Unitad States
Environmental Protection
Agency
Office of Air Quality
Planning and Standards
Reeearch Triangle Park NC 27711
EPA-463/B-94-O38
May 1994
Air
HAP-PRO MODEL USER'S MANUAL
Version 1 .2
control
technology center
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'JO
I
HAP-PRO
USER'S MANUAL
Version 1.2
By
Pacific Environmental Services, Inc.
5001 South Miami Boulevard
Research Triangle Park, NC 27709
EPA Contract 68-D1-0116
Work Assignments 11-1 and 11-11
EPA 453/B-94-038
Joseph Steigerwald
Office of Air Quality Planning and Standards
Region 5, >. ic
77 West Jackw
(Chicago, it
Prepared for.
EPA Control Technology Center
Research Triangle Park, NC 27711
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PREFACE
TRADEMARKS
FoxPro is trademark of Fox Software, Inc., Perrysburg, OH.
dBase III Plus and dBase IV are trademarks of Ashton-Tate, Inc., Culver City, CA.
MS-DOS is a trademark of Microsoft Corporation, Bellevue, WA.
PURPOSE
The primary purpose of the Hazardous Air Pollutant Program (HAP-PRO) is to assist permit engineers
in reviewing applications for control of air toxics by calculating the capital and annual costs for up to six
different volatile organic compound (VOC) and three particulate control devices, including selected
engineering parameters. Calculations used by the program mirror those presented in the EPA Handbook,
Control Technologies for Hazardous Air Toxics (June 1991)(EPA-625/6-91/014). A secondary purpose of HAP-
PRO is to generate reports that list all facilities containing 1) a specified pollutant in their emission stream(s)
or 2) a specified type of emission stream (e.g., organic or inorganic vapors and particulates).
Version 1.2 includes the addition of an expert review system for the design of thermal incinerators,
catalytic incinerators, and carbon adsorber systems. The program will review the design results generated,
make recommendations for changes, and allow for design sensitivities to be easily evaluated.
TECHNICAL NOTE
HAP-PRO was developed using FoxPro version 2.0, a Relational Database Management System developed
by Fox Software of Perrysburg, OH. The installation program was developed using Install 2.3 from Knowledge
Dynamics Corporation of Canyon Lake, TX.
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TABLE OF CONTENTS
Page
PREFACE ii
FIGURES iv
CHAPTER 1: INTRODUCTION
Hardware Requirements 1-1
System Files 1-2
Database Files 1-2
CHAPTER 2: SYSTEM OVERVIEW
Logging On 2-1
Main Menu 2-1
Data Screens 2-3
Commands 2-5
System Help 2-6
System Maintenance 2-7
Expert Review System 2-8
Calculating Results 2-12
CHAPTERS: DATA ENTRY TUTORIAL
Adding Records 3-1
CHAPTER 4: REPORTS
Generating a Report 4-1
Report B - List Sources by Stream Type 4-2
Report C - List Sources by Pollutants 4-5
APPENDIX A
Data Dictionary A-l
Update Stamp A-l
Facility Data A-l
Thermal Incinerator A-2
Catalytic Incinerator A-4
Flare A-6
Carbon Adsorber A-8
Packed Column Scrubber (Stripper) A-10
Condenser A-13
Fabric Filters A-15
Venturi Scrubber A-17
ESP (Electrostatic Precipitator) A-19
APPENDIX B
Costing Methodology 8-1
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FIGURES
Figure No. Title
1 Welcome screen 2-2
2 Main menu 2-2
3 Source data screens 2-4
4 Plant notes 2-4
5 Help screen 2-6
6 Typical Carbon Adsorber Vessel Dimensions 2-9
7 Thermal Incinerator Operating Ranges 2-10
8 Catalytic Incinerator Operating Ranges 2-11
iV
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CHAPTER 1
INTRODUCTION
Installation of HAP-PRO is accomplished by inserting the distribution disk into the disk drive
of your computer and typing X:install, where X is the drive letter of your disk drive, for most users
this will be Drive A. At this point, the opening screen illustrated below will appear. Press any key
to continue onto the next screen and follow the instructions. To accept the default installation
parameters, continue to press ENTER until installation is complete.
With the release of Version 1.2, the user has the option of either 1) installing HAP-PRO for
the first time, or 2) updating a previously installed version of HAP-PRO. Separate disks are provided
depending on the installation option preferred. For first time installations, insert disk 1, type
INSTALL, and follow the instructions displayed. For those users who wish to retain previously
entered data, insert disk 2 and type INSTALL. The new version of HAP-PRO will be installed with
conversion of existing files. Any new input parameters added by the new version will initialize at
their default values. Consult Appendix A to review the new parameters.
INSTALL HAP-PRO
Developed for:
U.S. EPA
Control Technology Center
Research Triangle Park, NC 27711
Developed by:
Pacific Environmental Services, Inc.
P. 0. Box 12077
Research Triangle Park, NC 27709
I Press any key to continue ... I
HARDWARE REQUIREMENTS
~ IBM PC/XT/AT or compatible
~ 515K minimum free RAM
- minimum of 3 megabytes of free hard disk storage space for installation
- Monochrome or CGA/EGA/VGA color monitor
- MS-DOS version 3.1 or greater
- Hard disk required
1-1
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SYSTEM FILES
File Name Purpose
HAP-PRO.EXE Compiled Program Code
FOXPRO.ESO FoxPro Runtime Module
FOXPRO.ESL FoxPro Runtime Module
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DATABASE FILES
File Name Purpose
CONTROL.DBF Data File for ALL CONTROL TYPES
HAP.DBF Data File for HAPS
MEMO.DBF Temporary Work File for PLANT NOTES
MEMO.FPT Temporary Work File for PLANT NOTES
PLANT.DBF Data File for FACILITY
PLANT.FPT Memo File for PLANT NOTES
STREAM.DBF Data File for STREAM PARAMETERS
1 ^
1-0
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CHAPTER 2
SYSTEM OVERVIEW
LOGGING ON
The Welcome Screen is the first screen that appears to the user after the initial logon. This
screen informs the reader as to the program's purpose and where help can be obtained if you have
difficulty in using this program (see Figure 3). Use the cursor and PgUp/PgDn keys to read the entire
screen. Pressing ENTER will allow you to bypass or exit this menu. Immediately following this
screen users are required to input their initials. This information is used to stamp any records that
are modified.
MAIN MENU
The Main Menu appears immediately after the Welcome Screen. It provides access to the data
input screens, as well as the report and database maintenance functions (see Figure 4). Choose a
selection by entering either its corresponding letter (e.g. A, B, C) or by highlighting the desired
selection with the up and down cursor movement keys and pressing ENTER. The message line at
the bottom of the screen briefly explains what each selection does. For example, the corresponding
message for Selection A is Use this selection to Add, Edit, Calculate Results, etc. If a selection has
been made by mistake, press the ESC (escape) key to return to the Main Menu. The purpose of
each selection on the Main Menu is briefly described below:
Selection
ENTER/VIEWDATA
LIST SOURCES BY
STREAM TYPE
LIST SOURCES BY
POLLUTANT
REBUILD ALL INDEXES
REMOVE RECORDS
MARKED FOR DELETION
QUIT
Purpose
Provides access to data about each permit.
Generates a report listing all permits that have a specified
stream type (organic or inorganic vapors andparticulates)
Generates a report listing all permits that have a
specified pollutant (ammonia, benzene, toluene, etc.)
Rebuilds all indexes from scratch.
Permanently removes all records marked for deletion.
Quits this system.
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FIGURE 1. Welcome Screen
WELCOME [Read Only]
HAP-PRO
Version 1.2
Joseph Steigerwald
Control Technology Center
U.S. Environmental Protection Agency
Developed by
PES Systems Development Group
PO Box 12077
Research Triangle Park, NC 27709
(919) 941-0333
The primary purpose of this program is to assist permit engineers in the
review of applications for control of air toxics by calculating capital
and yearly operating costs for a specified emissions control device.
Calculations used by this program mirror those presented in the EPA
Handbook, Control Technologies for Hazardous Air Pollutants (June 1991),
Use T I PgUp PgDn to Move Cursor or ENTER to Continue
FIGURE 2. Main Screen
HAP-PRO Version 1.2
::*;.'•$ '.% lift liiirvfi-feB-: (JAT&
B LIST SOURCES BY STREAM TYPE
C LIST SOURCES BY POLLUTANT
D REBUILD ALL INDEXES
E REMOVE RECORDS MARKED FOR DELETION
f QUIT
Use T and I to move cursor -- Press ENTER to Make Selection
Use this selection to ADD, EDIT, CALCULATE results, etc.
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DATA SCREENS
The source data screens (see Figure 5) are accessed through selection A on the Main Menu. The permit
records are sorted in alphabetical order by name of the facility and are organized into five groups. Each group
is described and listed below.
Group Description
Facility Name, address, and principal activity of the facility, as well
as the reviewer's name and the number of emission streams.
Emission Stream Stream type, flow rate, heat content, etc. of the specified emission
stream, e.g. stream no. 1. A multiple number of streams can be
assigned to each facility.
Control Device Control device assigned to an emission stream. Details design and
cost parameters. Onfy one control device can be assigned to any
one emission stream.
Hazardous Air Pollutants or HAPs in a given emission stream, including concentration
Pollutants and other parameters. Multiple pollutants may be assigned to any
stream.
