
transportation control measures.
Not Applicable
Covered in
Original Plan
Covered in 1
Transportation Plaj
Missing
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§ 51.20 Resources.
IEach plan shall include a description
of the resources available to the State
and local agencies at the date of sub-
1 mission of the plan and of any addi-
tional resources needed to carry out the
plan furing the 5-year period following
Iits submission. Such description, which
shall he provided in a form similar to
that in Appendix K to this part, shall
iuclude projections of the extent to
• which resources will be acquired at 1-,
• 3-, and5--yenr intervals. (Refer to F.R.)
I § 51.21 Intergovernmental cooperation.
(a) For the purpose of assisting in
Ithe development of a plan for any
interstate region, the State agency
responsible for implementing national
1 standards in any portion of such an inter-
state region shall furnish any available
data on emissions, air quality, and
1 control strategy development, upor request,
to any other State or local agency having
such responsibility in any other portion
of such interstate region.
£ (b) Each plan shall identify:
(1) The local agencies by official title
— (2) the responsibilities of such local
• agencies and the responsibilities of any
™ State governmental agency involved in
carrying out any portion of the plan.
• (c) Each plan shall provide assurances
that the State agency having primary
responsibility for implementing national
• standards in any region, or portion
• thereof, will promptly transmit to
other State agencies having similar or
1 related responsibility in the same or
other States, information on factors
(e.g., construction of new industrial
1 plants) which may significantly affect
air quality in any portion of such
region or in any adjoining region.
1
Not Applicable
Covered in
Original Plan
Covered in
Transportation Plan
hissing
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§ 51.22 Rules and regulations.
Emission limitations and other measures
necessary for attainment and maintenance
of any national standard, including any
measures necessary to implement the re-
quirements of § 51.11, shall be adopted
as rules and regulations enforceable
by the State agency. Copies of all such
rales and regulations shall be submitted
with the plan. Except as otherwise
provided by §51.11 (b), submittal of a
plan setting forth proposed rules and
regulations will not satisfy the require-
ments of this section nor will it be
considered a timely submittal.
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GUIDELINE SERIES
OAQPS NO. 1.2-004
EPA SOURCE PROMULGATION
- Recordkeeping and Reporting
- Public Availability of Data
US. ENVIRONMENTAL PROTECTION AGENCY
Office of Air Quality Planning and Standards
Research Triangle Park, North Carolina
WAR ',373
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ENVIRONMENTAL PROTECTION AGENCY
Office of Air Quality Planning and Standards
Research Triangle Park, North Carolina 27711
RAtil'oJ: OAQPS, CPDD, SIB Dttle: March 21, 1973
Guidelines for Regional Office Enforcement of EPA Regulations Regarding
Recordkeeping and Reporting and Public Availability of Data
To:
See Below
Enclosed is a copy of the guideline document for implementing
EPA promulgated regulations for source recordkeeping and reporting,
and for public availability of emission data. This document has been
prepared for use by those Regional Offices which must carry out the
data gathering activities required because of deficiencies in state
implementation plans. Additional copies of this document may be
obtained from Ted Creekmore, OAQPS, CPDD, SIB, Research Triangle Park,
North Carolina 27711 (Phone: 919-68878366).
Norman G. Edmisten, Chief
Standards Implementation Branch
Control Programs
Ho wn"lr*nmr»n-t- HTV/T c i* on
Enclosure
Addressees:
Regional Administrator, Regions I - X
Director, Division of Air and Water Programs, Regions I - X (2)
Principal Air Contacts, Regions I - X (3)
W. Megonnell (3)
B. Stoigerwald
J. Paugett
W. Cox
R. Baum
D. Goodwin
J. Ha:<,..-3rle (
J. Bosch
SIB Personnel
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ENVIRONMENTAL PROTECTION AGENCY
Reply to
Ann of.- OAQPS, CPDD, SIB Dale. 14 MflR 19?3
Subject: Guidelines for Implementing EPA Promulgated Regulations for Source Record-
keeping and Reporting and for Public Availability of Emission Data
To:
See Below
Where State implementation plans were disapproved because they did
not provide adequate procedures for making emissions data available to
the public [40 CFR 51.10(e)] or for requiring sources to maintain records
and make periodic reports to the State [40 CFR 51.19(a)], EPA has promul-
gated (or is in the process of promulgating) the necessary regulatory
procedures .
The Regional Offices are responsible for designating one or more
places in each affected State where emissions data collected by EPA
will be available to the public. A list of these locations should be
forwarded to Mr. Norm Edmisten, Chief, Standards Implementation Branch,
which is responsible for publishing this information in the Federal
Register.
On November 15, 1972 and January 31, 1973, draft copies of guidelines
which can be used by the Regional Offices in implementing these regulations
were circulated for review. Enclosed is the final copy of the guidelines,
which incorporates many of the comments received.
If you have any questions, please contact Ted Creekmore (919-688-
8365).
Jean J. Schueneman
Di rector
Control Programs
Development Division
Enclosure
Addressees:
Director, Division of Air and Water Programs, Regions I - X
Principal Air Contacts, Regions I - X
W. Megonnell R. Baum
B. Steigerwald N. Edmisten
R. Nellgan D. Goodwin
J. Padgett J. Hammerle
W. Cox J. Bosch
SIB Personnel
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I. General Policy Regarding the Implementation of EPA Regulations for
Stationary Source Recordkeeping and Reporting, and for Public
I Availability of Emission Data
I This 1s a general policy guideline for carrying out regulations
promulgated by EPA as a result of State Implementation plan deficiencies
I regarding i 51.10(e), Public Availability of Emissions Data, and/or i 51.19(a),
— Procedures for Source Recordkeeplng and Reporting, of the "Requirements for
™ Preparation, Adoption, and Submittal of Implementation Plans" (40 CFR Part 51).
• In cases where EPA has disapproved only i 51.10(e), a reoulatlon has
been promulgated for: (1) requiring sources to maintain records, (2) re-
| quiring sources to submit emissions data, etc. to EPA, and (3) making such
emissions data obtained by EPA, as correlated with applicable emission Umlta-
• tions, available to the public. The recordkeeping and reporting provisions
• are promulgated to provide a mechanism for obtaining the necessary data
directly from the sources in order to release it to the public. In the States
| where the above deficiency exists, EPA does not^ have the authority
_ to require State or local agencies to provide EPA with
• emission data from their files. Where both I 51.10(e) and i 51.19(a) have
• been disapproved, EPA has promulgated the provisions of (1) and (2) above to
correct the I 51.19(a) deficiency and the provisions* of (3) above to correct
| the f 51.10(e) deficiency. Where only i 51.19(a) has been disapproved, EPA
also has promulgated regulations for all three provisions. In this case, the
• procedures for making emissions data available to the public are promulgated
• to clearly indicate EPA's intent to carry out the requirements of Section H4(c)
of the Clean Air Act and of 51.10(e) of the implementation plan regulations
(40 CFR Part 51). In essence, the same regulation has been promulgated
where EPA disapproved 1 51.10(e), I 51.19(a), or both.
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Attachment 1 shows the text of these regulations as promulgated by EPA 1n I
the Federal Register. The regulations do not require action by any stationary •
source until notified by the Administrator.
Regional Offices have the responsibility for notifying all •
appropriate sources of the recordkeeplng and reporting requirements (see
II) and making emission data, as correlated with applicable emission •
limitations, available to the public (see III). •
II. Guidelines for Notifying Stationary Sources of Recordkeeping and
Reporting Requirements •
A. Sources to be Notified •
The number of stationary sources to be notified of EPA's recordkeeplng
and reporting requirements will depend on the nature of the deficiencies in •
the implementation plan. Some States have adequate procedures and authority
to require source recordkeeping and reporting as required by I 51.19(a), ™
but lack legal authority to make all emissions data available to the public. •
In such cases, the State may be able to make emissions data available to the
public for a majority of sources, but cannot release data for certain sources J
which request confidential treatment pursuant to provisions of State statutes.
Thus, EPA would need to notify only these sources; presumably, a 11st of such
sources certifying confidentiality could be obtained from the State agency.
EPA must notify citizens through the Federal Register where such information
obtained by the State 1s available. [The Regional Offices should notify
the Standards Implementation Branch (SIB), Control Programs Development
Division (CPDD) of these locatons. SIB will then publish this Information
1n the Federal Register.]
In States or air quality control regions where there 1s no clear limitation
on stationary source to be notified, as 1n the case above, the Regional
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Office should plan to notify all stationary sources having a potential for emit-
ting more than 25 tons/year* of any pollutant for which there 1s a national
• standard and which are affected by the control strategies approved by the
Administrator. All stationary point sources emitting less than 25 tons/year
• not affected by the approved control strategies, may be Included 1f time
• and resources permit.
Once the criteria as to which sources must be notified have been estab-
• Ushed, a 11st of appropriate sources should be compiled. The names and
addresses of appropriate sources could be obtained 1n the following manner:
I 1. The Initial source of Information should be the National A1r Data
• Branch (NADB), Monitoring and Data Evaluation Division (MDED), Office of
A1r Quality Planning and Standards (OAQPS), which 1s presently compiling
I emission data for Inclusion 1n the National Emission Data System (NEDS).
These data are being compiled by contacting State and local agencies and
• from the Implementation plans (Including BOA Inventories conducted to
• assist 1n plan development). The NADB has a fairly complete 11st of sources
for all States.
I 2. Additional Information not obtained by the NADB may be available from
the State or local agencies, particularly those that have permit or regls-
I tratlon systems or that have compiled comprehensive emission Inventories.
• 3. From Industrial directories, phone book yellow pages, or trade asso-
ciation publications (see APTD-1135 - Guide for Compiling a Comprehensive
I Emission Inventory).
• Since 1t 1s often difficult to determine from Industrial directories or
the yellow pages whether a company 1s a significant source or would be affected
*TMs refers to potential emissions from Individual stacks.
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by the approved control strategies, this 1s the least desirable means of com-
piling the notification 11st.
It should be noted that even though complete emissions data may be avail-
able from the NADB or State or local agencies for certain sources, such sources
must still be notified of the recordkeeplng and reporting requirements 1n order
to assure that these data are updated on a periodic basis.
B. Priority for Notifying Sources
Once a 11st of appropriate sources has been developed, priorities for noti-
fication should be established. The following 1s a suggested order "for contacting
sources:
1. Sources affected by approved control strategies
a. Large point sources (100 tons or more per year*)
1) Priority I Regions
2) Priority II Regions
3) Priority III Regions
b. Smaller point sources (25-100 tons per year*)
Priority I Regions
2) Priority II Regions
3) Priority III Regions
c. Sources listed in Appendix C of 40 CFR Part 51 and not covered
by (a) and (b) above.
d. Other sources (e.g., incinerators and fuel combustion sources
smaller than 25 tons/year).
*This refers to potential emissions from Individual stacks.
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• Where the source notification 11st must be developed without Initial
emission Information from NEDS, or State or local agencies, the priority list
I can be based on other Indices such as plant capacity, employees, or sales.
As a minimum, sources under (l)(a) should be notified by May 1, 1973;
I . sources under (l)(b) should be notified by July 31, 1973; and all other sources
• to be notified should be contacted by January 1, 1974. Where final promulgation
has been substantially delayed, this schedule may have to be modified accordingly.
I
• C. Requirements that Stationary Sources Must Meet
• The attached form letter (Attachment 2) explains the requirements that
each stationary source must meet to comply with the EPA regulations. Each
| source must complete form 158-R75, A1r Pollutant Emissions Report (Attachment 3),
and return it to the Regional Office no later than 45 days after the end of each
• reporting period (i.e., August 15, 1973, February 15, 1974, etc.). Each station-
• ary source must maintain records as necessary to substantiate the data submitted
to EPA. This recordkeeping should be initiated as of the date the questionnaire
• is received. The form must be updated every 6 months to coincide with the semi-annua
reporting periods of January 1 - June 30 and July 1 - December 31 or a certifl-
' cation received from the source that there has been no change.
• After submission of the initial report of information, subsequent
reports need only identify those items that have changed or certify
• that the information previously submitted has not changed. Where an
Item has changed, the subsequent semiannual report should include the
• " applicable section of Form 158-R75. Questions concerning annual fuel
• consumption, process weight, or emission rate should be on a calendar
year basis. Thus, after the initial report, information concerning annual
I operating or emission rates should be submitted only in the report
due February 15 of each year and should cover the previous calendar
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year. Other Information on the general operation of the above facility
(change 1n process, new control equipment, etc.) should be submitted
1n the first report following any such change.
D. Coordination with Questionnaires Sent to Sources Under Section 114 of the •
Clean Air Act •
Since form 158-R75 has been approved by the Office of Management and Budget
pursuant to the Federal Reports Act, 1t 1s anticipated that this form also will
be used to obtain information for purposes other than the recordkeeping and re-
porting requirements. This form will be used for obtaining necessary information
under Section 114 of the Act and for obtaining Information required under Federally •
promulgated regulations for review of new or modified sources. Regional Offices
should make every effort to combine requests for Information whenever practical. I
To avoid duplicate updating of data by sources, the Regional Offices
should not make copies of form 158-R75 and the accompanying Instruction ™
sheets. NADB is responsible for supplying the Regional Offices with •
form 158-R75 through the designated NEDS contact man 1n each regional
office, who in turn is responsible for distribution. I
III. Guidelines for Making Data Available to the Public •
A. Data which Should be Made Available to the Public
The attached form letter to the sources (Attachment 2) explains what data I
must be made available to the public and what data can be held confidential
along with procedures for obtaining confidential treatment of data submitted I
to EPA. It 1s the Regional Office's responsibility to collect emissions data, •
correlate these data with applicable emission limitations, and make such data
available to the public in one or more locations in every state. (See B for •
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discussion of how the data will be handled.) The exact procedures for making
• such data available should be decided by the Regional Office 1n accordance with
the Freedom of Information Act and the EPA's regulations set forth 1n 36 F.R.