Plant Notes Miscellaneous notes about a facility or permit (see Figure 6).
In order to view or edit the parameters associated with each group, the user must either select the appropriate
group with the Edit command or use the Calc command to view or print the parameters from each group that
are associated with a specified emission stream, assuming that all data needed to perform the calculations have
been entered.
The data that comprise the emission stream, control device, and HAPs can be thought of as three separate
tables, which are organized in a like manner consisting of three to four columns. Each column is listed and
described below. Chapter 3 provides further detail on data entry.
Column Function
Parameter Name Identifies the parameter displayed. Unit of measure is enclosed by
parentheses.
Applicant Displays the value input by the user. Initially defaults to the value
recorded in the third column (if any). The Applicant values are used
to calculate capital and operating costs.
Default Displays the default value for the given parameter, if any. This value cannot
be edited.
Verified Records whether the user is confident that the applicant value is
correct. May also be used to note whether the figures have been
double-checked.
2-3
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FIGURE 3. Source Data Screens
Last Updated by GMP on 06/15/93
F5 * Plant Notes
Company: ABC Chemical
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919>999-1919
Permit Date: 10/01/90
Reviewer: Pagett
Streams: 2
Ff
ISSION STREAM-
|Stream Deleted? Stream Type
1 N ORGANIC VAPOR
2 N ORGANIC VAPOR
UNDEFINED
UNDEFINED
-CONTROL DEVICE
Deleted? Control Device
N THERMAL INCINERATOR
N CARBON ADSORBER
HA7APnrU !
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COMMANDS
At the bottom of the data screen is the command line (See Figure 5). Any command can be
executed by highlighting the desired command (using either the cursor or the mouse) and pressing
ENTER or by entering the first letter of the command. If an incorrect selection is made, press ESC
(escape) to return the cursor to the command line. The Find command is highlighted by default. The
purpose of each command briefly described below.
Command Purpose
Find Searches for a facility by its name. Once the scroll box is displayed, use the arrow
keys, PgUp, and PgDn to move to the desired record or enter the first character of
the facility. To move to the facility currently highlighted press ENTER or press
ESC to abort.
Edit Changes field attributes of previously entered data; the user must first specify which
data group is to be edited (e.g. Facility, Stream, Control Device, or HAPs). Press F1 to
obtain help on data entry or to access lookup tables. To edit/view the contents of the
note field, however, press function key F5; hence, the Edit command is irrelevant for
plant notes.
Add Creates a new record not previously entered into the system.
Delete Marks the currently displayed record for deletion, including the note field.
Records are not permanently deleted until the database is packed, an option on the
Main Menu. Until then, these records can be undeleted using the Undelete
command. Records marked for deletion display the flashing message "This Record
is Marked for Deletion".
Undelete Undeletes the currently displayed record, including plant notes.
Next Skips to the next record in the database.
Last Skips to the previous record in the database.
Calc Calculates for both capital and operating costs for the selected emission
stream. Input parameters are optionally included.
Return Exits to the Main Menu.
2o
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SYSTEM HELP
Help is available for many of the data fields through the use of pop-up lookup tables or text-based
notes. For the lookup tables, simply page up or down to find the desired selection and then press
ENTER. If no selections are desired, press ESC. Several examples of lookup tables are found in
Chapter 3. For textual help, select the field to be edited and press F1. If help is not available for a
particular field, the system will respond that no help is available. Figure 7 below illustrates one example
of textual help.
FIGURE 5. Help Screen
Last Updated by GMP on 06/15/93
F5 = Plant Notes
Company: ABC Chemical
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)5)99-1919
Permit Date: 10/01/90
Reviewer: Pagetl:
Streams: 2
I- STREAM Parameters Applicant Verified —
r; MAXIMUM FLOW RATE (SCFM) -- Press ESC to exit or T and I to scroll text—
Maximum Flow Rate (scfm)
The value to be input is the maximum value of the emission stream flowrate
in standard cubic feet per minute (scfm). If the emission stream happens
to be in actual cubic feet per minute (acfm), the following formula can be
used to convert acfm to scfm:
Qe = Qe,a [537/Te + 460]
Where: Qe = Maximum emission stream flowrate, scfm.
Qe,a = Maximum emission stream flowrate, acfm.
Te = Temperature of emission stream, "F.
Example: Qe,a = 20,000 acfm.
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SYSTEM MAINTENANCE
Selections D and E on the Main Menu are used to maintain the database by 1) rebuilding all
indexes from scratch, except for the conditional indexes associated with each report, and 2) purging
the database of all records that have been marked for deletion. A third important database maintenance
function is not built into this system at the present time - system backups. It is therefore
recommended that the DOS backup utility or some other utility be used to periodically back up all files,
or at least the data files (*.dbf, *.fpt). If the DOS backup utility is used, type in the following command
at the DOS prompt, assuming that this system is installed on drive C and drive A is where you wish
to backup the data. Also be sure that the system path permits access to the backup command when
this command is issued.
To backup, use the following command.
backup c:\fiap-prol *. * a:
To restore the data, use the following command.
restore a: c:\hap-pro\ *. *
If HAP-PRO is installed on some other drive or subdirectory, be sure to replace c:\hap-pro as
appropriate.
2-7
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EXPERT REVIEW SYSTEM
Version 1.2 includes the addition of an expert review system to evaluate the results of carbon
adsorber designs as well as thermal and catalytic incinerators. HAP-PRO will review the design results
calculated for each of these systems and provide recommendations for changes so that the design
results fall within reasonable boundaries. A spreadsheet-like window is made available to the user so
that different design scenarios can be evaluated interactively. An example calculation utilizing the new
expert review system for a carbon adsorber design is depicted in the CALCULATING RESULTS section
beginning on page 2-12. The following three sub-sections describe the parameters that each control
system evaluates to confirm that a reasonably designed system has been obtained.
Carbon Adsorber
For carbon adsorbers, the program compares the calculated vessel dimensions with those found
in Figure 6. If the calculated results do not fall within these boundaries, HAP-PRO recommends that
one or a combination of program inputs be changed. If the final design is reasonable, HAP-PRO will
make no recommendations for design changes. The recommendations for changes to the design
revolve around three key parameters: the number of adsorbing beds, the bed velocity, and the carbon-
to-vessel ratio. The effects of changes to these three parameters can be evaluated interactively on the
review screen to quickly develop the best design. HAP-PRO will also now perform calculations and
evaluate designs for both vertical and horizontal vessels.
Thermal Incinerator
For thermal incinerators, Figure 7 depicts the relationship that HAP-PRO seeks to obtain for the
destruction efficiency, residence time, and combustion temperature. If these three parameters fall
within the boundaries set by Figure 7, HAP-PRO assumes that the design is reasonable. The family of
curves shown are not for any particular pollutant, but are used by the program to place
"reasonableness" borders on the three variables (destruction efficiency, combustion temperature, and
residence time). Ideally, the user will have a curve such as the one in Figure 7 for the pollutant being
controlled to confirm that the design values selected are consistent with thermal incinerator laboratory
test data.
Catalytic Incinerator
For catalytic incinerators. Figure 8 depicts the relationship that HAP-PRO seeks to obtain for
the destruction efficiency and oxidation temperature. As with the thermal incinerator relationship, the
curve shown is not for any particular pollutant, but is used by the program to place "reasonableness"
borders on the two design variables, destruction efficiency and oxidation temperature. Since there are
many catalysts that might be effective in destroying a particular pollutant or combination of pollutants,
an accurate design should evaluate several catalysts. Catalyst-specific lab data is therefore needed to
determine the destruction efficiency and oxidation temperature requirements for each catalyst-pollutant
combination. HAP-PRO uses the curve in Figure 8 as a minimum requirement in the absence of
pollutant and catalyst-specific data.
2-8
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Height <- 30 feet
Vertical
Adsorber
FIGURE 6. Typical Carbon Adsorber Vessel Dimensions
2-9
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100
lucoid
10
f
*
o
E
K
5
O
20
INCREASING RESIDENCE TIME
too
1000
1201 1400
TEMPERATURE, °F
1680
1800
2000
FIGURE 7. Thermal Incinerator Operating Ranges
2-10
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in
20
400
601
TEWEflATUJJE/F
100
1000
1200
FIGURE 8. Catalytic Incinerator Operating Ranges
2-11
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CALCULATING RESULTS
HAP-PRO provides the user with calculated values of important engineering parameters for
each evaluated control system. The calculated values presented for each control device correspond
to those values calculated in the revised HAP manual which are considered necessary to perform a
permit review. The calculated values are not meant to be definitive, rather they are to be used as a
"ball park" reference to which the applicant's design is compared.
Design results are calculated by executing the steps outlined in the next 9 pages. The
example is the design of a carbon adsorber system, which is one of three air pollution control
systems for which HAP-PRO provides "expert" comments on the design. Expert review is also
available for thermal and catalytic incinerator designs. The expert system will review the design
results generated, make recommendations for changes, and allow for design sensitivities to be
evaluated in a spreadsheet-like environment. Although the remaining six control system design
routines (flare, packed column scrubber, condenser, fabric filters, venturi scrubber, and ESP) do not
provide expert review or allow for interactive design changes at the present time, plans are to create
this option for all systems that HAP-PRO is designed to evaluate.