I 23058 (December 3, 1971).
• The Regional Offices are responsible for designating one or more places
1n each affected States where emissions data collected by EPA will be available
• to the public. It 1s suggested that the United States Attorney's Office or
Post Office be considered for this purpose. The details of this arrangement
I are left to the Regional Office. A 11st of these locations should be
• forwarded to the SIB, which 1s responsible for publishing this information
1n the Federal Register.
• B. Data Handling
• The Regional Office will be responsible for transferring the data received
from sources on Form 158-R75, Air Pollution Emissions Report, Into the NEDS for-
• mat, keypunching this information, and forwarding the data to the NADB within
— 21 days of validation. The NADB will enter these data into the central data
' bank in Durham. This data bank can be accessed directly by use of the computer
• terminals which will be Installed in each Regional Office when the system
is fully operational. The following format is suggested for making
• emission data available to the public.
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8
State of
AQCR Date
PlantOwner Process Allowed Actual Scheduled Applicable
Name and or or Emissions Emissions Compliance Regu- -j
Address Operator Source Pollutant ton/yr ton/yr Date lations
Refer to the applicable regulation (e.g., Section 03B, 10.03.37, Regulation
for Area II 1n Maryland). The NEDS data bank does not Include thls'informa-
tlon; thus, this column will have to be completed manually.
The NADB will prepare a program with standard report format as
described above as a service to the Regional Offices. The necessary ter-
minals to access the data bank for this Information will be available
after April 1973.
A copy of the NEDS format and explanation of how it 1s developed 1s pre-
sented 1n APTD-1135, Guide for Compiling a Comprehensive Emission Inventory.
Any questions regarding the NEDS format should be directed to John Bosch,
National A1r Data Branch, Monitoring and Data Evaluation Division, Research
Triangle Park, North Carolina 27711, FTS 919-688-8491.
After the Regional Offices have entered the applicable regulation for each
source, the above summary form should be adequate to fulfill most requests for
Information. If requested, the Regional Office should also make available the
complete NEDS printout or completed Form 158-R75, unless data have been
designated confidential.
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* Attachment 1
• Example of Promulgated Regulation for Source Recordkeeplng and
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Reporting and Public Availability of Emission
| (1) The owner or operator of any stationary source 1n the (State or
. Region) shall, upon notification from the Administrator, maintain records of
™ the nature and amounts of emissions from such source and/ or any other infor-
• matlon as may be deemed necessary by the Administrator to determine whether
such source 1s 1n compliance with applicable emission limitations or other
I control measures.
_ (2) The Information recorded shall be summarized and reported to the
• Administrator, on forms furnished by the Administrator, and shall be submitted
• within 45 days after the end of the reporting period. Reporting periods are
January 1 - June 30 and July 1 - December 31, except that the Initial reporting
I period shall commence on the date the Administrator issues notification of the
— recordkeeplng requirements.
• (3) Information recorded by the owner or operator and copies of the sum-
• marizing reports submitted to the Administrator shall be retained by the owner or
operator for 2 years after the date on which the pertinent report 1s submitted.
I (4) Emission data obtained from owners or operators of stationary sources
will be correlated with applicable emission limitations and other control measures,
• All such emission data and correlations will be available during normal business
• hours at the Regional Office (Region _ ). The Administrator will designate one
or more places 1n (State or Region) where such emission data and correlations
I will be available for public inspection.
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Attachment 2
Example Cover Letter to Source
Company Name
Dear Sir:
The Clean A1r Act, as amended 1n 1970, requires each State to submit an
Implementation plan for the attainment and maintenance of national ambient air
quality standards 1n each air quality control region of the State. Plans for
the attainment and maintenance of ambient standards for sulfur oxides, parti-
culate matter, carbon monoxide, non-methane hydrocarbons, photochemical oxidants,
and nitrogen dioxide were submitted to the Environmental Protection Agency (EPA)
early 1n 1972. These plans have been evaluated to determine their adequacy.
Those plans or portions thereof, found to be inadequate have been disapproved
by the Administrator [May 31, 1972, Federal Register (37 F.R. 10842), et. seq.]
As required by Section 110 of the Act, the Administrator must promulgate regu-
lations to correct deficiencies in State plans.
On (date) (37 F.R. ), the Administrator (EPA) disapproved the State of
's procedures (to require sources to maintain records of and periodically
report information on the nature and amount of emissions) and (for making emissions
data as correlated with applicable emission limitations, available to the public.)
(Copy enclosed.) On (date) (37 F.R. ), the Administrator promulgated regu-
lations to correct these deficiencies (copy enclosed).
Section 52. of the enclosed regulations requires that upon notification
from the Administrator you submit on a semiannual basis, information on the nature
and amount of air pollutant emissions and any other information necessary to
enable the EPA to determine compliance with applicable emission limitations or
other control measures of the Implementation plan for your facility located at
. The semiannual reporting periods are January 1 - June 30 and July 1 -
December 31, except that the initial report period commences on the date you
receive this notice. The information must be forwarded to this office no later
than 45 days following the end of the reporting period. The information shall
be submitted on Form 158-R75, Air Pollutant Emissions Report (copy enclosed).
In completing Form 158-R75, it 1s not Intended that a plant, institution,
or establishment purchase expensive equipment or hire a consultant to test the
stack effluents or determine other parameters. If any Information would require
substantial cost to obtain, notify the EPA at the address below so that estimates
may be developed jointly. However, EPA retains the right to require stack testing
1f 1t is found necessary to support the data presented 1n the form.
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The data presented are to be supplied as they pertain to: participate
matter, sulfur oxides, carbon monoxide, hydrocarbons, and nitrogen oxides.
If these pollutants are not emitted, only Section I (Page 1} need be completed.
The Initial report should be for the previous full calendar year (January- _
December). Although adequate records for the Initial report may not be available I
to respond accurately to some questions, please attempt to answer all applicable
questions. Adequate records must be maintained 1n order to accurately complete I
and substantiate the data submitted on all subsequent reports.
After submission of the Initial report of Information, subsequent reports I
need only Identify those Items that have changed or certify that the Information
previously submitted has not changed. Where an Hem has changed, the subsequent •
semiannual report should Include the applicable section of Form 158-R75. •
Questions concerning annual fuel consumption, process weight, or emission rate «
should be on a calendar year basis. Thus, after the Initial report, Information |
concerning annual operating or emission rates should be submitted only in the
report due February 15 of each year and should cover the previous calendar year. I
Other Information on the general operation of the above facility (change in
process, new control equipment, etc.) should be submitted in the first report I
following any such change. For the facility indicated above, your first report
1s due no later than ; the second report no later than ; etc. •
—
Records as necessary to substantiate the data submitted to EPA shall be m
maintained and submitted to EPA upon request. You must retain all records and M
reports for a period of two years from the date on which the pertinent report I
is submitted.
As specified In Section 113(c)(2) of the Act, any person who knowingly makes
••T^f - ;ter>er * - ?prf-- * --".•.•Mon, or ce?'.ifitatlcn ir arv record •;- report filed
or required to be maintained under the Act shall, upon conviction, be punished •
by a fine of not more than $10,000 or by Imprisonment for not more than six months
or both. •
Records and Information submitted under the requirements of I 52. shall be ™
made available to the public by EPA unless a satisfactory showing has been made to •
the Administrator, EPA, that release of the Information obtained would divulge a I
trade secret. Information required pursuant to I 52. cannot be withheld from EPA
on the grounds that you consider 1t to be confidential. If you believe that any of
the information we reauest would reveal a trade secret if divulged, you should
clearly idertify that information. Emission data, however, will always be available
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to the public. Any Information determined to constitute a trade secret will be
covered by 18 U.S.C. Section 1905, except that such Information may be disclosed tc
other officers, employees or authorized representatives of the United States con-
cerned with carrying out the Act, or when relevant in any proceeding under the Act.
Questions concerning the completion of Form 158-R75 or requests for additional
forms should be directed to:
Completed forms should be forwarded to the above address
Regional Administrator
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f ATTACHMENTS ^
Instructions for Completing the A1r
Pollutant Emissions Report (Form 158-R75)
The data requested are to be supplied as they pertain to the
following pollutants:
. If these pollutants are not emitted,
only Section I need be completed; check to Indicate this at the bottom
of page 1 and sign 1n the space provided.
Section I requests general Information on the size and location of
the plant, Institution, or establishment. Sources of pollution must be
located on a map by L'PA to within 100 meters, thus, more than the
plant or establishment address is requested. Give the distance and
direction to the nearest cross streets, crossroads or landmark. Where
there is more than one btiMina or where sources of pollution are
separated by more than b ' meters, enclose a sketch, map or engineering
drawing on which source^ (stacks, vents, etc.) are located and identified
by source code. Indicate the north direction and scale on the sketch
or map.
Section II (two pages) relates to fuel combustion; Section III, to
the disposal of combustible solid and liquid wastes; Section IV, to
manufacturing, processes, and other operations; Section V, to air
cleaning equipment; and Section VI, to stack and pollutants emission
data. In Sections II through VI, the first column 1s headed "Source
Code". Footnote "a of Section II through IV describes the designation
of source codes. A source code is unique for each source of pollutants
so It may be used to relate a fuel combustion source, a waste disposal
source, or a process and operations source 1n Sections II through IV
with Its air cleaning equipment data In Section V and Its stack and
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pollutants emission data 1n Section VI. A boiler in Section II would
be related by Us source code (e.g., Ha) to Us air cleaning equip-
ment 1n Section V and Us stack and pollutant emissions data reported
1n Section VI using the same source code.
The attached 11st of example sources, Attachment A, provides
identification numbers, (an eight digit I.D. code) which are to be
used instead of word descriptions for "Type of Unit" (column 4) in
Section II, "Method of Disposal" (column 5) in Section III, and
"Process or Operation" (column 2) in Section IV. A source must be
appropriately described by the example to use the identification number.
Example listings in Attachment A which end with "other not classified"
or "general/other" do not appropriately describe processes or
operations; do not use. Attachment B lists example air cleaning equip-
ment, each with an Identification number, ID code (see footnote
instruction "b" of Section V). Air cleaning equipment to remove a
pollutant (e.g., particulates) from a source may consist of a combination
of two or more types, report all types and the arrangement of the
combinations.
The normal operating schedule 1s essential data for each pollutant
source. If sources reported in Sections II, III or IV have normal
operating schedules different from that reported in the space
provided, enclose, on a separate sheet, the normal operating schedule
of each such source and identify the source by its source code.
Sources, boilers or process units may be grouped, combined (see
instruction a^ for Sections II and IV) when units are essentially
identical or discharge through the same stack or common emissions
control equipment. The combined capacity of grouped boilers should
not exceed 10 million BTU per hour. Report the number of units which
have been grouped. If units which are grouped discharge through
separate stacks, report stack data for one typical, representative
stack.
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Fuel combustion sources, reported 1n Section II includes
internal combustion units, turbines and fuel combustion for kilns,
dryers, etc. Where combustion 1s a part of a process as 1n kilns,
dryers,foundaries, glass melt tanks, etc., this is indicated in
'.e-;tior II, pages 2 and 3, oy using the process source code (e.g.
IVa, IVi.', etc.). Waste materials as bark, woodwaste, and waste
solvents used as fuel in boilers or dryers will be reported in the
OTibust- )r> section, Section II (do not report in the waste disposal
section;. Give the heat content,ash and sulfur contents of special
fuels and wastes 'jsed as fuel. Solvents, liquid and gas fuels
handling and storage operations which have losses to the air are
reported as sources. Report the units (pounds, tons, gallons, barrels
or 1C)3 cubic feet) for any quantity which is reported. Pollutants
from each source are reported separately.
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SC
Attachment A
Table of Contents
Source Coding Table*
External Combustion Boiler - Electric Generation
External Combustion Boiler - Industrial
External Combustion Boiler - Commercial Institutional
Internal Combustion Boiler - Electric Generation
Internal Combustion Boiler - Industrial
Internal Combustion Boiler - Commercial Institutional
Internal Combustion Boiler - Engine testing
Industrial Processes - Chemical MFG
Industrial Processes - Food/ Agriculture
Industrial Processes - Primary Metals
Industrial Processes - Secondary Metals
Industrial Processes - Mineral Products
Industrial Processes - Petroleum Industry
Industrial Processes - Wood Products
Industrial Processes - Metal Fabrication
Industrial Processes - Leather Products
Industrial Processes - Textile Manufacture
Industrial Processes - In Process Fuel
Point Source Evaporation - Cleaning Solvent
Point Source Evaporation - Surface Coating
Point Source Evaporation - Petroleum Storage
Point Source Evaporation - Miscellaneous Organic Storage
Point Source Evaporation - Printing Press
Point Source Evaporation - Miscellaneous Hydrocarbon Evaporation
Solid Waste - Government
Solid Waste - Commercial Institutional
Solid Waste - Industrial
ID represents the first two categories of the source code
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Attachment B
Air Cleaning Equipment Coding Table
Is a. list of the Identification numbers and names of
the control devices used with NEDS. For the parti cul ate control
devices (wet scrubbers, gravity collectors, centrifugal collectors, and
electrostatic
preclpUators), the efficiency ranges correspond to the
following percentages:
Identification
OCO
001
002
003
004
005
006
007
008
009
010
on
012
013
014
015
016
017
High: 95 - 99 +
Medium: 80 - 95
Low: < 80
Number: Control Device/ftethod:
No Equipment
Wet Scrubber - High Efficiency
Wet Scrubber - Medium Efficiency
Wet Scrubber - Low Efficiency
Gravity Collector - High Efficiency
Gravity Collector - Medium Efficiency
Gravity Collector - Low Efficiency
Centrif 53! Collector - High Efficiency
Centrifugal Collector - Medium Efficiency
Centrifugal Collector - Low Efficiency
Electrostatic Precipltator - High
Efficiency
Electrostatic Precipltator - Medium
Efficiency
Electrostatic Precipltator - Low
Efficiency
Gas Scrubber (general, not classified)
Mist Eliminator - High Velocity
Mist Eliminator - Low Velocity
Fabric Filter - High Temperature
Fabric Filter - Medium Temperature
-------
Attachment 8-2
Identification Number; Control Device/Method;
018 Fabric Filter - Low Temperature
019 Catalytic Afterburner
020 Catalytic Afterburner with Heat
Exchanger
021 Direct Flame Afterburner
022 Direct Flame Afterburner with Heat
Exchanger
023 Flaring
039 Catalytic Oxidation - Flue Gas
DesulfuHzatlon
040 Alkalized Alumina
041 Dry Limestone Injection
042 Wet Limestone Injection
043 Sulfurlc Add Plant - Contact Process
044 Sulfurlc Add Plant - Double Contact
Process
045 Sulfur Plant
046 Process Change
047 Vapor Recovery System (Including
condensers, hooding, and other enclosures)
048 Activated Carbon Adsorption
049 Liquid Filtration System
050 Packed Gas Absorption Column
051 Tray-Type Gas Absorption Column
052 Spray Tower (Gaseous Control Only)
053 Venturl Scrubber (Gaseous Control Only)
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I
x UNITED STATHS ENVIRONMENTAL PROTECTION AGENCY
Office of Mi; Quality Planning and Standards
Research Triangle Park, North Carolina 27711
/
SUBJECT: Recommended Approach to Promulgation- of EPA ' DATE: March 19, 1973
Transportation Control Jiang . . .
FROM:
•
SASD/LUPB
I
I
TO: ' Regional Transportation Representatives
Regions; I-X * • • « • * o
0 "
The primary philosophy in approaching the transportation control
• ' c plans is to insure maximum State participation. States should be
encouraged at every opportunity to develop and submit transportation
control plans that will achieve-the NAAQS by 1975. • They should use a
balance of approaches including non-hardware items Such as mass trans-
. portation, car pooling, pricing policies; and hardware items such as
inspection, maintenance, and retrofit where necessary. If portions of
. c a State plan are deemed inadequate, EPA should first consider approaches
that the State itself would like to have taken. It would be ill-advised
to pursue a plan that had been previously considered and outrightly
rejected by the State.
4 , - «
As it becomes necessary for EPA to propose a plan or portions of a
) plan, the following approach should be taken:
1. Utilize approved portions of State plans where possible, ,
including indirect approach to transportation controls such
as encouraging car pools, bus lanes, etc.
* • '
2. Maximum use should be made of additional stationary source
'controls.
3. Propose EPA plans that are consistent with State desires.,
4t Consideration should be given to gasoline, handling regulations.
5, Direct approach transportation controls such as VMT reductions
• • through auto free zones .should be considered. Indirect
approaches such as encouraging car pools are not a recommended
policy for EPA promulgations.
6. Hardware controls including inspection, maintenance and limited
retrofit such as vacuum spark disconnect, lean idle adjustment,
and air bleed to intake manifold shoutld now be considered.
7. Catalytic retrofit for-post- controlled cars; and exhaust gas
recirculation (EGR) only for extreme'cases.
8. Gasoline rationing should be used only'as the last recourse
. •. to attain the standards by 1975. • ' *
- -- • * »'
The attached table delineates an approach that will enable EPA to
propose j pjan for attain i.n;r, the starcUrds by 197 j. This is bc.-.cd on
national figure;; and the hardw.ire approach.' You rjhouJd approach inc.
-------
problem as outlined above; re-evaluate additional reductions obtainable
through these approaches and determine how much remains to be obtained
through hardware controls. The percent reduction in tlhc table does
not include items one through five above. Therefore, additional reductions
may be possible through their use prior to vise of hardware items. Each
AQCR must' be individually evaluated and a EPA plan specifically tailored
to the AQCR. It is recommended that a contingency plan based on the
above-be outlined and held in reserve in the event plans are not received
or deemed inadequate. «
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•' .. ,
Notes: , ,;. ..
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• • The data provide'd in these charts may not reflect the latest information
which you may have. The following notes identify specific'changes which should
B * be made. If you have more recent data, or recognize any errors', please -notify
I' the Land Use Planning Branch. „
' ' • « •.
1.1. More recent air quality data for -the Metropolitan Philadelphis Region
' ' ' ' '- ,' 3
• "o -shows a second high value of 30 ppm (34 ing/m ) for carbon monoxide.
I • e 2. Louisiana's recently adopted hydrocarbon regulation wi'll provide
significant reductions from stationary sources. Transportation controls
• . will probably not be needed. Air quality data from Louisiana was used
t '
• • *
• • t. ' for'this entire Region. Recent data taken in the Texas portion shows
a second high value of .30 ppm for oxidants. This' is the value which
Texas will use to develop a plan for its portion of the Region.
• '3.' The'revised Texas emission inventory shows a significant change in the
mobile source contribution to total hydrocarbons. The ratio of mobile
I to total emissions is now .14. Transportation controls.will therefore
. • have less of an effect on total emission reductions. , The same type
™ • ratio for the Houston-Galveston Region also changed, and now is .16.
• • *
• 'Stationary source controls must obtain significant reductions in these
two Regions if the NAAQS are to be achieved by'May 31, 1972.
I ' 4. The^air quality data used for these calculations are second high values.
• However, the California Air Resources Board wi'll use the maximum values
.
of .46 ppm and .40 ppn for the Southeast Desert and San Diego Regions
I- - • - .
respectively in developing their plans-.
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UNITED STATES ENVIRONMENTAL PROTECTION AGENCY
Office of Air Quality Planning and Standards
Research Triangle Park, North'Carolina 27711
"HjECT: Format for the Review and Evaluation of Transpor- DATE: March 28 1973
tation Control Plans • *
TO: Transportation Planning Representatives
Regions I-X
At the meeting of Air and Water Program directors and transpor-
tation planning representatives in Chicago on March 20, 1973, Dr.
Tom Wright of TR1-I Systems, Incorporated, handed out two documents
that pertained to TRW's Basic Ordering Agreement No. 68-02-0048,
Task Order No. 14.
One document was a 20-page set of tables that TRU plans to use
during their initial review of the SIPs to gather data concerning
items one and two of the Task Order. Item one primarily covers
the social and economic impacts of transportation controls while
item two summarizes the general and specific features of transpor-
tation control strategies selected by the States. The other document
furnishes some brief directions for the completion and use of the
tables.
It was explained at the meeting that these tables were going to
Obe used by TRU and could be used by the Regional offices if they found
them useful. It was' further requested that tne Regional otnces sena
comments in to the Land Use Planning Branch concerning the adequacy of
the tables so that these comments could oe forwaraed 10 "IK'W.
Dave Tamny, of the Land Use Planning Branch, has contacted the
transportation planning representatives by phone again asking for
comments. It was his understanding that if he did not receive
comments by March 23, 1973, it meant the Regional offices had no
comments regarding the forms/tables to be used by TRW for the review
and evaluation of the transportation control plans. • *
As of March 27, "1973, no significant comments have been received
regarding TRW's format for review and evaluation of transportation
control plans. Therefore it is assumed the Regional offices have no
additional comments and there is no need to issue revised tables.
Frederick Winkler
Land Use Planning Branch
EPA Foim 1320-6 (Rev. 6-72)
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',,,-
UNITED STATES ENViriONMEHTAL PROTECTION
.Office of Air Quality PI aim ing and Standards
Research Triangle Park, North Carolina 277,11
sbv/jV,CT: Transportation Control Meeting
(3/30/73 -.Chicago, Illinois)
,.c
DATE: March 28, 1973
FROM: •' SASD/I.UPB
TO:
O
See Addressees
I ,
A meeting was held in Chicago on March 20, 1973, to discuss
the status of transportation control plan development, and the
reccirinoided approach to HPA plan development. All EPA regional
offices, GAMP, OGC, OAQPS, MSAPC, MSF.D, FHUA and TRW were represented
at the meeting. An attendance list is enclosed.
Also enclosed are the minutes of this meeting. Questions
concerning the minutes should be directed to the Land Use Planning
Branch (Dob Clark: (919) 688-8291.) Follow-up on Action Items (see
enclosure) generated at the meeting is continuing. Questions
concerning these items should also be directed to the above.
Pvonald A. Venezia
Chief
Land Use Planning Branch
Enclosures (3)
Addressees:
T. Cortese
T. Dwyer
I. Mil nor
B. Burch
E. Enstrom
J. Crocker
D. Durst
J. Phil brook
R. Mueller
B.J. Steigerwald
J. Padgett
J. Horowitz
J. Me r-en da
D. Hanson
D. Grahani
H. Gompf ;
T. Wright i
EPA Coim 1320-6 (Rev. 6-7?)
-------
o
AGENDA
Transportation Control Meeting
Chicago', Illinois - March 20, 1973
O
10:00 Welcome from Region V
.
10:05 tOpening Remarks
10:15
Regional Status Reports
(Ten minutes each)
1:00
1:15
1:30
1:45
2:00
2:15
2: l\ 5
3:15
3:30
(B.J. Steiger^ald)
, (Region^ I-X)
Region IX will also discuss L.A. Hearings (Twenty minutes total)
12:00- Lunch
1:00
Review of SIP Task Schedule
•
Guidance for Writing Transportation Plans
(Venezia)
(Armstrong)
Hydrocarbon Emission Inventory and Controls 4 (Armstrong arid Horowitz)
EPA Proposed Strategies
o
Enforceability of Transportation Control
Strategies
Basis for Extensions
Transportation Regulations ~ Appendix N
•
Evaluation Reports
Discussion
(Venezia) . • «
(Graham)
•
(Trick)
(Armstrong and Mcrenda)
•
(Venezia) ,
5:OC . Adjourn
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I
Transportation Control N.oosures, tmcago i\\.
• . '• March 20, 1973 • • !
I
1
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Name. :
Wallace VJoo
Tony Cortese
Israel Milner
Chuck Miesse
Bill Burch
Lance Vins'on
'Ed Enstrom
Ed Muse .
Manuel Marks
Jack'Chicca
"Diana Dutton
. John Crocker
Dewayne Durst
Irwin L. Uickstein
'Charles W. Hurray Or.
John Phil brook
Ron Mueller
B.O. Steigerwald
0. Padgett
Ronald Venezia
•Donald Armstrong
David Tamnyt
Robert Clark
Ooel Horowitz
Joe Korenda
Dave Hanson
David B. Graham
Dick Kozlowskii
• i
Henry Gompf
Tom Uriqht
' Organization^ '
Region I - EPA
Region I - EPA
Region II - EPA
.Region III - EPA-
Region III - EPA
Region IV - EPA
Region V - FHUA
Region V - FHWA
•Region V - EPA
Region V - EPA
Region V.-EPA •
Region VI - EPA
Region VI - EPA .
Region VII - EPA.
'Region VIII - EPA
.Region VIII - EPA
Region VIII - EPA
[.Region IX--EPA
OAQPS, Durham
OAQPS, Durham
LUP.B, Durham
LUPB, Durham
. LUPB, Durham .
LUPB, Durham
DAMP
OAWP>
OAWP
USED
MSED
MSAPC
TRV!
Telephone
617-223-5609
617-223-5630
212-264-9800
215-597-9164
215-597-9303
404-526-3285
312-253-1471 '
312-353-6942
312-799-6300
312-799-6300
214-749-2142
214-749-1231
816-374-3791
513-837-3868
513-837,:4871.
305-837-4831
415-556-2332
919-688-8576
919-688-8204
919-688-8291
919-688-8291
919-688-8291
919-688-8291
202-755-0630
202-755-0650
202-755-0460
202-755-2598
202-755-2518
313-761-5230
703-893-2000
-------
MINUTES
Transportation Control Meeting
Chicago, 111. -'March 20, 1973
• • •
o" '
I. Ronion Office Summaries ' «
« —j . •
c
Region I: . %
• • * « « «
A. • Metropolitan Boston " "
1. New air quality data for this AQCR (.25 - .26ppm) in-
• . dlcatcs that a reduction in hydrocarbons of 86% will-be
, o required based on App. J of the Federal Register. Region
« , ,° I is considering letting the State use°a proportional
rollback for calculating the required reduction (about 70%).