The following depicts the steps required to calculate results for the three systems that utilize
HAP-PRO's expert analysis. Control device design calculations for the six systems where HAP-PRO
does not provide expert analysis are executed by following steps 1 through 7, then steps 13
through 18. Steps 8 through 12 are applicable only for those systems that have expert review
capabilities.
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/. Select ENTER/VIEW DA TA off of the Main Menu.
HAP-PRO Version 1.2
: A mj&wm win. -
B LIST SOURCES BY STREAM TYPE
C LIST SOURCES BY POLLUTANT
D REBUILD ALL INDEXES
E REMOVE RECORDS MARKED FOR DELETION
F EXIT TO DOS
Use T and I to move cursor -- Press ENTER to Make Selection
2 Select the Calc command from the menu at the bottom of the screen.
Last Updated by GMP on 06/15/93
F5 = Plant Notes
-FACILITY-
Company: ABC Chemical
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Pagett
Streams: 2
EMISSION STREAM-
Stream Deleted? Stream Type
1 N ORGANIC VAPOR
2 N ORGANIC VAPOR
UNDEFINED
UNDEFINED
-CONTROL DEVICE
Deleted? Control Device
N THERMAL INCINERATOR
N CARBON ADSORBER
UNDEFINED
UNDEFINED
Stream Deleted? Pollutant
1 N TOLUENE
1 N BEN2ENE
2 N TOLUENE
2 N BENZENE
UNDEFINED
Cone (pptnv or %)
1000.0
500.0
1000.0
500.0
Calculates Cost for a Specified Stream of this Plant
FIND EDIT ADO DELETE UNDELETE NEXT LAST CALC RETURN
2-13
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3. Select the stream for which the calculations will be performed.
Last Updated by GMP on 06/15/93
F5 > Plant Notes
-FACILITY-
Company: ABC Chemical
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Pagett
Streams: 2
Stream Deleted? Stream Type
1 N ORGANIC VAPOR
* * -mtttw*
Deleted? Control Device
N THERMAL INCINERATOR
'*' *ttftftgtttt«ttl*f
Stream Deleted? Pollutant
1 N TOLUENE
1
2
2
N
N
N
BENZENE
TOLUENE
BENZENE
UNDEFINED
Cone (ppmv or X)
1000.0
500.0
1000.0
500.0
Select Stream for CALCULATION
ESC * Exit ENTER = Select
4. Select the pollutant for which the calculations will be performed. (If only one pollutant has been input, this
screen will not appear.)
Last Updated by GMP on 06/15/93
F5 = Plant Notes
-FACILITY-
Company: ABC Chemical
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)5*99-1919
10/01/90
Permit Date:
Reviewer:
Streams:
Pagett
2
EMISSION STREAM-
Stream Deleted? Stream Type
-CONTROL DEVICE
Deleted? Control Device
1
ORGANIC VAPOR
CARBON ADSORBER
I HAZAR
Stream D
1
1
SOO'.'O'ppmv'"-"BENZENE
(ppmv or X)
0
BENZENE
UNDEFINED
UNDEFINED
UNDEFINED
500.0
Select HAP for Analysis
ESC = Exit ENTER = Select
2-14
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5. As the results are being calculated, 'Calculating" will be displayed.
Last Updated by GMP on 06/15/93
-FACILITY
F5 = Plant Notes
Company: ABC Chemical
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John
Telephone: (919
Calculating
Permit Date: 10/01/90
Reviewer: Pagett
Streams: 2
EMISSION
Stream Deleted? Stream Type
-CONTROL
Deleted? Control Device
1
ORGANIC VAPOR
CARBON ADSORBER
HAZARDOUS AIR POLLUTANTS-
Stream Deleted? Pollutant
1 N TOLUENE
1 N BENZENE
UNDEFINED
UNDEFINED
UNDEFINED
Cone (ppmv or X)
1000.0
500.0
ESC = Exit ENTER = Select
6, Once complete, the results will be displayed in the report box illustrated below. Use the arrow keys
to scroll back and forth through the document.
Last Updated by GMP on 06/15/93
• F AC ILIT Y
| Company: ABC Chemical
F5 = Plant Notes
Plant Contact: John Jones
C Please Review Calculated Results for Accuracy ]
HAP-PRO Version 1.2
Date of Print: 06/15/93
Note: Parameters marked with a * are not used in calculations; all other
parameters must be input to perform calculations accurately.
PLANT DATA
Plant ID: 000024
Company: ABC Chemical
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
STREAM TYPE -- ORGANIC VAPOR
DEVICE TYPE -- CARBON ADSORBER
Plant Contact: John Jones
Telephone: (919)999-1919
Agency Contact: John Jones
Permit Date: 10/01/90
Reviewer: Pagett
Streams: 002
« Print » < Review > < Help > < Exit >
2-15
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7. The output includes intermediate and calculated results as well as the results of the expert review system.
After reviewing the output, push either *P* to PRINT the results, "R' to proceed to the REVIEW section, "ff to
get HELP, or "£" to EXIT the calculation routine. [NOTE: For the six control systems that do not currently
allow expert review (the "R* option), proceed to Step 13.]
Last Updated by CMP on 06/15/93
-FACILITY-
F5 - Plant Notes
r
Company: ABC Chemical Plant Contact: John Jones
•[ Please Review Calculated Results for Accuracy ]
EXPERT REVIEW
The Length and diameter calculated were 43.6 feet and 15.9 feet,
respectively. The pressure drop calculated was 13.1 inches of water.
Typical Horizontal carbon adsorber dimensions are lengths less than 60 feet
and diameters between 4 and 12 feet. Pressure drop should be no more than
15 inches.
HAP-PRO recommends that one of the following parameters be changed and
the design rerun to generate more reasonable results:
Input Parameter
Current Recommen-
Value dation
Acceptable Range
No. of Adsorbing Beds 6 5 1-10
Bed Velocity (ft/min) 60.00000 44 < 150 ft/s
Carbon-to-Vessel Ratio .4000000 0.4 0.25 - 0.4 ft3/ft3
« Print » < Review >
Help
Exit
8. If'R" is selected, the REVIEW screen appears. This spreadsheet-like screen allows the user to perform
unlimited sensitivities to develop the most effective carbon adsorber design. Any of the four input parameters at
the top of the screen may be changed and the design recalculated. The design type can be changed by pressing
the space bar.
Las»l
— 1 UPI IT DAD AMPTFPQ
r™" 1 NrU 1 r An/\nc 1 CKd
1 Design Type
— No. of Adsorbing Beds
EX Bed Velocity (ft/min)
Carbon-to-Vessel Ratio
re CALCULATED RESULTS
Ty HAP Density (Ib/ft3)
an Inlet HAP Loading (Ib/hr)
15 Adsorptive Capacity
Carbon Requirement (Ibs)
Vessel Diameter (ft)
th Vessel Length (ft)
Vessel Surface Area (ft2)
Steam Requirement (Ibs/min)
In Pressure Drop (in of water)
System Fan Power (hp)
No Bed Gas Flow Rate (scfm)
Be Total Capital Costs ($)
Ca Direct Annual Costs ($)
Total Annual Costs ($}
Pi IPPWl^ Df*O\/ 1 DPOW 9
l«UI icill r 1 CV 1 r 1 CV £
HORI2TL
6
60.000
0.400
0.235
3,525.000
0.067
732,715.9
15.9
43.5
2,579.4
1,794.4
13.0
880.4
697,824.6
4,496,900
4,889,600
5,547,500
« Recalc » < Save > < Cancel > < Help >
e»
2-16
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9, Recalculations are performed by editing the input field (or fields) desired and pressing *R" for RECALC, or
by pressing « RECALC » with the mouse or pressing CNTL-ENTER. The new results are instantly
displayed. HAP-PRO saves up to two iterations.
LBSl
r- INPUT PARAMETERS
1 Design Type
— No. of Adsorbing Beds
Bed Velocity (ft/min)
Carbon- to- Vessel Ratio
EX CALCULATED RESULTS
HAP Density (Ib/ft3)
Inlet HAP Loading (Ib/hr)
re Absorptive Capacity
Ty Carbon Requirement (Ibs)
an Vessel Diameter (ft)
15 Vessel Length (ft)
Vessel Surface Area (ft2)
Steam Requirement (Ibs/min)
th Pressure Drop (in of water)
System Fan Power (hp)
Bed Gas Flow Rate (scfm)
In Total Capital Costs ($)
Direct Annual Costs ($)
No Total Annual Costs ($)
Current Prev 1 Prev 2
HORIZTL
5
60.000
0.400
0.235
3,525.000
0.067
732.715.9
15.9
43.5
2,579.4
1,794.4
13.0
880.4
697,824.6
4,496,900
4,889,600
5,547,500
« Recalc » < Save > < Cancel > < Help >
C»
10. Once the sensitivities are complete, push < SAVE > or press "S". The program will then prompt the user
for the input data set to save.