'«
. « '2.. 'Region I expects the State to submit only a token plan.
• Therefore, EPA promulgation is likely.
B. Hartford - New Haven - Springfield
<•
1. Region I expects that the State will not submit a plan
for this AQCR until June. 6CA has been contracted by
Region I to-prepare an EPA plan.
. * - . «
Region II: . »
•,
A. New York - New Jersey -^Connecticut •• «
t
1. New York and New Jersey are using air quality data in
their respective portions of this AQCR for.plan development.
2. New York and New Jersey will be meeting to discuss reciprocal
transportation control strategies. Region II requested
advice on EPA's position on such strategies for interstate
regions'.
i
3. Region II expects a late submittal from New Jersey. Clari-
fication was requested on how this would be handled in
Federal Register notices.
«
4. No hearings for New Jersey's plan have been scheduled.
B. Metropolitan Philadelphia
. •
* 1. Pennsylvania and New Jersey are using air quality data from
their respective portions of this AQCR for plan development.
*--*"- * „•
2. Region II dxpects 3 late submittal -from New Jersey. Mo
• -'hearings have bo on :.>. u-jdulcd tor the plan.
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™ , Region III:
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O A. • National Capital/ • '
1. Results of the preliminary review of the plan for this
AQCR indicate that no EPA promulgation will be necessary.
However, minor changes to the plan have been requested
by Region III.
• 2. Based on new air quality data (.20 ppni), Virginia wi.ll
* • . submit a transportation'control plan for photochemical
oxidants. A special session of the State.legislature
° c must be called to approve the necessary legal authority.
o
* • • 3. ''Virginia is considering gas rationing as a back-up
strategy for its portion of this AQCR.
* • *
B. Metropolitan Baltimore
• 1. Region III anticipates an extension -request for this
AQCR. It is expected that such a request will be justified.
2. No promulgation is expected for this AQCR.
C. Metropolitan Philadelphia
c '
1 1. Region Ill-expects a justifiable extension request for
this AQCR. No EPA promulgation is anticipated.
D. Southwest Pennsylvania
1. . Region III expects a justifiable extension request-for this
AQCR. No EPA promulgation is anticipated.
Region IV:
* • .
A. Metropolitan Birmingham
» .
1. Region IV does not expect that transportation controls will
be required for this AQCR.
B. Mobile - Pensacola - Panama City
1
I
C. Regions IV thinks that there may be carbon monoxide problems
in Atlanta and Miami. However, no steps have* been taken to call
for a revision to the plans for these AQCR's.
-------
Region V:
. A. ' Metropolitan Chicago
1. Public hearing dates have been announced for this
AQCR. The basis for the plan is a city -developed
/ Inspection/maintenance program. There may be conflict
with State authority/responsibility for the plan.
Region V does not think that the State has authority
to take over the program if the City, defaults.
.
2. Region V questions the method used to device emissions
• from heavy duty vehicles. If the method is not acceptable,
• -. <(a'larger reduction of carbon monoxide would be required.
•
' . e
B. Metropolitan Dayton c .
1. The State has revised the emissions inventory and will
use more recent air quality data for oxidants, Region V
expects the NAAQS to be met in this 'AQCR by 1975 without
transportation controls. However, an inspection/main-
tenance progrnm will probably be implemented by the State.
° • .
Q. Metropolitan Cincinnati
c
* I •*
* 1. * The emissions inventory has-been revised and mobile source
emissions recalculated. As a result, Region V expects
that stationary source controls in this AQCR will be
~~" sufficient to allow attainment of the NAAQS by 1975.
D. Metropolitan Toledo
1. As a result of emission inventory and mobile source emission
revisions, Region V expc-cts the NAAQS to be met by 1975
without transportation controls.
• .
E. Minneapolis - St. Paul i
*
1, As a result of new air quality data, Region V expects the
NAAQS to be met by 1975. GCA has been contracted by
Region V to rework the transportation data base for this AQCR.
*
•
• .
Region VI: '
1
A. Southern Louisiana - Southeast Texas '
•
•"* " i
1. Based on recently adopted stationary source controls by
the State, Louisiana is not expected to noed transportation
controls for its portion of this AQCR.
!
B. Texas will-not submit a plan containing transportation controls.
The Stale claims that 'the: N/'AOS can bo met in all applicable
AQCR'r, through more stringent'stationary source control:: v;!rich
have been adopted. Region VI does'not expect that stationary
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O source controls alone will bo sufficient. .Consequently,
•''Region VI con s.i do ring contractor assistance! for preparation
m . of a transportation conlroTplan for Texas.i
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. . C.• Region VI expressed concern for a potential problem in the
,- • / El Paso - Las Cruces - Alamogardo AQCR. Emissions from Mexico
• , may prevent NAAQS from being met in this AQCR. * .
D., Texas will held public hearings-on April 4, 1973 to obtain
public reaction to transportation controls. No specific
c strategies will be recommended. The only purpose of this effort
is to get. public opinion if "transportation controls were
., implemented. '
* : ' • 6 * t *
Region 0VII: „ •
A. Metropolitan Kansas. City *
1.- Region VII expects that a 10% reduction in total carbon
'monoxide emissions will have'to be realized from trans-
' portation controls in this AQCR. Region VII thinks that
: 'a short extension (7 months) can be justified.
2. P£DCo has been contracted by Region VII to revise mobile
source emissions..
i
Region VIII: • -. •
; " - . * •
A. Wasatch Front
• • '
1. Region VIII expects to have to promulgate a plan for this
AQCR.
2. New air quality data indicates a CO problem in Ogden similar
to the one in Salt Lake City.
B. Metropolitan Denver
1 Region VIII has doubts as to whether Denver's preliminary plan
P ' 1s sufficient for meeting NAAQS by 1975. The state has proposed
stationary source controls which will provide some help in getting
H the necessary hydrocarbon reductions.
. Region IX: ' • •
A, No hearing dates have been announced by. California. Region IX
>0 does not expect a plan submittal until June. -
B. California's current inspection/maintenance program is designed
to randomly select 15% of the L.A. vehicle population. The State
is considering a 50/' rejection.
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C. With the exception of Los Angeles, Region IX considers the
'San Diego and San Francisco AQCR's as most critical. The
Southeast Desert AQCR problem is considered a carry-over of
the Los Angeles problcml • •
• D. Phoenix - Tucson
. •
Region IX has discussed new emission inventory calculations
« with the State. Plan submittal is expected on April 15, 1973.
* fc ' « v
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E. ' Clark - .Mohave 9 • '
€ t
" Emission reductions .assumed for transportation controls in
•.Nevada's SIP are too high compared to that allowable'under .
« the proposed guidelines. In addition the State's committment
• < - to implement'the strategies set forth in the SIP is question-
able. Consequently, Region IX expects that a re-evaluation
,of the SIP would prove it to be inadequate for meeting the
• NAAQS by 1975.'
Region X: '
..Washington has the legal authority to implement an inspection/mainr
tenance program. However, lack of a vehicle safety inspection
x program would make it very difficult for such a strategy by 1975.
II. Plan Review Schedule • * '
* *
*
A. One of the main points of discussion was the importance of having
the FHWA participate in plan reviews and any EPA plan development;
Generally, FHWA and Region personnel have had only limited contact.
The Regions were urged to actively pursue participation by FHWA
both in plan review and development. FHWA representatives at the
meeting expressed a desire to participate and a willingness to
assist EPA.
B. The Regions were reminded that preliminary as well as final plans
were to be sent to all reviewers for comments. Comments should
be returned to the Regions as soon as possible.
C. The Regions are supposed to notify OGC (Bill Frick) immediately
on receipt of plans.
111.' Guidance for Writing Plans •
A. The recommended approach to preparing an EPA.plan was presented
• (See attachment I). During the ensuing discussion, the avail-
ability of various retrofit hardware and implementability of
•Inspection/maintenance programs were questioned. It was.generally
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agreed that the'VSAD and LIAF options would bo available
and implemcntablc by 1975. -There was disagrepment, however,
on the availability and'implementability of the EGR and
catalytic converter options. This disagreement led to the
question of whether a State's plan should be 'approved if one
or, both of these options were included as part of the overall
* ^trategy for NAAQS attainment by 1975. HSPCP pointed out • •
'„ 'that the proposed Appendix N required States to substantiate
the-availability of such retrofits and provide assurance that imple-
mentation could be achieved by the required deadline. If these
.requirements were satisfied,- then there would be no grounds for
« disapproval. "
1 •
. • • • * •
B. The" ability of States to have operational inspection/maintenance
• . ; programs by 1975 was questioned, especially- for those states
-: which do not now have safety inspection programs. MSPCP agreed
•• to provide information on the steps required to develop an
inspection/maintenance program and an estimate of the time
I needed for each phase of development. This information should
i be available early in the week of March 26.
IV. Enforceability of Strategies '
Dave Graham*(MSED) provided^a memorandum concerning this subject.
• \ ' ' . . .
V. Basis for Extensions -
•.
A. The following information on attainment date extensions.was
provided by OGC. . ,
1. Adequacy of extension justifications must be determined for
each specific case.
2. Although a maximum extension of two years may be granted, EPA
must ensure that States attain NAAQS as expeditiously as
, practicable.
I . • '
3. To be granted an extension (of any length) a State must have"
considered all available alternatives.
i *
! •
4; It would be very difficult for EPA to grant an extension reques
! which is based on social impact.
•*• *
B. i An interesting point was brought out during the discussion on plan
extensions. If EPA proposed a plan which included an extension,
* then this would essentially be a garranteed extension for the State
if the..State in turn submitted a late plan.
!•
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VI. Evaluation Reports
/ •
A checklist (prepared by TRW) for'plan review as part of •
TRW's impact analysis was'handed out to all reviewers.
Comments concerning this checklist should be returned to
, LUPB as soon as possible in order to make the list as
useful as possible for TRW. Reviewers may also use this
checklist as necessary in their review of SIPs.
VII. Transportation Regulations.- Appendix N" «
• .
A. All numbers of reflecting allowable reductions for the
, various control measures are to be used as a guide until
. . Appendix N has been officially approved.
«• •
•
B. MSPCP pointed out that failure rates for inspection/
' . maintenance programs are for individual pollutants.
° - For example, the worst 30% of hydrocarbon emitters
may not necessarily be the worth 30% of carbon monoxide
emitters. It is possible then, to have more than 3Q%
of the vehicle population fail if vehicles are tested for
hydrocarbons and carbon monoxide.
VII. Action Items
4 •«- .
A list of action items were identified as a result of the
various questions raised, points of disagreement, and
requests for guidance. This list, which includes the
responsible agency, is provided in Attachment 2.
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II GUIDELINES FOR WAIVERS OF EMISSION
J TESTING IN FACILITIES INVOLVING
J BERYLLIUM
I
, I. Introduction
* < These guidelines cover requirements necessary to qualify
— ' i
• for a waiver of emission testing for beryllium extraction
' plants, machine shops, ceramic plants, foundries, and
I • others processing beryllium-containing materials.
I
1. Beryllium Emission Limit
I According to Section 61.32, Suupart C, of the National
!
j Emission Standards for Hazardous A1r Pollutants, total
mt •• effluents emitted to the atmosphere from a source must be
m controlled so as to limit beryllium emissions to a maximum
™ of 10 grams in a 24-hour period,
• 2. Waiver of Emission Tests
Emission tests - initial, periodic or both - may be
1 waived upon written application to the Administrator, if in
I his judgement the source is meeting the applicable emission
i . limits or 1f the source 1s operating under a waiver of
• , compliance or has requested a waiver of compliance.
| ! Sources not meeting the requirements of II(a) below may
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apply for waiver of emission testing. The decision on
the application will be based on the amount of material
processed, the type of operation, the type of control
system Installed and special factors pertinent to that
source.
II. General Waiver Qualifications
The following requirements are necessary to qualify for
a waiver of emission testing and recordkeeplng required
by the National Emission Standards for Hazardous A1r
Pollutants, Section 61.13.
a* Sources which certify that less than 10 pounds per
month of beryllium 1s processed will automatically
be granted a waiver of both Initial and periodic
emission testing.
b. The source must be controlled so that the total
effluents emitted to the atmosphere do not contain
more than 10 grams of beryllium 1n a 24 hour period.
c. Control equipment and operation thereof must be
correctly represented 1n the waiver request application
and must continue to exist and be operated as was
represented. If source test results were submitted
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with the waiver application, collection efficiencies
M shall continue to equal or exceed those claimed 1n
• the application.
I III. Required Information for Waiver of Emission Testing
I
The following specific Information concerning the beryllium
control systems with which the facility is attempting to
m qualify for a waiver must be supplied with the waiver
application.
• 1. Process Information
™ i
a. Complete flow diagrams of all operations contributing
I
to emissions. Include material balances.
b. Estimated flow rate, composition, temperature, and
^ other pertinent Information on atmospheric emissions.
c. Location and number of emission points.
I
d. Operations considered to be the major sources of
emissions.
I e. Process calculations having any bearing on emissions
and emission rates.
f. Effects of startup, shutdown and abnormal operation
1
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on emission rates. Description of process instrumentation
which can correct overloads or failures (such as alarm
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for ruptured prefliter or an override on a recording
flow control to a baghouse).
2» Control Equipment Information
a. Engineering design calculations, including assumptions,
operation principle, and operating variables affecting
performance and efficiency,
b« Manufacturer and ntudel number.
c. Equipment specifications including: design capacity,
guaranteed efficiency, performance, operating instructions.
Include,, where applicable, information such as:
allowable pressure d,- . , gas velocity, filter ratio,
temperature, partlculate gas loading, etc.
d. Equipment drawings*.
e, Engineering drawings of control equipment as
Installed; wHh ductst hoods, fans, piping and other <
auxl S ic»f>., *.
\
f,, Spare pa^ts wn'.ch a^e proposed.
g, Scheduled maintefsance procedures,
3, Source Tests for Emission
If requested, the results of an emission test performed
according to EPA-approveo sampling and analytical techniques
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published with the standard must be Included 1n the waiver
• application. All reports should Include the name and
, telephone number of a company representative who can be
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contacted to clarify any Information submitted.
IV. Suggested Procedures for Applicants for Waiver of
Emission Testing
_
The following maintenance and Inspection procedures,
• where applicable, are suggested for those sources applying
• or qualifying for a waiver of emission testing.
- 1. Fabric Filters
The following maintenance and operating procedures
«hall be adhered to wherever fabric filters (baghouses)
are utilized to control emissions regardless of their
position 1n any specific control arrangement.
Dally Inspections
1. The clean side of all baghouses must be Inspected
for leaky, torn, or poorly sealed bags. In cases where
• sufficient light 1s not available to properly Inspect
all bags, a portable light source shall be used.
2. All dust tubes shall be Inspected for abrasion
ft . or wear.
3. The clean side of the cell plant floor shall be
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Inspected for any dust accumulation. Dust build-up 1n this
area 1s evidence of leaky fabric filters or cell plate joints.
Weekly Inspections
1, The baghouse housing shall be Inspected for air
leaks and all Interior sections checked for excessive
abrasion or wear.
2. The shaker mechanism shall be Inspected for
proper condition.
3. All fans, drivers, and power equipment shall be
Inspected for wear, damaged parts and leaks.
General Maintenance
1. All maintenance and Inspection requirements
cited by the manufacturer of the subject control equipment
shall be strictly adhered to with the exception of those
that require fewer Inspections to be performed than cited
In this document.
2. Periodic Inspection of the dust collector housing
and structural components 1s required. All bolts shall be
Inspected and tightened and Inspection door seals checked
for leaks.
3. Upon determination of any unsatisfactory conditions
of control equipment. Immediate correction action shall be
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taken. In order to avoid excessive emissions and/or loss
of operating time, a supply of spare parts shall be
maintained. Control equipment manufacturers should
provide recommendations as to which parts should be kept
I on hand. In all cases, enough wearable parts and fabric
m filters should be stocked to equip one baghouse or one
compartment of a baghouse.
•»
Fabric Filter Material and Construction
*
In the event filter material, filter construction, or any
control or process variable that may adversely affect
m
I collection efficiency or increase total emissions 1s
• changed after a source test waiver has been granted, the
waiver 1s cancelled until these changes have been approved
m by the Administrator.
| 2. HEPA Filters
_ The following maintenance and operating procedures
* shall be adhered to wherever HEPA (High Efficiency Partlculate
• A1r) filters are utilized as the final emission control
device 1n any control arrangement.
Maintenance
• 1, Filters and mounting frames shall be visually
Inspected on a dally basis for damage or defects. Special
• j attention shall be paid to the assurance of a proper
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filter seal to the frame, condition of frame clamps, and
any obvious damage to both frame and filters.
2, Pre-fliter banks shall be visually Inspected
on a weekly basis for damage or defects. Special attention
shall be paid to the clean side of pre-fliter banks where
any leaks may be Indicated by the presence of soiled or
discolored areas.
3. The filter housing shall be Inspected for air
leaks and damaged or corroded areas that may result 1n
filter damage and the reduction of both filter efficiency
and life.
4. Prior to Installation of HEPA filter, the following
Inspections shall be performed. A record shall be retained
verifying performance of such Inspection for the period
1n which the filter is 1n service.
a* Exposed filter areas shall be visually Inspected
with the aid of a strong light source for cracks,
plnholes, and breaks. Special attention shall be
paid to the presence of cracks or breaks on the edge
of the filter pleats and the adhesive seal around
the filter unit face.
b. The filter case gasket shall be Inspected for non-
uniformity of thickness, Improperly formed comers,
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•Incomplete bond to the filter housing, degraded
normal plant operations.
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m , 6. Upon determination of any unsatisfactory conditions
I!
of control equipment, Immediate corrective action shall
j be taken. Exhaust gases normally passed through HEPA
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filters prior to entering the atmosphere shall not be
f emitted 1n the event the HEPA filter control arrangement
Is defective or damaged 1n any way that may affect filter
• efficiency. Such conditions Include, but are not limited
to, those cited 1n this document with respect to the
I HEPA filter and/or the HEPA filter bank.
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HEPA Filter Material and Construction
Ij In the event filter material, construction, specifications,
|
I or any control or process variable that may adversely
I * affect collection efficiency or Increase total emissions
1s changed after a source test waiver has been granted,
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the waiver 1s cancelled until these changes have been
approved by the Administrator.
V. Evaluation of Information Submitted with Testing
Waiver Application
The application examiner can automatically grant a waiver
for cases covered by II(a) above. In other cases, he
must be convinced that beryllium emissions have been or
will be kept within the limits shown 1n II(b). The safest
course 1s to act upon the evidence of actual source tests
submitted with the waiver application. Here, the examiner
must convince himself that the data are truly representative
and not accidentally low.
In the absence of source tests, the safest course 1s
to realize that control equipment will probably operate
satisfactorily 1f 1t has a history of good operation
1n similar duties elsewhere. Accordingly, we hereby
present Figures 1 through 8. These figures show
the controls used 1n several beryllium machine shops and
a foundry and ceramic plant. All of these sources were
tested by EPA and were found to be well-controlled. These
figures are given for perspective, however, and should not
be used to judge waiver applications.
The Information received with an emission testing waiver
application should be evaluated by an experienced engineer.
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FIGURE 1
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SOURCES AND CONTROLS \
1. Beryllium Machine Shops
Emission Point A2
.
unip ^01 lecLiun
MarhinP1; 9 lathes i ; ...
in Material - ' — __ r~~"j
Operation Be j~~~[
__ r~-i
i 1
<— .I
i i
ST3 — ' /~^» •
r f
Baghouse
"1
jl I
Test! Point <
i
rV
1 •
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s
y
i 1
Number of bags 45 45
1
1
1
1
M
1
1
1 '
I
61 61
Total cloth area 188 188 383 383
(ft2)
Avg. air to cloth
ratio ft
Avg. total
(min)
flow
rate (cfm)
4.3
4800
Fabric specifications:
Material
- silicon treated cotton
weave - 12
Thread count - 78 x 70
Permeability - 4-4.5 cfm/ft2
Max. temp. - 180°F
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Test Point
FIGURE 2
Emission Point Al
Machines in Operation
t
9 mills
Material - Be
Chip Collection
i — -H i
4
Number of bags > 61
Total cloth area (ft2) 383
Jaghouse
^"
6'
3*
L
13
\^^
Avg. air to cloth 2.8
ra tio'( ft/mi n)
Total flow rate (cfm) 1600
Fabric Specifications: same as A2
12
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FIGURE 3
Emission Point A3
A-3
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Emission Point Bl
Machines in
operation
15 Lathes
13 Dry
2 Wet
Material Be
Emission Point 82
FIGURE 4
Avg. flow rate (cfm) 2960
Test
Point
CP
Baghouse
•e-
Machines in
operation
2 Grinder,
wet
Material BeO
Avg. flow rate (cfm) 920
14
Test
Point
Baghbuse
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FIGURE 5
-:-:-,i.-.. r'o!:tt 3-3
Operations
3 mills-wet
2 ultra sonic-wet
1 lathe dry
1 Grinder-wet
material BeO.Be
Test
Point
Baghouse
Avg. flow rate (cfm) 1875
15
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FIGURE 6
2. Beryllium-Copper Foundry
Test Point C]
Emission Point
cooling
Test
Point
V
Cyclone
Test
Point
Bag-
House
Avg. flow rate (cfm) 20,435
Permeability ft/min 15-25
Material Dacron
Total filter area (ft2) 7,986
Fabric count 78 x 74
Air to cloth ratio (ft/min) 2.5
16
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FIGURE 7
3. Beryllium Oxide Ceramic Plant
Emission Point D-l
Operations
Machining
Grinding
Formi ng
Weighing
etc.
Mt. BeO
nrs/uay
\r
i
(T
L
_
1
0— i
t—
n
l_;
i
i
<=
r
r
c.
n i Te!
) Pnii
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1
1
i
<
5t
->4-
It
(
\
Pre-Filters
HEPA Filter
Dimensions (ft) 4'x4'xT
Avg. Flow Rate (cfm) 18,900
17
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Emission Point D-2
FIGURE 8
Spray
Drier
40 Ibs
BeO/hr.
r
C
I
\>
I
Baghouse
Reverse
Jet
Test ^
Point v>
HEPA
Filter
Bag Material - Dacron, Silicon treated
Avg. flow rate (cfm) - 1,857
Cleaning Cyclo - 2 ea., 5 sec. pulses per min.
Emission Point 0-3
Calciner
250-660°C
Zone Heating
I
Test
Point
Pre
Filter
HEPA
Filter
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This can be performed 1n as much detail as manpower
8 I will allow, consistent with the number and complexity of
emission points and control devices. As a minimum, the
evaluator must match gas flows from the material
balance to the available area of the various filtering
devices proposed and given in the vendors specifications.
Beryllium extraction plants have all been designed to
limit ambient concentrations of beryllium to 0.01
micrograms/cu meter and have demonstrated the capability for
operation within this limit. They have a great variety
of potential beryllium emission sources. Appropriate
practices for control o* fmissions include:
1. Ventilation hoods of very careful design.
2. Removal of larger partlculates by prefilter,
followed by HEPA filter for fines.
3. High energy wet collectors.
The following general comments may act as a guide to
the waiver evaluator.
1. Wet Collectors
In general, wet collectors are applied in beryllium
handling to remove hot, wet, sticky, agglomerating, hygroscopic,
or inflammable materials from a gas stream. Efficiency is
not high enough to remove submicron particles satisfactorily.
19 .
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2. Fabric Filters
These devices have over 99 percent efficiency for
ore handling operations of crushing and milling, and for
handling dry beryllium hydroxide. They are used to
control emissions from conversion of beryllium metal
billets to metal forms; and of beryllium hydroxide to
alloys, oxide powder, and ceramics. They depend upon
use of filter aids and buildup of a cake, for their
highest efficiency* Oaoron, Orion and nylon are used
for fine partlculates because cotton sateen bags are more
easily blinded by fine dusts. The usual filter ratios are
1:1 to 1:3 cfm/sq ft cloth area, and operating pressure
drop range 1s about 2" - 8" H-O.
The choice of an effective filter can be made with
confidence only on the basis of previous successful
operating experience with a similar system. Otherwise,
the determination of a satisfactory combination of filter
fabric and bag cleaning system should be considered as
a development program, rather than as an engineering task.
20
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3. Prefliters
These filters are frequently utilized to protect
HEPA filters from high partlculate concentrations. They
can be designed to collect high concentrations of the
larger particulates; this statement applies particularly
I
to the viscuous impingement panel type. There are
two other, extended medium, dry type prefliters which
operate at higher pressure drops and have higher dust
collection efficiencies. Some idea of the nominal
values of air handling capacity, pressure loss and dust
holding capacity of prefilters is given by Table 1.
The cited dust holding capacities are those for Cottrell
precipHator dust as determined by NBS test method. The
properties of a beryllium dust might produce a considerably
different dust holding capacity.
21
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CO
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o u u u
X Id «0,
I D.O O|
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ou.
o «
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in
o
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•
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to
•
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*
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in
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4. HEPA (High Efficiency Participate A1r) Filters
This 1s a filter with very extended surface. The
filtering medium (a special fibre glass or paper sheet) 1s
wrapped 1n an S pattern across corrugated metal or ceramic
spacers which support the fragile filter sheet and
maintain the appropriate spacing between adjacent faces of
the filter medium. The dusty gas enters the filter
at the covered edges of the paper supports, flows Inward
parallel to the paper, and then passes at right angles
thru the numerous layers of filter sheet.
The HEPA filter 1s defined by the following specifications:
a. It 1s an extended-medium, dry, throw-away type.
b. Collection efficiency 1s at least 99.97 percent
for partlculates of 0.3 micron diameter.
c. Clean flow resistance at rated air flow capacity
Is no larger than 1.0 Inch w.g.
d. A rigid housing extends the entire length of the
filter medium.
The waiver evaluator should compare the proposed air flow
to the filter with that 1n the vendors recommendations.
23
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Overpressurlzatlon of HEPA filters for even short periods
of time can rupture the filter medium, or even cause
complete blowout of the filter core. Instrumentation
should exist to prevent excessive airflows leading to
filter damage. The shock overpressure resistance, which
1s the maximum short-duration overpressure that a filter
can sustain with no visible damage and no decrease 1n
collection efficiency, 1s shown 1n Table 2.