Las
r
HA
No
PL
INPUT PARAMETERS
Design Type
No. of Adsorbing Beds
Bed Velocity (ft/min)
Carbon-to-Vessel Ratio
CALCULATED RESULTS
HAP Density (Ib/ft3)
Inlet HAP Loading (Ib/hr)
Adsorptive Capacity
Carbon Requirement (Ib
Vessel Diameter (ft)
Vessel Length (ft)
Vessel Surface Area (f
Steam Requirement (Ibs
Current
HORIZTL
6
50.000
0.400
0.235
3,525.000
0.067
Previous Set 1
Previous Set 2
Pressure Drop (in of water) 8.8
System Fan Power (hp) 616.0
Bed Gas Flow Rate (scfm) 697,824.6
Total Capital Costs ($) 4,651,900
Direct Annual Costs ($) 4,742,000
Total Annual Costs ($) 5,431,200
Prev 1
HORIZTL
5
50.000
0.400
0.235
3,525.000
0.067
628,042.2
11.0
90.3
3,332.3
1.495.3
7.3
523.7
697,824.6
4,167,800
3,960,300
4,589,200
Prev 2
HORIZTL
5
60.000
0.400
0.235
3,525.000
0.067
628,042.2
13.2
62.7
2,893.6
1,495.3
10.9
744.0
697,824.6
3,987,500
4,083,200
4,675,600
« Recalc » *'•;' Save'-;'* < Cancel > < Help >
es
2-17
-------
11. As the new input is saved, "Saving Data" will be displayed.
LOS
r
HA
No
PL
ST
ST
I UP! IT PARAMETERS Current Prm/ 1
i Hru 1 r nimnc i cno bui i cin r i w I
Design Type HORIZTL HORIZTL
kin of Arbtnrhina Rarla A 4
HO • VI nv!9 VI U 1 [Iff DC\J9 O 7
Bed Velocity (ft/min) 50.000 50.000
Carbon-to-Vessel Ratio 0.400 0.400
CALCULATED RESULTS
HAP Density (Ib/ft3) 0.235 0.235
Inlet HAP Loading (Ib/hr) 3,525.000 3,525.000
Adsorptive Capacity 0.067 0.067
Carbon Requirement (Ibs) 732,715.9 628,042.2
Vessel Diameter (ft) 13.2 11.0
Vessel Length (ft) 62.7 90.3
Vessel Surface Area (ft2) 2,893.6 3,332.3
Steam Requirement (Ibs/min) 1,794.4 1,495.3
Pressure Drop (in of water) 8.8 7.3
System Fan Power (hp) 616.0 523.7
Bed Gas Flow Rate (scfm) 697,824.6 697,824.6
Total Capital Costs ($) 4,651,900 4,167,800
Direct Annual Costs ($) 4,742,000 3,960,300
Total Annual Costs ($) 5,431,200 4,589,200
« Recalc » £$$iinii?sf < Cancel > < Help
Saving Data
60.000
0.400
0.235
3,525.000
0.067
628,042.2
13.2
62.7
2,893.6
1,495.3
10.9
744.0
697,824.6
3,987,500
4,083,200
4,675,600
i >
es
12. After saving, the final output is displayed as in Step 6. Additional sensitivities may be run at this point or
the output may simply be sent to the printer.
Last Updated by GMP on 06/15/93
-FACILITY-
F5 = Plant Notes
r
Company: ABC Chemical Plant Contact: John Jones
[ Please Review Calculated Results for Accuracy :i
HAP-PRO Version 1.2
Date of Print: 06/15/93
Note: Parameters marked with a * are not used in calculations; all other
parameters must be input to perform calculations accurately.
PLANT DATA
Plant ID: 000024
Company: ABC Chemical
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
STREAM TYPE -- ORGANIC VAPOR
STREAM RELATED PARAMETERS
Plant Contact: John Jones
Telephone: (919)999-1919
Agency Contact: John Jones
Permit Date: 10/01/90
Reviewer: Pagett
Streams: 002
« Print » < Review >
Help
Exit
2-18
-------
13. Files may be printed from either the review screen or the initial results screen. For printing options, select
« PRINT » or *P*.
Last Updated by GHP on 06/15/93
-FACI LITY-
F5 * Plant Notes
Company: ABC Chemical Plant Contact: John Jones
-[ Please Review Calculated Results for Accuracy ]
INTERMEDIATE RESULTS
Dilution Air Requirements (scfm):
Temp of Stream after Heat Exchange CF):
Natural Gas Flow Rate (scfm):
Combustion Chamber Volume (ft3):
Flue Gas Flow Rate (scfm):
Electricity Requirement (Kwh/yr);
0
478.1000
76.99343
.0000000
15076.99
.0000000
Fuel Usage (ft3/yr): 27717634
CAPITAL COSTS
Site Preparation: 0
Building: 0
Purchased Equipment: 255,400
Direct Installation: 76,600
Total Direct Costs: 332,000
Total Indirect Costs: 79,200
« Print » < Review > < Help > < Exit >
14, If printing is selected, a menu pops up to prompt the user for the type of output desired (Le., ASCII file or hard
copy).
Last Updated by GMP on 06/15/93
. runt ?TV
F5 = Plant Notes
| Company: ABC Chemical Plant Contact: John Jones
-[ Please Review Calculated Res
HAP-PRO Version 1.2
Date of Print: 06/15/93
INTERMEDIATE RESULTS
Dilution Air Requirements (scfm):
Temp of Stream after Heat Exchange (*F):
Natural Gas Flow Rate (scfm):
Combustion Chamber Volume (ft3):
Flue Gas Flow Rate (scfm):
Electricity Requirement (Kwh/yr):
CAPITAL COSTS
Fuel Usage (ft3/yr):
0
478.1000
76.99343
.0000000
15076.99
.0000000
27717634
Site Preparation: 0
Pure
Dire
9n
u
: 'StS'Clg -WlV; t: 255,400
Printer n: 76,600
«? j»F£rif '. '•'% < Review > < Help > < Exit >
2-19
-------
15. For an ASCII file output, another menu requests the receiving drive name and the file name.
Last Updated by GHP on 06/15/93
FACILITY
F5 = Plant Notes
r
Company: ABC Chemical Plant Contact: John Jones
C Please Review Calculated Results for Accuracy ]-
HAP-PRO Version 1.2
INTERMEDIATE RESULTS
Dilution Ai
Temp of Stream aft
Natural
Combustion
Flue
Electricity
CAPITAL COSTS
Site Prepa
Date of Print: 06/15/93
A
B
C
D
Filename: FILEOUT.DOC
Building: 0
Purchased Equipment: 255,400
Direct Installation: 76,600
< Review > < Help > < Exit >
16. Once the ASCII file is input, push ENTER to execute. "Creating File..." will appear.
Last Updated by GMP on 06/15/93
FACILITY
F5 = Plant Notes
r
Company: ABC Chemical
PI
-C Please Review Calculated Res
Creating File C:\FILEOUT.DOC
HAP-PRO Version 1.2
INTERMEDIATE RESULTS
Dilution Air Requirements (scfm):
Temp of Stream after Heat Exchange (*F):
Natural Gas Flow Rate (scfm):
Combustion Chamber Volume (ft3):
Flue Gas Flow Rate (scfm):
Electricity Requirement (Kwh/yr):
Fuel Usage (ft3/yr):
CAPITAL COSTS
Site Preparation: 0
Building: 0
Purchased Equipment: 255,400
Direct Installation: 76,600
Date of Print: 06/15/93
0
478.1000
76.99343
.0000000
15076.99
.0000000
27717634
< Review > < Help > < Exit >
2-20
-------
17. For a hardcopy report, select "Printer*.
Last Updated by GMP on 06/15/93
FACILITY
F5 = Plant Notes
Company: ABC Chemical Plant Contact: John Jones
C Please Review Calculated Results for Accuracy ]
HAP-PRO Version 1.2
Date of Print: 06/15/93
Note: Parameters marked with a * are not used in calculations; all other
other parameters must be input to perform calculations accurately.
PLANT DATA
Plant ID: 00024
Company: ABC Chemical
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State
STREAM TYPE -
STREAM RELATE
09-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Pagett
Streams: 002
* Review > < Help > < Exit >
18. After pushing ENTER, a box will appear with the text "Printing.'
Last Updated by GMP on 06/15/93
-FACILITY-
F5 = Plant Notes
r
Company: ABC Chemical
Plant Contact: John Jo
-[ Please Review Calculated Results for Accuracy ]-
Printing
HAP-PRO Version 1.2
Date of Print: 06/15/93
Note: Parameters marked with a * are not used in calculations; all other
other parameters must be input to perform calculations accurately.
PLANT DATA
Plant ID: 00024
Company: ABC Chemical
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
STREAM TYPE -- ORGANIC VAPOR
STREAM RELATED PARAMETERS
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Pagett
Streams: 002
< Review >
Help
Exit
After printing the output, press Esc or "E" to exit from this screen. You will then be able to select another
stream for calculation or return to the Main Menu.
-------
CHAPTERS
DATA ENTRY TUTORIAL
This chapter consists of step-by-step instructions on how to enter a new record into the
system. In general, the same procedures can be used when editing a previously existing record.
ADDING RECORDS
7. Select ENTER/VIEWDATA from the Main Menu by pressing ENTER or by clicking on the horizontal
bar for users with a mouse.
HAP-PRO Version 1.2
- ^^i^MftMf^^^ DATA
:•:•:•: :•:• W- ••:-.-*lt \M\f. .¥ t*iW W\fft
B LIST SOURCES BY STREAM TYPE
C LIST SOURCES BY POLLUTANT
0 REBUILD ALL INDEXES
E REMOVE RECORDS MARKED FOR DELETION
F QUIT
Use t and I to move cursor -- Press ENTER to Make Selection
Use this selection to ADD, EDIT, CALCULATE results, etc.
Z Select ADD from the command line at the bottom of the screen.
Last Updated by GMP on 02/12/94
-FACILIT Y
F5 = Plant Notes
Company: Glaze Chemical Co.
Description: Chemical Mfg.
Street: 87 Octane Drive
City: Durham
State: NC Zip: 27707-
Plant Contact: John Doe
Telephone: (999)555-5024
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
EMISSION STREAM-
Stream Deleted? Stream Type
1 N ORGANIC VAPOR
-CONTROL DEVICE
Deleted? Control Device
N THERMAL INCINERATOR
, HAZARDOUS AIR POLLUTANTS-
Stream Deleted? Pollutant
1 N TOLUENE
UNDEFINED
UNDEFINED
UNDEFINED
UNDEFINED
Cone (ppmv or X)
73.0
Creates a new Plant Record
FIND EDIT AOB DELETE UNDELETE NEXT LAST CALC RETURN
2-1
-------
3. Select FACILITY if you wish to enter data about a new facility; otherwise select the group to which you wish
to add data.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: Glaze Chemical
Description: Chemical Mfg.
Street: 87 Octane Drive
City: Durham
State: NC Zip:
EMISSION STREAM
Stream Deleted? Stream
1 N ORGANIC 'i^S
2 N ORGANIC
3 N ORGANIC
4 N ORGANIC
Stream Deleted? Pollutant
1 N TOLUENE
UNDEFINED
UNDEFINED
UNDEFINED
UNDEFINED
Co. Plant Contact: John Doe
Telephone: (999)555-5024
Permit Date: 10/01/90
Reviewer: Moore
27707- Streams: 4
'"' "EMI ssi ON " STREAM
CONTROL DEVICE
HAP POLLUTANTS
Device
INCINERATOR
1C INCINERATOR
ADSORBER
Cone (ppmv or %)
73.0
Use this selection to ADD a new facility
4. At this point the cursor will be reposition itself to the first field in the Facility Group. Enter in the appropriate
data and press ENTER or the down cursor key to advance to the next field. Up to 99 streams can be assigned to
a facility, although this number is more likely to be no more than two or three. You will also notice that the data
for the other groups have now been blanked out.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ^ " '• •"•. •- ':
Description: = . : : • .. i
Street: . .. .. •: ...- :
City: ' . . ";" : .
State: : . Zip:
:•'.' • Plant Contact: : . ,.;
'•••; Telephone: (. . i> ~..r
Permit Date: /'./'•
Reviewer:
Streams: Q
EMISSION STREAM-
Stream Deleted? Stream Type
-CONTROL DEVICE
Deleted? Control Device
HAZARDOUS AIR POLLUTANTS-
Stream Deleted? Pollutant
Cone (ppmv or %)
ESC = ABORT F10 = EXIT
Enter Name of Facility
3-2
-------
5. To access the State pop-up displayed below, press Fl. Then press the first letter of the state you are seeking
and use the cursor keys to highlight the desired state. Press ENTER to accept a selection or press ESC to abort.
Users with a mouse may alternatively scroll through the states by clicking and holding down the mouse button on
the arrow indicators of the scroll box f* *). Selections are accepted with a double click. These procedures will
hold true for all scroll boxes.
Last Updated by GMP on 02/12/94
= Plant Notes
Company: ABC Chemical, Inc.
Description: CN«fltf«at flfg>
Street: Isaac ReHtOR AVe>
City: ftes«rrch Tn'frgte
State: ;..: Zip:
Plant Contact:
Telephone:
Permit Date:
Reviewer:
Streams:
EMISSION STREAM-
Stream Deleted? Stream
HAZARDOUS AIR POLLUT
Stream Deleted? Polluta
MONTANA
NEBRASKA
NEVADA
NEW HAMPSHIRE
NEW JERSEY
NEW MEXICO
NEW YORK
NORTH DAKOTA
OHIO
OKLAHOMA
Device
Cone (ppmv or %)
ESC
ABORT F10 = EXIT
Select State
6. Once ENTER has been pressed, the popup will disappear and the state code will be automatically written into
the field.
Last Updated by GMP on 02/12/94 F5 = Plant Notes
-FACILIT Y
Company: ABC. Cljjjsijtfcal, Inc.'
Description: ChemtcdlXfj: ' :
Street: Isaac;Newton Ave, .. : .
city: Research Triangle Park
State: feC Zip: : . *
Plant Contact: . .
Telephone: t';'..•')•'..-
Permit Date: •.'.;/ /
Reviewer:
Streams: .D
-EMISSION STREAM-
Stream Deleted? Stream Type
-CONTROL DEVICE
Deleted? Control Device
I HAZARDOUS AIR POLLUTANTS-
Stream Deleted? Pollutant
Cone (ppmv or
ESC = ABORT F10 = EXIT
Enter Name of Facility
o-o
-------
7. If you need to enter notes about this facility, you may do so at any time by pressing F5. The size of the note
field is limited onfy by the amount of free disk space.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
-PLANT NOTES -- Press Ctrl-W to Save or ESC to Abort-
Plant to cease CFC production in 1991.
8. Once data has been entered into each field, press F10 to exit. Accept the highlighted selection by pressing
ENTER.
Last Updated by GMP on 02/12/94
-FACILITY
F!i = Plant Notes
Company:
Description:
Street: Usetd Hewtoft
City: Research Triangle Park
State: m Zip: 2T7G9-
Plant Contact: John Joftes
Telephone:
Permit Date:
Reviewer: Moore
Streams: 2
EMISSION STREAM-
-CONTROL DEVICE-
Stream Deleted? Stream Type Deleted? Control Device
Select Disposition
i HAZARDOUS AIR P
Stream Deleted? Po
ABORT DATA ENTRY AND EXIT
RETURN FOR FURTHER EDITING
Cone (ppmv or %)
ESC = ABORT F10 = EXIT
Enter Name of Facility
3-4
-------
9. You must now specify the stream for which you are entering data. The default value is 1. If you enter a stream
number greater than the number specified in the streams field, you will be given an error message and will not be
allowed to proceed.
Last Updated by GMP on 02/12/94
-FACILITY-
F5 = Plant Notes
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC
Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
EMISSION STREAM-
Stream Deleted? Stream Type
-CONTROL DEVICE
Deleted? Control Device
HAZARDOUS AIR POLLUTANTS-
Stream Deleted? Pollutant
Cone (ppmv or %)
Enter Stream No.: t
10. Now specify one of the four types of emission streams. The type of stream you specify now will determine which
of the control types you have access to later. However, the control type can be changed if it is incorrectly specified
(see step 13).
Last Updated by GMP on 02/12/94
-FACILITY
F5 = Plant Notes
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
EMISSION STREAM-
Stream Deleted? Stream Type
-CONTROL DEVICE-
HAZARDOUS AIR P
Stream Deleted? Po
Deleted? Control Device
-Select STREAM Type
'ORGANIC VAPOR;
INORGANIC VAPOR
ORGANIC PARTICULATE
INORGANIC PARTICULATE
Cone (ppmv or
Use r and 1 to move cursor
ESC = Abort ENTER = Select
3-5
-------
11. Once ENTER has been pressed, the table below appears, consisting of the parameters associated with the
stream type specified, in this case, Organic Vapor. Users with color monitors will notice that this table differs in
color from rest of the screen. The data itself is arranged into three columns. The first column lists the parameter
name, the second column lists the applicant value, and the last column notes whether the value indicated by the
applicant column has been verified or checked. Default values are supplied for many of the applicant parameters.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Issac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
r- STREAM Parameters
«•
Emission Stream No.
Stream Type - ORGANIC VAPOR
Maximum Flow Rate (scfm)
Stream Temperature (deg F)
•- Moisture Content (%)
S Stream Pressure (mmHg)
Mean Particle Diameter (Ug)
Particulate Content (gr/scf)
S03 Concentration (ESPs only, ppmv)
Drift Velocity (ESPs only, ft/s)
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
Applicant Default Verified
1
1
0 N
77 77 N
20.0 20 N
0.0 N
760.0 760 N
0.000 N
0.000 N
0.000 N
0.000 ' N
%)
ESC = Abort ENTER = Edit Parameter F10 = Continue
Unavailable Selections Not Appropriate for Selected Stream Type
12. Every parameter except for the Emission Stream number, specified in step 9, can be edited by highlighting the
appropriate line and pressing ENTER. If you attempt to edit the first line, however, you will be given the error
message illustrated below.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company:
Description:
Street:
City:
State:
ABC Chemical, Inc. PI
Chemical Mfg.
Issac Newton Ave.
Research Triangle Park
NC Zip: 27709-
Th is
Press
Line
Any
Cannot
Key to
be Edited
Continue
r- STREAM Parameters
c-
Emission Stream No.
Stream Type - ORGANIC VAPOR
Maximum Flow Rate (scfm)
Stream Temperature (deg F)
— Oxygen Content (%)
r— Moisture Content (%)
S Stream Pressure (ntnHg)
Mean Particle Diameter (Ug)
Particulate Content (gr/scf)
S03 Concentration (ESPs only, ppmv)
Drift Velocity (ESPs only, ft/s)
Appl icant
1
1
0
77
20.0
0.0
760.0
0.000
0.000
0.000
0.000
Default
77
20
760
Verified •
N
N
N
N
N
N
M
X)
U
H •
Unavailable Selections Not Appropriate for Selected Stream Type
3-6
-------
13. If you have incorrectly specified the stream type, it may be changed by highlighting the second line and pressing
ENTER, which displays the edit box illustrated below. To change the emission stream, press the spacebar to cycle
through the four different stream types and press PgDn or ENTER to accept the new stream type. If no change
is desired, press ESC.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC chemical, Inc.