Table 2. SHOCK OVERPRESSURE RESISTANCE OF OPEN-FACE HEPA FILTERS
Overpressure (pslg)
Filter
Dimensions. (In
Face
8 by 8
8 by 8
12 by 12
24 by 24
24 by 24
A
Tepth
3 1/16
5 7/8
5 7/8
5 7/8
11 1/2
Test
Vilua*
3.6
4.5
3.6
2.2
3.2
Recommended .
Design L1m1tD
With Face
Guards
3.1
3.8
3.1
1.9
2.7
Without Face
Guards
2.0
2.5
2.0
1.2
1.8
"dean filter with 4 by 4 mesh face guards on both faces.
bD1rty filters.
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• ^ The nominal dust-holding capacity of HEPA filters varies
with the type of particulates, but 1s approximately 4
| pounds per 1000 cfm of rated gas flow capacity. Prefliters
B are definitely recommended 1f the particulate loading
™ 1s greater than 50 nrfcrograms per cubic meter.
• Particles having a fibre or flake form are capable of
• * Inducing rapid clogging of a HEPA filter.
_ ] 5. Beryllium Machine Shops
j Figures 1 through 5 Illustrate some of the
• 1 emission controls.
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; Finish cutting and grinding operations produce more and
« finer particulates than rough cutting. Open face hood
velocities usually range from 150 to 300 fpm. Dust
• j and chip capture velocities range from 500 to 3000 fpm.
Transport velocities are usually 3000 to 4000 fpm.
6. Foundries
* ' Gas fired lancing forms excessive fumes. One
• i foundry control 1s shown 1n Figure 6.
\
• i The evaluator should check emission controls for finishing
operations, which are dusty, and Involve cutting, grinding
i i
and buffing. Fabric filter installations have bags with
I
25
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air flow permeabilities 1n the range of 15 to 25 cfm/sq ft
and have been successfully operated at filter face
velocities of about 2 ft/m1n 1n beryllium - copper foundries.
The filter vendor's recommendations should be noted.
7. Beryllium Oxide Ceramics
Controls useful 1n ceramic plants are shown in
Figure 7 and 8. Such plants generate considerable submicron
partlculates.
26
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I
!
GUIDELINES FOR WAIVERS OF EMISSION
TESTING IN FACILITIES INVOLVING
MERCURY
I. Introduction
These guidelines cover requirements necessary to qualify for
a waiver of emission testing for mercury extraction facilities
•
and facilities using mercury chlor-alkali cells to produce
chlorine gas and alkali metal hydroxide,
A. Mercury Emission Limit
According to Section 61.52,, Subpart E, of the National
Emission Standards tor Hdiardoub Air FulluiauLA, i,ul«u merCur v
emissions to the atmosphere from a source must be limited to a
maximum of 2300 grams in a 24-hour period. This limitation applies
to the stack gas emissions from mercury extraction facilities
and the combined hydrogen stream, end-box ventilation stream,
and cell-room emissions from chlor-alkali facilities using mercury
cells. Sources subject to the mercury standard must ver'f? their
compliance by conducting periodic emission tests, Section 61 ..53
of the National Emission Standard for Hazardous Air Pollutants
includes provisions for the initial and periodic testing of
both types of affected facilities.
B. Waiver of Emission Tests
Emission tests - initial, periodic or both - may be
waived upon written application to the Administrator, if in his
1
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Judgement the source 1s meeting the applicable emission limit
or 1f the source 1s operating under a waiver of compliance.
Sources not meeting the requirements of II(a) may apply for a
waiver of emission testing. The decision on whether or not to
grant the waiver will be based on the amount of material processed,
the type of operation, the type of control system Installed,
and special factors pertinent to that source.
II. General Waiver Qualifications
The following requirements are necessary to qualify for a
waiver of emission testing under Section 61.13 of the National
Emission Standard for Hazardous Air Pollutants.
A. Mercury extraction facilities which are either retort
operations producing 2 .^sks of mercury per day or less
or directly heated operations with capacities of 20 tons
of mercury ore per day or less will automatically be granted
a waiver of both initial and periodic emission testing.
B. Sources not qualifying for an automatic waiver of
testing under II(A) must be controlled so that the total
effluents emitted to the atmosphere do not contain more
than 23QO grams of mercury per 24-hour period.
C. Control equipment and operation thereof must be correctly
represented in the waiver request application and must continue
to exist and be operated as was represented. If source
test results were submitted with the waiver application,
collection efficiencies should equal or exceed those claimed
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I
I
|1n the application.
, , .. -
_ D'. Owners or operators 'of facilities employing mercury
chlor-alkall cells may demonstrate compliance with the
8 cell room ventilation portion of the allowable emissions
by applying the following design, maintenance, and house-
I keeping practices specified by the Administrator. Initial
•* and periodic source test requirements applying to the cell
room will then be waived. A- value of 1300 grams of mercury
I per day will be assigned to the cell-room emissions.
• (a) Chlorine cells and end-box covers should be
Installed, operated, and maintained in a manner to
•' minimize leakagt of mercury and mercury-contaminated
materials.
(b) Daily inspection should be made by operating
| personnel to detect leaks, and Immediate steps to
_ stop the leaks should be taken.
(c) High housekeeping standards should be enforced
• and any spills of mercury should be prompt!: cleaned
• up either mechanically or chemically, or by other
appropriate means. Each cell room facility should
• have available and should employ a well -defined
procedure for handling these situations.
(d) Floor seams should be smoothed over to minimize
«
depressions and to facilitate washing down of the
floors.
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(e) All floors should be maintained in good condition,
free of cracking and spall ing, and should be»regularly
Inspected, cleaned, and to the extent practical, chemically
•
decontaminated.
•
(f) Gaskets on denuders and hydrogen piping should be
maintained 1n good condition. Daily inspection should
be made to detect hydrogen leaks and prompt Corrective
action taken. Covers on decomposers, end-boxes, and
mercury pump tanks should be well maintained and kept
closed at all times except when operation requires
opening.
(g) Precautions should le taken to avoid all mercury
spills when changing graphite grids or balls in horizontal
decomposers or graphite packinq in vertical decomposers.
Mercury-contaminated graphite should be stored in closed
containers or under water or chemically treated solutions
until it is processed for reuse or disposal.
(h) Where submerged pumps are used for recycling
mercury from the decomposer to the inlet of the chlorine
cell, the mercury should be covered with an aqueous
layer maintained at a temperature below Its boiling point.
(i) Each submerged pump should have a vapor outlet with
a connection to the end-box ventilation system. The
connection should be under a slight negative pressure
so that all vapors flow into the end-box ventilation system.
-------
(j) Unless' vapor tfght covers are provided, end-boxes
• » • •
of both Inlet and outlet ends of chlorine cells should
* i •
be maintained under an aqueous layer maintained at a
temperature below Us boiling point.
(k*) End boxes df cells should either be maintained under
a negative pressure by a ventilation system or should be
equipped with fixed covers which are leak tight. The
ventilation system or end box covers should be maintained
1n good condition.
(1) Any drips from hydrogen seal pots and compressor
seals should be collected and confined for processing
•
to remove mercurv, and these drips should not be allowed
to run on the floor or in open trenches.
(m) Solids and liquids collected from back-flushing
the filter used for alkali metal hydroxide should be
collected in an enclosed system.
(n) Impure amalgam removed from cells and mercury
recovered from process systems should be stored r> an
enclosed system.
(o) Brine should not be purged to the cell room floor.
Headers or trenches should be provided when it Is
necessary to purge brine from the process. Purged brine
should be returned to the system or sent to a treating
system to remove Its mercury content.
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(p) A portable tank should be used to collect any
mercury spills during maintenance procedures.
(q) Good maintenance practice should be followed
when cleaning chlorine cells. All cells when cleaned
should have any mercury surface covered continuously
with an aqueous medium. When the cells are
disassembled for overhaul maintenance, the bed plate
should be either decontaminated chemically or thoroughly
flushed with water.
(r) Brine, alkali metal hydroxide, and water-wash
process lines and pumps should be maintained in good
condition, and leaks should be minimized. Lea!;:;
should be collected n -u1table containers rather than
allowed to spill on floor areas.
III. Required Information for Waiver of Emission Testing
The following process data and Information concerning the
mercury control systems with which the facility is attempting to
qualify for a waiver must be supplied with the waiver application.
A. Process Information
1. Complete flow diagrams of all operations contributing
to emissions. Include mpteHal balances.
2. Estimated flow rate, composition, temperature,
and other pertinent information on atmospheric emissions.
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I
I
3. Location and number of emission points.
4. Operations considered to be the major soyrces
of emissions.
•
5. Process calculations having any bearing on emissions
and emission rates.
6. Effects of startup, shutdown, and abnormal operation
on emission rates. Description of process instrumentation
designed to correct overloads or failures.
B. Control Equipment Information
1. Engineering design calculations, Including
assumptions, operation principle, and operating variables
affecting performance and efficiency.
2. Manufacturer and model number.
3. Equipment specifications, include: design capacity,
guaranteed efficiency, performance data, and operating
Instructions. Include, where applicable, Info-nation
such as: allowable pressure drop, gas velocity, temperature,
particulate loading, etc.
4. Equipment drawings.
5. Engineering drawings of control equipment as installed;
with ducts, hoods, fans, piping and other auxiliaries.
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6. Spare parts required.
7. Scheduled maintenance procedures.
C. Source Test for Emissions
If requested, the results of an emission test performed
according to EPA - approved sampling and analytical techniques
published with the standard must be included 1n the waiver
application. All reports should Include the name and telephone
number of a company representative who can be contacted to
clarify any information submitted.
IV. General Maintenance and Inspection Procedure
The following general maintenance and inspection procedures
are suggested for those sources applying or qualifying for a
waiver of emission testing.
A. All maintenance and Inspection requirements cited by
the manufacturer of the subject control equipment should be
strictly adhered to with the exception of those that require
fewer inspections to be performed than cited 1n this document,
B. If the good housekeeping option is used to demonstrate
compliance with the cell room ventilation portion of the
allowable emissions from a chlor-alkali facility, the maintenance
and inspection procedure discussed on pages 3-6 must be followed.
C. Upon determination of any unsatisfactory conditions,
corrective action should be taken. In order to avoid excessive
8
-------
emissions and/or loss of operating time, a supply
of spare parts should be maintained. Control equipment
t
manufacturers can provide recommendations as to which
•
parts should be kept on hand.
V. Evaluation of Information Submitted with Testing Waiver
Application
•
The sources meeting the requirements of II(A) or II(D) should be
automatically granted a waiver of emission testing. When evaluating
the application of sources not qualifying for an automatic waiver,
the examiner must be convinced that mercury emissions have been
or will be kept within the allowable Urit (2300 grams per ^-nour
period). The safest course is to base any decision upon actual
source test results submitted with the waiver application. In
this case, the examiner must convince himself that the data are
truly representative and not accidentally low.
The Information received with an emission testing waiver application
should be evaluated by an experienced engineer. This can t,<
performed in as much detail as manpower will allow, consistent
with the number and complexity of emission points and control
devices. As a minimum, the examiner should compare the gas flow
rates, temperatures, and mercury concentrations with the values
listed in the vendors specifications and use the estimated collection
efficiencies of the control equipment to calculate an approximate
emission rate.
-------
The condenser gas stream is the major source of emissions
from a mercury extraction facility. Appropriate control techniques
Include cooling and mist elimination, wet scrubbing, er absorption
beds. Major emissions of mercury from chlor-alkali- plants using
mercury cells are from the hydrogen gas stream, the end-box
ventilation stream, and the cell room ventilation air. Emissions
from the hydrogen gas and the end-box ventilation air streams
can be controlled by cooling and mist elimination, chemical
scrubbing, or adsorption beds. No techniques are presently
available to control the cell room ventilation air. The control
of emissions from this source is dependent upon the application
of the good housekeeping practices presented in Section II of this
document.
The following general comments "^xr-ning control techniques
may act as a guide to the waiver evaluator.
A. Cooling and Condensing
The cooling of a gas stream containing mercury vapo** below
Its mercury saturation temperature will cause the vapor to
condense, thereby reducing the mercury content of the gas.
Cooling can be accomplished by the use of either direct or
Indirect cooling techniques. Because of the large particulate
loading of several of the process gas streams, direct cooling
methods may possess an advantage over indirect methods since
direct cooling would aid 1n mist and particulate removal. The
use of direct cooling, however, would also introduce the
10
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I
necessity of water treatment facilities and create the possibility
of a water pollution problem.
In order to be effective as a control technique, cooling should
be followed by some type of mist elimination device.
B. Mist Elimination
There are two basic types of mist eliminators commercially
available to remove mercury mist from process gas streams. One
of these consists of a fiber bed, equipped with water sprays,
that removes the entrained mist by the mechanisms of impaction,
Interception, and Brownian movement. A high particulate loading
(of contaminants other than mercury) may cause the efficiency of
this device tc be Icv/cr 1 ^n normal. L'3c of additional flushing
water within the mist eliminator or installation of air precleaning
equipment prior to the mist eliminator may effectively solve the
problem. The particulate mercury removal efficiency of this
type of mist elimination device has been estimated at 86 percent.
Another type of mist eliminator utilizes a coverglng - diverging
nozzle arranged so that the gases being cleaned follow o ,<'rved
path and are acted upon by high centrifugal forces in the
throat area. These forces are reported to cause the coalescence
of mercury mist and entrapment of sub-micron mercury particulate
upon the upper wall of the divergent section. This mist eliminator
1s reported to have an efficiency comparable to that of the fiber
pad type mist eliminator.