Description: Chemical Mfg.
Street: Jssac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
i- STREAM Parameters
Applicant Default Verified ,
Emission Stream No.
Stream Type
Maximum F
Stream Te
Oxygen Co
1
-Enter Parameter-
Stream Type - ORGANIC VAPOR
S
Stream Pr
Mean Part
Particula
S03 Conce
Drift VeU
(Press spacebar for selections)
ESC = Abort F1 = Help PgDn = Exit
scity (ESPs only, ft/s) 0.000 N
Unavailable Selections Not Appropriate for Selected Stream Type
14. To edit parameters other than the stream type, highlight the desired parameter and press ENTER, as you did
in step 13. This time, however, simply type in the value of the parameter to the greatest known degree of accuracy
or to the greatest level of accuracy the field permits. Be sure to express all values in the units specified. Use the
Verified field to record whether you are confident that applicant value is correct.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Issac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
S
s
STREAM Parameters Applicant Default Verified
Emission St
Stream Type
Maximum F
Stream Te
Oxygen Co
Moisture
Stream Pr
Mean Part
Particula
S03 Conce
Drift VeU
•earn No. 1
Maximum Flow Rate (scfm)
'Applicant Value: ;Q - •
Default:
Verified? (Y/N): N
ESC = Abort F1 = Help PgDn = Exit
)city (ESPs only, ft/s) 0.000 N
%)
Unavailable Selections Not Appropriate for Selected Stream Type
3-7
-------
75. If you are not sure what value to input, press Fl for help. The textual information will generally define the
parameter, state the formula used to derive it (if any), and give a citation to the revised edition of the EPA
Handbook, Control Technologies for Hazardous Air Pollutants. To scroll through a lengthy help note use the
cursor and PgUp/PgDn keys. To exit from the help file, press ESC.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
rnci LI i i
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
—
XIMUM FLOW RATE"(S'CFM)'":-""Press"ESC'to exit or T i to scroll"text——
Maximum Flow Rate (scfm)
The value to be input is the maximum value of the emission stream flowrate
in standard cubic feet per minute (scfm). If the emission stream happens
to be in actual cubic feet per minute (acfm), the following formula can be
used to convert acfm to scfm:
Qe = Qe.a [537/Te + 460]
Where: Qe = Maximum emission stream flowrate, scfm.
Qe,a = Maximum emission stream flowrate, acfm.
Te = Temperature of emission stream, "F.
Example: Qe,a = 20,000 acfm.
16. Qnce the data has been entered in the edit box, press PgDn or ENTER to return to the stream parameter table.
You will note that the Applicant and Verified columns now reflect the newly input values. Continue this process
until all of the data is input.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Issac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
r-. STREAM parameters . .••.
S'
Emission Stream No.
Stream Type - ORGANIC VAPOR
Maximum Flow Rate (scfra) . '
Stream Temperature (deg F)
— Oxygen Content (%)
S Stream Pressure (mmHg)
Mean Particle Diameter (Ug)
Particuiate Content (gr/scf)
S03 Concentration (ESPs only, ppm>
Drift Velocity CESPs only, ft/s)
i
Plant Contact:
Telephone:
Permit Date:
Reviewer:
Streams:
Applfc'aht D'e'flay
1
1
D :'
77 ' '
20.0
0 0
760.0 7
0.000
0.000
/) 0.000
0.000
John Jones
(919)999-1919
10/01/90
Moore
2
It ;VeHfVed ; 1
r 'ft ' ':
77 ' N '
60 N %)
M
N
N
ESC = Abort ENTER = Edit Parameter F10 = Continue
Unavailable Selections Not Aopropriate for Selected Stream Type
3-3
-------
17. To exit from the stream parameter table, press F10. You are now given an opportunity to save the data, abort
data entry, or return for further editing. If you choose to save the data, the system will automatically take you to
the next step, which is to input data about the control device.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
rm. inii
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Issac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
S
S
siKtAH parameters Applicant ueraun vennea
Emission Stream
Stream Type - OR
Maximum Flow R
Stream Tempera
Oxygen Content
Moisture Conte
Stream Pressur
Mean Particle C
Particutate Cor
S03 Concent rat
Drift Velocity
T?" " SAVE SfiREA^iCiATA'AH&i'EXiT " •" '".""
ABORT DATA ENTRY AND EXIT
RETURN FOR FURTHER EDITING
iameter (Ug) 0.000
itent (gr/scf) 0.000
on (ESPs only, ppmv) 0.000
(ESPs only, ft/s) 0.000
N
N
N
N
N
N
N
N
N
%)
Unavailable Selections Not Appropriate for Selected Stream Type
]8. You are now prompted to specify the control device. The list of control types from which you may choose is
determined by the emission stream type specified earlier, as not every control technology is appropriate for use with
each emission stream type. If you do not wish to input the control device data at this time, press ESC to return
to (he command line at the bottom of the screen.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC Chemical, Inc. Plant Contact: John Jones
Description: Chemical Mfg. Telephone: (919)999-1919
Street: Issac Newton Ave. Permit Date: 10/01/90
City: Research Triangle Park Reviewer: Moore
State: NC Zip: 27709- Streams: 2
| EMISSION STREAM
Stream Deleted? Stream
1 N ORGAN I
HAZARDOUS AIR POLLU
Stream Deleted? Pollut
UNDEFI
UNDEF!
IJNDFFI
THERMAL JKCtNERATQB •
CATALYTIC INCINERATOR
FLARE
CARBON ADSORBER
PACKED COLUMN SCRUBBER
CONDENSER
FABRIC FILTERS
VENTURI SCRUBBERS
ESP
I Device
NED
Cone (ppmv or %)
UNDEFINED
UNDEFINED
Unavailable selections are not are applicable for specified Stream Type
-------
19. The parameters for the control device are entered using the same methods as described for data entry into the
emission stream table (see steps 12-17). The data is organized into four columns under two different groups-
Design Related Parameters and Cost Related Parameters. Default values are provided for many of the parameters.
Last Updated by CMP on 02/12/94
FS = Plant Notes
Company: ABC Chemical, Inc. Plant Contact: John Jones
Description: Chemical Mfg. Telephone: (919)999-1919
Street: Isaac Newton Ave. Permit Date: 10/01/90
City: Research Triangle Park Reviewer: Moore
State: NC Zip: 27709- Streams: 2
frsi rameiwr? " for' -If W%Htf ' 1 SCi HiES'ATDH
bfeWCfi-J'tfpE"'-* ft«ERW::::iftCftiERATOR
bESIGN RELATED PARAMETERS
Destruction Efficiency (%)
Combustion Temp (°F)
Residence Time (sec)
Heat Exchanger Efficiency (%)
Reference Temp (°F)
Heat Cap. of Air at Comb. Temp (Btu/scf°F)
COST RELATED PARAMETERS
Applicant I
98.0
.0000000
.0000000
70.0
77.00000
.2650000
JefauU Verified — ,
98
70
77
0.265
N
N
N
N
N
N
*
ESC = Abort ENTER = Edit Parameter F10 = Exit
20. To edit a parameter, select the appropriate line with the scroll bar and press ENTER. The Device Type cannot
be edited at the present time. If an attempt is made to edit a line that cannot be edited, a warning will be given
to the user. In general, data should be entered to the greatest degree of accuracy known. Most design parameters
will permit the decimal point to float from -1 to -7; exceptions are percentages and those which require whole
numbers. Be sure to express all values in the units indicated.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
parameters for THERMAL INCINERATOR :' . ...Applicant default Verified —,
HFV/I PF TYPF c— 4--_ n. --.««.«. ~-
DESIGN RELATE
Destruction
Combustion
Residence T
Heat Exchan
Reference T
Heat Cap. o
Destruction Efficiency (%)
Applicant Value: 95.0
Default Value: 98
Verified? (Y/N): V
ESC = Abort F1 = Help PgDn = Exit
' N
N
N
N
N
N
COST RELATED PARAMETERS
3-10
-------
21. Press PgDn or ENTER to exit from the edit box and return to the device table. You will now notice that the
columns reflect your newfy entered values. Continue this process until data has been input for all of the Design