11
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C, Wet Scrubbing • •
Wet scrubbing devices employ a variety of mechanisms
to collect particulate matter. Interception of partlculate
matter by liquid dro'plets resulting In a heavier dust-liquid
•
agglomerate Is the most important of these mechanisms. Particulate
matter collected on a liquid droplet in this manner can be
efficiently removed from the gas stream by a centrifugal collector.
The particulate collection efficiencies of wet scrubbers vary
with energy input and can extend over a wide range depending on
the design.
The venturi scrubber is a high-energy, high efficiency scrubber
•
that has been used to remove particulate matter from gas streams
•
similar to the stack gas streams of mercury extraction facilities.
The water necessary to scrub a ,oOO SCFM gas stream is estimated
to be between 5 and 9 CPM, depending on the gas loading and
size distribution of the partlculate matter. It is expected
that a particulate collection efficiency of 95 percent cc-jld be
achieved with a pressure drop of 20 to 30 inches of water through
the venturi and cyclone.
D. Chemical Scrubbing
1. Depleted Brine Scrubbing
The depleted brine scrubbing technique uses the brine
discharged from the chlorine cell as the scrubbing
liquor. This depleted brine contains about 250 grams
per liter of sodium chloride and 0.6 to 0.9 grams per
12
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I
I
• lit'er of available chlorine; it has a pH of from 2
to 4. The solution is used as the scrubbing medium
in a sieve plate tower or in a packed bed scrubber.
M Upon contact with the brine scrubbing solution, the
mercury vapor and mist form soluble mercury complexes.
Mercury can be recovered by electrolysis when the
scrubbing medium is recycled to the cell. The exit
mercury concentration of a hydrogen stream treated by
H this system has been reported to be approximately 85
micrograms per cubic meter.
• 2. Hypochlorite Scrubbing
• This system employs a dilute solution of sodium hypochlorite
with a large excess of sodium chloride over the
• stoichiometric quantity. The mercury removal efficiency
of this system is maintained over a wide enough pH range
• to make control possible. A mercury collection efficiency
of 95 to 99 percent has been reported.
E. Adsorption Beds
1. Treated Activated Carbon
Control systems containing either sulfur or iodine-
impregnated activated carbon are being utilized by several
chlor-alkali facilities for reduction of the mercury
concentration in the hydrogen stream. In these systems,
the mercury vapor is adsorbed by the carbon and chemically
13
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reacts with 'the iulfur of Iodine to form mercury
* * *
compounds. Some problems could arise 1f substantial
amounts of particulate mercury are present In the gas
stream; however, this situation could be corrected by
•
• t
either preheating the gas stream or by using a mist
elimination device prior to the carbon bed.
In order for treated activated carbon to perform
efficiently, the gas stream velocity through the bed
should be In the range of 20 to 40 feet per minute.
This low gas velocity is required to allow sufficient
contact^time between the mercury and the treated carbon.
A mercury vapor collection efficiency of approximately
90 percent is expected. Destructive distillation of
the spent carbon appears practical for recovering the
adsorbed mercury.
2. Molecular Sieve
The molecular sieve control technique utilizes a sieve-
adsorbent blend to adsorb the mercury contained in the
gas stream. A molecular sieve system currently available
for the treatment of both the hydrogen gas and the end-box
ventilation streams of chlor-alkali plants is the
PuraSiv - Hg System. The designer of this system
guarantees a reduction of the mercury concentration to
0.50 milligrams per cubic meter.
14
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I ..
i ••;•'.-
i
I GUIDELINES FOR' WAIVERS OF
•COMPLIANCE WITH EMISSION STANDARDS
_ FOR BERYLLIUM
_ I. Introduction
• 1. Legal Basis for Waivers of Compliance.
• According to Section 61.10 of Subpart A of the National
| Emission Standards for Hazardous Pollutants, the operator of
| an existing stationary source unable to operate 1n compliance
_ with the standard prescribed under Subpart C may request a waiver
™ of compliance with such standard. Therefore, a plant that is
• operating (including plants that are starting up) at the time the
NESHAP 1s promulgated and that is a source category covered by the
£ «t»»tri;irri should be eliaible for a waiver of compliance. Plants
f not 1n operation on the date of promulgation should not be
•• granted waivers of compliance. An eligible plant may apply to EPA
1M for a compliance waiver by presenting the information required by
Section 61.10 of NESHAP. Presentation of complete and necessary
I Information is the operator's responsibility and should be done
.
_ with his first transmittal of Information, drawings, and data.
™ It 1s particularly important for him to be concise on his ^ onosal
fl for emission controls and on the timetable for their accomplishment,
^
m II. Guidelines to Length of Waivers
According to Section 61.11 of NESHAP, the Administrator may
• grant a waiver of compliance with the beryllium emission standard
for a period not exceeding tv/o years.
I
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The request for a waiver of compliance should Include the
>
listing of certain milestone dates 1n a plant's effort to achieve
compliance. The persons 1r EPA evaluating a waiver request should
use the information presented 1n Section III as a guideline to
determine the length of the waiver. It is suggested that the
milestone guidelines be used as follows:
A) If the owner's or operator's requested lead time is .
less than the EPA guideline time, allow a waiver time equal to
•
the operator's requested lead time.
B) If the owner's or operator's requested lead time exceeds
the EPA guideline time by up to 20 percent, allow a waiver time
equal to the operator's requested lead time.
C) If the owner's or operator's requested time exceeds the
EPA guideline value over 20 percent., justification must be
supplied for this longer milestone time or the EPA milestone
lead tire? will be granted.
III. Derivation of Allowable Waiver Lengths
1. Operations Involved in Emission Control.
Table I shows a typical sequence of ooerations Involved in
the design and construction of any sizable emission control equip-
ment. Major activities are Included; many minor ones are omitted.
If a simple item like a small cyclone were the only one installed,
many of the 23 listed operations would not be involved. The most
complex case would involve large baghouses with new fans and
ductwork.
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, i
4
i
TABLE I. SEQUENCE OF OPERATIONS IN
DESIGN AND CONSTRUCTION OF BERYLLIUM EMISSION
CONTROL EQUIPMENT.
1. Process design and flow diagram. • ^
2. Engineering flow diagram and preliminary plot plans.
3. Specification and procurement of major items such as fans
and baghouse.
4. Specification of minor items, obtainable without complete
i
drawings.
5. Design of electrical starters, switch-gear and distribution system,
6. Duct and piping arrangements and specifications.
7. Foundation design.
8. Structural steel design.
9. Receipt of certified dimension drawings of fans, baghouse, etc.
10. Release of foundation and structural steel drawings.
11. Start construction.
12. Complete pipe and ductwork takeoffs, and drawings for field support
13. Release drawings and material listings for construction.
14. Complete underground installations.
15. Complete foundations.
16. Delivery of structural steel and major items of equipment.
17. Erect major items.
18. Install ductwork and piping.
19. Install electrical.
20. Install instrumentation.
21. Startup
22. Source testing and analytical.
23. Final report.
3
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Table I shows that, 1n general, design continues Into
procurement and Into the early part of construction. Nor can
>
design be complete until receipt of certified drawings; which
presupposes that equipment purchase orders have been'placed
sometime before. In short, many operations necessarily overlap.
Thus, the waiver evaluator should be an experienced engineer
who can deal with the real complexities of plant design and
scheduling; and - if at all possible - each waiver application
should be dealt with on a case by case basis. Only for a simple
retrofit is it possible to generalize on project timing with
very much confidence.
2. Time Requirements for Construction and Startup.
Table 2 gives the approximate lead times required for
fabrication, installation and startup of the equipment and
accessories likely to be Involved 1n retrofitting a plant
handling beryllium.
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Fabrication lead times are Influenced by many things, Including
size of equipment, materials of construction, general and specific
»
level of construction activity, condition of war or peace, foreign
and domestic labor trouble, government policies, and so on. This
1s largely because of the effects of the above upon materials
and labor availability. For Instance, foreign expropriation of
U. S, - owned copper mines can cause delays 1n delivery of
electrical equipment. A condition of war tends to Increase
delivery time for all non-military Items. The waiver evaluator
should make his own check on Table 2 lead times, especially 1f any
of the Items are large and costly, or 1f strategic iretals like
copper, nickel or chromium are Involved.
3. Events Required for Meeting Emission Standards.
A waiver request can be granted for up to 2 years, but the
actual waiver time allowance should only be that required to
design, install, startup, test and prove the performance of
suitable control equipment. For this overall objective, a
number of events must take place, or a number of milestones have
to be met. Table 3 Illustrates these events or milestones of
emission control progress. The reader should note the range
of time requirements. Table 3 fits no actual case. If one
package control item only were involved, events could tend to
be consecutive: thus, ordering could follow grant of waiver,
Installation would follow procurement, startup follow installation,
etc. In the more general case of more than one control, with
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each control requiring fabrication, no simple sequence of
consecutive events 1s possible. Instead, the events overlap
1n a manner which requires case - by - case study. Thus, the
wise operator will begin engineering design before he submits
t
his waiver application; and some design work must continue
during equipment fabrication and sometimes even continue Into
the Installation period. Fabrication starts as early as possible
on Items needed early; they may be installed while other items
are still being fabricated.
It 1s clear that the total time requirements suggested by
Table 3 apply to only a complex case, such as 1f a beryllium
extraction facility were suddenly to require emission controls
throughout (a hypothetical case). Early initiation of an activity
tends to be controlling (such as a quick start on bids and
fabrication). The lengthening of an activity (like engineering
design) is only important to the degree that 1t can lengthen the
overall time schedule. Startup, of course, must follow installation
without overlap. However, report writing can be partly done
before completion of source testing.
Line lengths on Table 3 indicate 5 month ranges for fabrication
and installation. But two 5 - month Items could require a
longer total fabrication time if not started simultaneously.
In other words, the total times for fabrication or installation of
all Items could be considerably more than 5 months, depending
upon proper project management.
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• 4. Compliance Wa(1ver,T1mq Requirements.
• The derivation of allowable waiver time 1s best represented
1 by specific examples. Consider an operation currently having
P bag filters. To Insure that beryllium emissions will be
^ maintained below the lega> fimits, a HEPA filter will be added.
* Its operating pressure drop will be low enouqh to require no
ft additional fan capacity, and additional ductwork will be minimal.
] This, then, 1s a simple case of addition of one equipment piece
0 without significant auxiliaries. The derivation of allowable
— waiver tiire is given in Table 4 and the total waiver time 1s
* the sum of Items in the last column of that table. The total
ft allowable waiver, time is therefore 302 days after grant of
v/aiver, assuming ordering activity started at time of waiver
ft grant.
I In Table 4, filter ordering includes writing specifications,
getting and comparing bids, and placing an order. Filter delivery
P Includes fabrication and assembly, shipping and delivery to
• jobs He.
M Note that the waiver evaluator must feel that the HEPA
^ filter addition will be an Improvement and will do the job;
i
ft otherwise he would refuse the waiver.
to Waiver evaluations for more complex situations can be treated
by a similar method, with exceptions as pointed out below. Consider
I a beryllium oxide ceramic plant which must add control equipment
to a certain operation. The flow 1s 10,000 cfm and a baghouse
I
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must be added. This baghouse must be proceeded by a cyclone
separator. Also, because of a wide particle size distribution,
a HEPA 1s advisable to remove part of the fines that escape the
baghouse.
Referring to Table 2, this case clearly involves design
and Installation of all of the equipment shown in the table,
including fan and extensive ductwork. One could therefore make
five tables (like table 4) to cover the five major items of
work. If we assume that design, procurement, and Installation
could proceed independently for each item/1.e. for baghouse,
fan, etc) the time to startup would just be the latest time shovm
among the five items.
For Instance, from table 2, the time for fabrication and
deliveries to the job site are:
cyclones 164 days
Im baghouse 164 days
, HEPA filter 164 days
jl fan 98 days
! ductwork 74 days
!• and this part of the job would consume 164 days if all orders
i
• were placed simultaneously. This can seldom happen, due to
manpower limitations and it 1s less likely to happen as the
I number of items increases.
• The waiver evaluation for addition of controls to the ceramic
plant is shown in Table 5. Time starts at arant of waiver.
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I
Procurement work was started first on the baahouse. It Is
assumed that the staff 1s not large enouqh to start on all
Items simultaneously, but that some work can be done on the
HEPA after 20 days, on the cyclone after 30 and on the fan after
40. The ductwork can be done right along, due to previous work
on engineering and to the simple specifications.
Other appropriate time requirements are added to Table 5
from Table 2. The on-site time for the various Items is
shown. Ductwork is available when other Items arrive. Some
of it can be installed after the fan arrives, most of it when
the baghouse is set up, and all of it wnen the HEPA is in place.
In other v/ords, all ductwork can be installed within about 150
days of 244 + 30 days (Hi.A column, table 5). However, we will
start installation when the fan is positioned, after say, 197
days. Our time schedule will be as shown in table 6 and will
be the total waiver time. Table 6 corresponds to column 3 in
table 4 for the simple case. The other missing columns may
readily be derived for the ceramic plant, to make a table like
table 4.