Related parameters.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
-FACILITY-
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
rar?fflet?r¥ T
-------
23. Once all of the data has been input, press F10 to exit and save the control device table to the disk.
Last Updated by CMP on 02/12/94
F5 = Plant Notes
im»iLi i i
Company: ABC Chemical, Inc. Plant Contact: John Jones
Description: Chemical Hfg. Telephone: (919)999-1919
Street: Issac Newton Ave. Permit Date: 10/01/90
City: Research Triangle Park Reviewer: Moore
State: NC Zip: 27709- Streams: 2
Device Input Parameters
COST RELATED PARAN
Site Preparation
Building Cost ($
Damper Cost ($)
Duct Cost ($/lin
Length of Duct (
Total Pressure D
Average Equipment
Fan/Motor Efficic
Interest Rate (X]
frlrrt
Applicant
Default
SAVE BEVICE £>*TA XN0 EXIT
ABORT DATA ENTRY AND EXIT
RETURN FOR FURTHER EDITING
Life (yr)
•ncy (%)
10
60
10
10
60
10
Verified — ,
N
N
N
N
N
N
N
N
N
X)
UNDEFINED
24. You are now prompted to input the stream number to which the HAPs will be linked. This value defaults at
1.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
-FACILITY-
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
EMISSION STREAM-
Stream Deleted? Stream Type
-CONTROL DEVICE
Deleted? Control Device
HAZARDOUS AIR POLLUTANTS-
Stream Deleted? Pollutant
Cone (ppmv or X)
Enter Stream No.: |.;
-------
25a. You are now ready to specify the method which will be used to input the pollutants in the designated stream,
Le. stream number 1. If you choose POLLUTANT LIST, the first option, the pollutants from which you will
choose are presented by one of two alphabetical lists, one for organic pollutants and another for inorganic
pollutants.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
-FACILITY-
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Isaac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
EMISSION STREAM-
-CONTROL DEVICE-
Stream Deleted? Stream Type Deleted? Control Device
efine Method of HAPS Selection
-HAZARDOUS AIR P
SiC"CAtEGORY
Stream Deleted? Pollutant
Cone (ppmv or
ESC = Exit Enter = Select
26a. Now select the pollutant(s) potentially present in this emission stream by pressing ENTER. The first letter
of each pollutant is hot-keyed, meaning that typing this letter will position the scroll bar on the first pollutant listed
for that letter. For example, typing "TO" will move the scroll bar to TOLUENE. You will notice that only the
organic pollutants are listed since the emission stream was defined as an organic vapor stream.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Issac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
Stream Deleted? St
1 N OR
UN
UN
UN
HAZARDOUS AIR P
Stream Deleted? Po
UN
UN
UN
UN
TETRAHYDROPTHALIMIDE
THJOPHENE
THIOPHOSGENE
THIOUREA
THIRAM
TQUfgws ?-..-• •••;•-• :' ••'.••' ' •,;••••••;•'- :
TOLUENE DIISOCYANATE '
TOLUENE , 24 , D 1 1 SOCYAMATE
TOLUIDINE.O-
TRIBUTYL PHOSPHATE
TRICHLOROBENZENE, 1,2,3-
ce
NERATOR
Cone (ppmv or %)
UNDEFINED
ESC = Exit Enter = Select
Select Potential HAPS Present (Organic)
! O
-------
27a. The pollutant data is arranged into four columns, in the same manner as the control device table. For most
of the common pollutants, the applicant values will already be known, except for the concentration.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Issac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
r- HAP Parameters
«•
ftftttutdftti TOlUEffi -,,-,
Inlet HAP Concentration (ppmv or X)
Molecular Weight (Ib/lb mole)
Specific Heat Equation Constant A
- Specific Heat Equation Constant B
- Specific Heat Equation Constant C
S Specific Gravity
Boiling Point (deg R)
Refractive Index
Heat Vaporization (BTU/lb mole)
Heat of Combustion (BTU/lb mole)
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
Applicant Default Verified
0.0 N
92.2 92.2 N
0.57600 0.57600 N
93.49300 93.49300 N
-31.2200 -31.2200 N
0.86600 0.86600 N
695.08 695.08 N
1.49610 1.49610 N
16863.3 16863.3 N
1683043 1683043 N
X)
ESC = Abort Enter = Select F10 = Continue
28a. The HAP parameters are edited in same manner as described for the stream and control device tables, by
selecting the desired line with the scroll bar and pressing ENTER to access the edit box below. For most pollutants,
you will onfy need to input the concentration of the pollutant in the emission stream.
Last Updated by GMP on 02/12/94
F!) = Plant Notes
Company: ABC Chemical, Inc. Plant Contact: John Jones
Description: Chemical Mfg. Telephone: (919)999-1919
Street: Issac Newton Ave. Permit Date: 10/01/90
City: Research Triangle Park Reviewer: Moore
State: NC Zip: 27709- Streams: 2
S
S
HAP Parameters Applicant Default Verified
Pollutant:
Inlet HAP
Molecular
Specific H
Specific H
Specific H
Specific G
Boiling Po
Refractive
Heat Vapon
Heat of Con
Inlet HAP Concentration (ppmv or X)
AppU**S# Values *2°0 ,0
Default Value:
Verified? (Y/N): N
ESC = Abort F1 = Help PgDn = Exit
ration (BTU/lb mole) 16863.3 16863.3
[fcustion (BTU/lb mole) 1683043 1683043
N
N
N
N
N
N
N
N
N
N
X)
3-14
-------
29a. Save the parameters to the disk by pressing PgDn and selecting the default option.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
-FACILITY-
Company: ABC Chemical, Inc. Plant Contact: John Jones
Description: Chemical Mfg. - Telephone: (919)999-1919
Street: Issac Newton Ave. Permit Date: 10/01/90
City: Research Triangle Park Reviewer: Moore
State: NC Zip: 27709- Streams: 2
r— HAP Parameters
Applicant Default Verified 1
Pollutant: TOLUE
Inlet HAP Conce
Molecular Weigh
Specific Heat E
Specific Heat E
-Select Disposition-
ABORT DATA ENTRY AND EX it '
RETURN FOR FURTHER EDITING
s
specific neat t
Specific Gravit
Boiling Point (c
Refractive Inde>
Heat Vapor izatic
Heat of Combust
leg R) 695.08 695.08
c 1.49610 1.49610
>n (BTU/lb mole) 16863.3 16863.3
on (BTU/lb mole) 1683043 1683043
N
N
N
N
N
N
%)
256. An alternative method of inputing HAPs is to select the SIC category which best describes the processes at
this facility.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Issac Newton Ave.
City: Research Triangle Park
State: NC
, CMTQCTrtij ^TBPAM
Zip: 27709-
Stream Deleted? Stream Type
1 N OR
.UN
UN
UN
i Define Method
Plant Contact:
Telephone:
Permit Date:
Reviewer:
Streams:
rnuTPni nrurrP
Deleted? Control
of HAPS Selection-
John Jones
(919)999-1919
10/01/90
Moore
2
Device
.NERATOR
POLLUTANT LIST
:...;. '... ' ;' sic CAitGtiR*' '..'l;; _'"•' : ;
Stream Deleted? Pollutant
1 N TOLUENE
Cone (ppmv or %)
1290.0
UNDEFINED
UNDEFINED
UNDEFINED
UNDEFINED
ESC = Exit Enter = Select
-------
26b. Now select the appropriate category. The first character of each category is hot-keyed to enable you to move
quickfy through the categories.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
FACILITY-
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Issac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant Contact: John Jones
Telephone: (919)999-1919
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
Stream Deleted? St
1 N OR
UN
UN
UN
I HAZARDOUS AIR P
Stream Deleted? Po
1 N TO
UN
UN
UN
UNC
A'CCO^ll'Tt¥G7'AubTfilJ'G7w^''''B'd^'iSE'EPTN6''
ADHESIVES AND SEALANTS
ADVERTISING, NEC
AGRICULTURAL CHEMICALS
AGRICULTURAL CHEMICALS
AGRICULTURAL CHEMICALS, NEC
AIR AND GAS COMPRESSORS
AIR, WATER & SOLID WASTE MANAGEMENT
AIRCRAFT
AIRCRAFT AND PARTS
EFINED
ce
NERATOR
Cone (ppmv or %)
1290.0
ESC = Exit Enter = Select
Select Appropriate SIC
27b. For ABC Chemical, Inc., the SIC category highlighted below best describes the activities which occur at this
plant.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC Chemical, Inc. Plant Contact: John Jones
Description: Chemical Mfg. Telephone: (919)999-1919
Street: Issac Newton Ave. Permit Date: 10/01/90
City: Research Triangle Park Reviewer: Moore
State: NC Zip: 27709- Streams: 2
I EMISSION STREAM
Stream Deleted? St
1 N OR
UN
UN
UN
| HAZARDOUS AIR P
Stream Deleted? Po
1 N TO
UN
UN
UN
UNC
AA
CARBURETORS, PISTONS, RINGS, VALVES
CARPENTERING
CARPET AND UPHOLSTERY CLEANING
CEMENT, HYDRAULIC
CERAMIC WALL AND FLOOR TILE
CHEESE, NATURAL AND PROCESSED
CHEMICAL PREPARATIONS, NEC
CHlKtCALS :AND 'ALltffl PRODUCTS' : . ' " •• ;
CHEMICALS AND ALLIED PRODUCTS
CHILDREN'S DRESSES AND BLOUSES
CHILDREN'S OUTERWEAR, NEC
A
JEFINED
ce
NERATOR
Cone (ppmv or %)
1290.0
ESC = Exit Enter = Select
Select Appropriate SIC
-------
28b. Listed below are the pollutants associated with the SIC category CHEMICALS AND ALLIED PRODUCTS.
Pick the pollutants present in your stream by pressing ENTER
Last Updated by GHP on 02/12/94
F5 = Plant Notes
FACIL1TY-
Company: ABC Chemical, Inc.
Description: Chemical Mfg.
Street: Issac Newton Ave.