13
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TABLE 6 TOTAL WAIVER TIME FOR CERAMIC PLANT
»
Procurement 85 days ' .•
Delivery 98_
on site time 183
Installation, fan 14
Installation, ductwork 150
•
Startup 14
Source sampling & analysis 40
Final report 30
Total waiver time 431 days
Table 5 assumes one source sampling team, starting on the
HEPA exit and then moving to the baghouse. A less conservative
waiver time would assume ductwork Installation time to
commence upon positioning of the baghouse (I.e. 224 + 30 •»• 150
etc. days) for a total waiver time of 508 days.
A second method of estimating total waiver time for the
above beryllium ceramic plant v/ould Involve the use of critical
path techniques. To do this, one needs to 11st all of the tasks
Involved, from grant of waiver to final report. The time required
to perform each task Is then carefully determined and listed.
Secondly, the necessary and sufficient predecessor of each task
1s determined. In general, this will lead to two or more parallel
lines of tasks, or chains of milestones or events. In general, also,
14
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the time required to perform'each of these lines of tasks will
differ. The longest time path will be the allowable waiver time,
to be modified as shov/n in table 4. This critical path technique 1s
well known and 1s explained in numerous reference v/orks.
15
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•T
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GUIDELINES FOR WAIVERS OF
COMPLIANCE WITH EMISSION STANDARDS
FOR MERCURY
I. Introduction
1, Legal Basis for Waivers of Compliance.
According to Section 61.10 of Subpart A of the National
Emission Standards for Hazardous Pollutants, the operator of
an existing stationary source unable to operate in compliance
with the standard prescribed under Subpart C may request a waiver
of compliance with such standard. Therefore, a plant that is
operating (including plants trvc are starting up) at the time the
NESHAP is promulgated and that is a source category covered bv the
standard shou'M be eligible *'-.r a waiver of compliance. Plants
not in or>frai (.. > thr ' ,•* 'MS!Cation should not be
grant's; •. - , e plant may apply to EPA
frr a -ro", i -. -. i-:f f'V ,- • '"e ^formation requ*"rnd hv
Section 61,;. ' -{ SHAIJ, Prt-- :.L:,i- ./f complete and nec'lssarv
information i': t'-- operator'j r-\^- n•-• ^H ny and should be dr ie
v/ith his ?ir-i' ,.<• I'ssmittal of infom-.f>on, drawings, a°d data.
It is part:, .• < > important ^or film to tie concise oo his proposal
for en• ••.,.••'^ f-n.if;>is and on the timetable for their ac^. ishment.
II. Guidelines to Length of fivers
According to Section 61.11 of NESHAP, the Administrator may
grant a waiver of compliance with the mercury emission standard
for a period not exceeding two vt^r^.
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The request for a waiver of compliance should Include the
listing of certain milestone dates in a plant's effort to achiove
compliance. The persons in EPA evaluating a v/aiver request should
use the information presented in Section III as a guideline to
determine the length of the waiver. It is suggested that the
milestone guidelines he used as follows:
A) If the owner's or operator's requested lead time is
less than the EPA guideline time, allow a waiver time equal to
the operator's requested lead time.
B) If the owner's or operator's requested lead time exceeds
the EPA guideline time by up to 20 percent, allow a waiver time
equal to the operator's requested lead time.
C) If the ov/ner's or operator's requested time exceeds the
EPA guideline value over 20 percent, justification must be
supplied for this longer mllesx^ie time or the EPA milestone
leau ti>e v, 11 be granted.
Ill, Derivation of Allowable Waiver Lengths
1. Operations Involved in Emission Control.
Table I shows a typical sequence of operations involved in
the design and construction of any sizable emission control equip-
ment. Major activities are included; many minor ones are omitt; >.
If a simple item like a mist eliminator were the only one installed,
many of the 23 listed operations would not be involved. The more
complex cases would involve such items as chemical scrubbers, or
cell room modifications.
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TABLE I. SEQUENCE OF OPERATIONS IN
DESIGN AND CONSTRUCTION OF M
CONTROL EQUIPMENT,
1. Process design and flow ••; --i!i»
2. Engineer ;.'(=., !•;..* diagram *•..'< rn i •• inary plot plans,
3. SpecifH;atiu!\ and procurnM->.> c,' rvjor Items such as molecular
'if , 'i» t-innablf1 without complete
5,
siribution system.
/, f< •;:' 1ft! '•• : ...-
B H ?''»; ; i ' - '
1 ! ' . ' ,
12 •''• • I. .- ,
- ; , t J .. •'
"4, < :•', i l-r>
i«- n equipment.
' ;" ;i.'' ' '-;" .
^or field supnnrt
22
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Table I shows that, in qcneral, de/nn conn rues Into
procurement and Into the eurly part :. ' , .,, , [on, Nor can
design be complete until rerc^pt <">; v ; ' . .-'V.incs., which
presupposes that equipment purchase :-\ <•••.-,—, • %-c- been placed
some time before. In short, many operations necessarily overlap.
Thus, the waiver evaU'a*^'" should b.? ;>n exr^r- -:nrecl engineer
who can deal with *• ' <• ;': r ::plexit <; • "•'; • * .-ipv;..- ^r»H
schedul inri; ••• ••.,'-,:, , A-^ * •_•••••
should be k ,-.;•'.;• . , -, . , . , < ^ -^inple
retrofit is u po-.^ -> - ! • ,-• • M .- '.lining with very
much confidence,
2"| - r . > *~s t , *. - - s ,
t I ' E c, \ u « ,-
Table ." -;' - -r: ; - \ • • • . 1 'or
fabricatic . :•.• . • . •.••, ^'i
ce '< . \ fM- j o«"ii,i;irv . ,, » riro^i , :.••'_. It;;'t, 15
17 in1- o-vt process chap ...;ic,- cov. -• x •• - • ..-^ ,,
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• Fabrication lead times are Influenced by many things, Including
• size of equipment, materials of construction, general and specific
level of construction activity, r (•••-> <.i if ion of war or peace, foreign
| and domestic labor trouble, - ^enr policies, and so on. This
— is largely b-f,. . ,,, tiiL !•-'• •,-. -..: •• dbove t-p'^n materials
™
and lafior ,-\\-.\ •;• "?•; Kn , •:•••(•, rire <<'r-. -• > ;>r(V:riation of
• U, S. <'M,vJ • p; • r 'tis.-'S t.u. , :.,••.' ;i,'"i', " . ,s • ". ' ii"da"ds.
A v/aiv'-" - •• r -- t,r'» : ^r.-M'.eci f,; jp tr; ? years, but the
• actua" wa-V'.-; *•.:<• ! ••'•'., ,;,-s on)v ;>t' <.f-af f'Vouired to
•ic: ; v '••••• ' - -v • • ; -. ' .- ;.«r -run ,re of
• -' ' - •• 7 >ft
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tO be li ."I , ' • . •• i--', ^.iriijS
• emission coritrr • i'-ess, • -•.'•;.'?-> nns'Uf note the *anqe
of time tt ; ,-, r- ' *., fable '; f^r, no '*rtu-"«'! c.'.sA, If one
m pack?[-,- •• =- • -. >>;'v i- r '.- ,'•. •'/*-•.;, rvent-s >;o,.nd if ,
•j oe ee>r>-.'''. . . - . a-' •••, • ;u- i i- '.'., i " o» waiver,
• etc, ;« -oir. i^' c; . • - • tfi,
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each control ren.^rii>n fabric.iri'in, no :>4t-,ple scM(uencr» of
consecutive ; :•< • \ \'- j<'.;ss1!'
in a manne-r •,'••'••
wise oper-s* • • ' . •••' ii •*;-••
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• • t-il ioci .."i c*-- f:;> - Hems
It is clear that tne tot, "^' t
Table 3 apply to '-hlv a comp-e«, •>. t-,
mercur, ex^'ar 1 \ --rs < ^' > ,
cul rrinonts suggested by
v »i -'^ it" a large primary
, : *rnt, , i- emission
',;<", ir. ': ' ,-^tHin of an
» 0- '• <,tr"-*t r.p f-'^ls anil
, ' :' -• engineer inq
, • -' ' ' L -1 lotion
{irtore t •*'••, ,•'
raoncii v «
items could f
simul tdr,eA.-s 1
lon.;«r tot.,) r ar,r' c.at TO- r line it not started
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4. Compliance Waiver Time R<*;<-. • '?ents,
The derivation of dUowablp .? s i no is best represented
by specific exar-'ip-v, . certain ,, « r,-• urv extraction
facility has o>-3l^ed a new supplv t.t cola 'nountain v/ater v/hich
novi changes their mercury condenser ccoMnc water temperature
from 78°F to a new temperature of ro°(-. This results in increased
particulate me re urv emission and they ""H>e$t a v/aiver during
installation of ^ T,err...> ^ist el in incite-, 'Ms is a simnle case
of additi'-r. o"" ' -ir . -\,
The derivation of a'• h
the total v.Mv--r u-:.-j
that table, T» e • '
after gram at wa i ver
of waiver - - •'. .
', a i vf-r
.mfirant auxiliaries.
•""- *!ri "fable 4 and
.••!=• ir-st column of
! •; tnr-refore 271 days
• ly star.ed at time
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In Table 4, mist eliminator or<•"•'' :>
treated by a similar net hod, with e< -
below. Consider the folio M: ; •• mv»? >t
a chlor-alkali pl:»' -•> • ,:,jl(, • >
plant will ,,,e i >J;-;inicd! •••-•' r,
box vet'.t", ''^ -~>r. •• • 'i- ' - fi/fif. ,-<•'•,
can be
- -~ pointed out
,^,": -pceived from
i:\a ;.i.indard., This
.. ,- ;in jioth the end
v. - ' *• »r, to achieve
lov-e-/ ,r, t-,t, pla-it . - ;,5-. ; •
their end boxes and t*H- e vn 1 ] be cor, itr..;
and design work sill '• ie in-hou-.r
All the engineering
Referrinr t-.-. 'lat-i- , , this cas-; clearly involves design
and co- v.t >":>•• - '-> • " i:~., t ^ -• , ,a! tank, scruhbor,
mist eliminator,. . •. t ;-^ ,,-v. ?•-,„ _,>,. '>.-/:•. ,j',j Herhc.p> fan. However,
it will be assumed trial (-.-• addit'."'.--'! ''>**•• ". '"^lui^ed for
this job di.n auv n-^tde.: ; • ',. •-, ; 1 1 -e ' ••"• • ' ••! \/1th the scrubber.
One could there"(,M, HWK^ f^vt- t-. i • ' < ,• .. . 1; ti> cove,1
the five me • • ':..•„ t, - ^tsign, procurement
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_ and Installation could proceed independently for each item
' (I.e. for seal tank, scrubber, etc) the time to startup would just
I be the latest time shown among tK< five items.
• For instance, from tabie \'., tne tme for fabrication and
deliveries to the job site are-,
• scrubber 1^4 days
mist eliminator 140 days
• end t\jx covers 74 days
• and this part of the job would consume 194 days if all orders
were placed simultaneously, This can seldom hanpen, due to
• manpower limitanoris arid it is l- ss likely to happen as the
number of items increases,
The waive' * valuation f -: addition of controls to the
| chlor-aikalie plant is sf• rable 5, Time starts at grant
_ ,>f wav-->! « 'fun-'o : , Hrct on the chr--ri_,'i scrubber which
• • -•• -••• !,: 41- .M.^tiC'^i '"", DM* proc'-irnmenl
mt at this S3--i' ;.• - .. ^..u-, ;-•: f- ".i !;/„ sore cf t'iis f-'ork may be
done «_•-• >. •
™ The r>(5,.'• t-si-- is a ?.im> i-.- - ie.fi wMc1- : *.f- i-o >tarted at any
• reasonable time, If time permits, the end bc,\ covers should be
started eariy, because of thnir relation to connections,,
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Other appropriate time requirements are added to table 5
from table 2, The on-site time for the various Items is shown.
All ductwork and piping is avaiKl-le shortly before scrubber
arrival and sonic :" t'vis v/oulc , JDUUV ; .;• on rite and installed
even e^ ' ;
exst of n
ThUS, O'u: « ?c.
wil! br th-' f
in tabi column 3
'; • •<.-!• sin<; columns
;,<• the chlor-alkalie
• >us to table 4.
1 ••*, ;~ "-pducpd somevhat,
• • • i.hc conservative
otal waiver" time for lt;f
• '.'^: :is-.- o* cr Hlcal
•-• ,-•> ! *i ,* ! of the
•"•.,'ui • •.'r.-.r'f, The time
• -j^Hient preaecessor of
I
17
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TABLE 6. TOTAL WAIVER TIME FOR CHLOR-AlML IF PLANT
Procurement 145 days
Delivery JB£
On site tine ~-'1r-
Install at ion
Startup
Source sampling and analysis
Final report
Total v/aiver t i;\e
18
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each task is determined. In general, this will lead to two
or more parallel lines of tasks, or chains of milestones or events,
In general, also, the time required to perform each of these
lines of tasks will differ. The longest time path will be the
allowable waiver time, to be modified as shown in table 4. This
critical path technique is well known and is explained in
numerous reference works.
ravi..'or.m T.r,:.I Protection Agency
R-" ] -. V,_ Jr.brery
rc> i >... .-h r>.;sr-bo'rn Street
Cl—„, i/>D Illinois 6060«f
19
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