City: Research Triangle Park
State: NC Zip: 27709-
Plant
T
Selecting Associated HAPs
Permit Date: 10/01/90
Reviewer: Moore
Streams: 2
cmaaiun aincwi
Stream Deleted? St
1 N OR
UN
UN
UN
I HAZARDOUS AIR P
Stream Deleted? Po
1 N TO
UN
UN
UN
UNC
CARBURETO
CARPENTER
CARPET AN
CEMENT, H
CERAMIC U
CHEESE, N
CHEMICAL
E«EHieAtS
CHEMICALS
CHILDREN'
CHILDREN'
i
ACEt«»E
BUTYL :" ALCOHOL"
CRESOL.O-
CURENE
METHOXYETHANOL.2-
NAPHTHALENE
SILICA
TOLUENE
TOLUENE , 24 , D 1 1 SOCYANATE
TRICHLOROETHANE.1,1,1-
EFINED
v or X)
Use AX and
ESC = Exit Enter = Select
AY to Move Cursor -- Press ENTER to Make Selection or ESC to Exit
29b. Once this point has been reached, input and edit the HAP parameters as described in steps 28a and 29a.
Last Updated by GMP on 02/12/94
F5 = Plant Notes
Company: ABC Chemical, Inc. Plant Contact: John Jones
Description: Chemical Mfg. Telephone: (919)999-1919
Street: Issac Newton Ave. Permit Date: 10/01/90
City: Research Triangle Park Reviewer: Moore
State: NC Zip: 27709- Streams: 2
r-HAP'ParsmetKrs. '
S ' " '
PfriiutjBftti ACETQ8E
In i let HAP '"'Concent rat ibn""(ppmv" or
Molecular Weight (Ib/lb mole)
Specific Heat Equation Constant A
- Specific Heat Equation Constant B
- Specific Heat Equation Constant C
S Specific Gravity
Boiling Point (deg R)
Refractive Index
Heat Vaporization (BTU/lb mole)
Heat of Combustion (BTU/lb mole)
'*sppt»<5*it 'itefadT* Verified
*>' 6.0 N
58.1 58.1 N
1.50500 1.50500 N
62.24000 62.24000 N
-29.2900 -29.2900 N
0.79200 0.79200 N
593.16 593.16 N
1.35880 1.35880 N
13754.7 13754.7 N
768917.0 768917.0 N
X)
ESC = Abort Enter = Select F10 = Continue
3-1'
-------
CHAPTER 4
REPORTS
GENERATING A REPORT
HAP-PRO is designed to generate the following two reports, in addition to its primary function of
calculating capital and yearly costs for a specified control device. Both reports are options on the Main
Menu.
Report • Purpose
LIST SOURCES BY Generates a report listing all permits that have a specified
STREAM TYPE stream type (organic or inorganic vapors and particulates)
LIST SOURCES BY Generates a report listing all permits that have a
POLLUTANT specified pollutant (ammonia, benzene, toluene, etc.)
The length of time it takes to generate a report will vary with the speed of the computer itself and
the number of records in the system.
What follows is a step-by-step guide on how to generate each report.
-------
REPORT B - LIST SOURCES BY STREAM TYPE
/. Select the desired report with the scroll bar, in this case Selection B.
HAP-PRO Version 1.2
A ENTER/VIEW DATA
:B LIST; SOURCES BY STREAM TYPE
C LIST SOURCES BY POLLUTANT
D REBUILD ALL INDEXES
E REMOVE RECORDS MARKED FOR DELETION
f EXIT TO DOS
Use T and i to move cursor -- Press ENTER to Make Selection
List all Facilities with a specified STREAM TYPE
Specify the desired STREAM TYPE.
HAP-PRO Version 1.2
A ENTER/VIEW DATA
B LIST SOURCES BY STREAM TYPE
: ORGANIC VAPOR ;
INORGANIC VAPOR
ORGANIC PARTICULATE
INORGANIC PARTICULATE
!
Use T and i to move cursor
E£C = Abort ENTER = Select
4-2
-------
3. Choose a destination for your report.
HAP-PRO Version 1.2
A ENTER/VIEW DATA
. & LIST SOURCES BY STREAM TYPE
-- '• ' screen; : :
Printer
ASCII File
Use T and i to move cursor
Sends Report to CRT
4a. The following display will appear.
Printed 06/08/93
at 11:19:09
FACILITIES WITH THE FOLLOWING STREAM TYPE
ORGANIC VAPOR
Page
Facility
ABC Chemical
Aerospace NESHAP
Bob's Example Problem
Carbon Adsorber Test Case
GLASS PAINTING - 1
GLASS PAINTING - 2
GM Adsorber Case
HAP Manual Case
Plant # 1
Texti le Plant A
« Done » < More > Column:
No. Pollutant(s) in Stream
001 TOLUENE
001 BENZENE
001 STYRENE
001 TOLUENE
001 ZINC
001 TOLUIDINE,0-
002 TOLUENE
001 TOLUENE
001 ACETIC ACID
001 Not Recorded
001 Not Recorded
001 TOLUENE
000 Not Recorded
001 Not Recorded
001 Not Recorded
0
Cone.
1000.
500.
0.
1000.
1.
0.
1000.
1000.
1000.
0.
0.
300.
0.
0.
0.
4-3
-------
4b. If a report is sent to an ASCII file, you will be prompted to enter the filename. Type in the name and press
ENTER to continue. The file will automatically be written into the current (default) subdirectory (e.g. \HAP-PRO).
HAP-PRO Version 1.2
A) Enter/View Data
Receiving Drive:
B
C
D
Filename: ! FILEOUT.DOC
Use T and i to move cursor
ESC = Abort ENTER = Select
5. Once the Quit command has been issued (if the report is sent to the screen), the system returns control to HAP-
PRO 's Main Menu.
HAP-PRO Version 1.2
A ENTER/VIEW DATA
B LIST SOURCES BY STREAM TYPE :
C LIST SOURCES BY POLLUTANT
D REBUILD ALL INDEXES
E REMOVE RECORDS MARKED FOR DELETION
F EXIT TO DOS
i
Use T and l to move cursor -- Press ENTER to Make Selection
List all Facilities with a specified STREAM TYPE
4-4
-------
REPORT C - LIST SOURCES BY POLLUTANT
1. Instead of Selection B on the Main Menu, choose selection C.
HAP-PRO Version 1.2
A ENTER/VIEW DATA
B LIST SOURCES BY STREAM TYPE
C L I ST SOURCES BV POLWTANT
D REBUILD ALL INDEXES
E REMOVE RECORDS MARKED FOR DELETION
F EXIT TO DOS
Use T and i to move cursor -- Press ENTER to Make Selection
List all Facilities with a specified STREAM TYPE
2. Now select the type of pollutant by choosing Organic.
HAP-PRO Version 1.2
A ENTER/VIEW DATA
B LIST SOURCES BY STREAM TYPE
C LIST SOURCES BY POLLUTANT
D | Select Pollutant Type—
E Organic ION
F !
Inorganic
Use r and I to move cursor -- Press ENTER to Make Selection
-------
3. Once ENTER is pressed, the pollutant pop-up displayed below should appear. Use the cursor, PgDn, and PgUp
to move the cursor or press the first character of the pollutant you are seeking.
HAP-PRO Version 1.2
A ENTER/VIEW DATA
B LIST SOURCES BY STREAM TYPE
C LIST SOURCES BY POLLUTANT
ACENAPHTHEME :
ACENAPHTHYLENE
ACETALDEHYDE
ACETALDEHYDE
ACETIC ACID
ACETIC ANHYDRIDE
ACETONE
Use i and T to move cursor -- Press ENTER to Make Selection
4. Once the desired pollutant is highlighted, in this case ACETONE, press ENTER to select it.
HAP-PRO Version 1.2
A ENTER/VIEW DATA
B LIST SOURCES BY STREAM TYPE
C LIST SOURCES BY POLLUTANT
ACENAPHTHENE
ACENAPHTHYLENE
ACETALDEHYDE
ACETALDEHYDE
ACETIC ACID
ACETIC ANHYDRIDE
ACETONE
Use r and i to move cursor -- Press ENTER to Make Selection
-------
5. At this point, the screen shown below is generated, assuming these records were found for the pollutant specified.
Printed 06/08/93
at 11:19:22
Facility
ABC Chemical
NC Petroleum
FACILITIES WITH THE FOLLOWING POLLUTANT
ACETONE
No. Cone.
Page
001 1000.0
001 1000.1
002 1000.0
« Done » < More > Column:
6. Once the Done command has been issued (if the report is sent to the screen), the system returns control to HAP-
PRO's Main Menu.
HAP-PRO Version 1.2
A ENTER/VIEW DATA
B LIST SOURCES BY STREAM TYPE
C LIST SOURCES BY POLLUTANT
D REBUILD ALL INDEXES
E REMOVE RECORDS MARKED FOR DELETION
F EXIT TO DOS
Use T and i to move cursor -- Press ENTER to Make Selection
List all Facilities with a specified POLLUTANT
-------
APPENDIX A
DATA DICTIONARY
Parameters marked with a * are not used in calculations; all other parameters must be input to perform
calculations accurately.
Key to DATA TYPE
C - Character
N - Numeric
F - Floating Decimal
M * Memo
UPDATE STAMP
INPUT PARAMETERS
Last Updated by
on
FACILITY DATA
INPUT PARAMETERS
Data
Type
C
D
Len Fieldname Range Values (default)
3
8
updated_by
updt_date
Company
Description
Street
City
State
Zip
Plant Contact
Telephone
Permit Date
Reviewer
Streams
Plant Notes
C
C
C
C
C
C
C
C
D
C
N
M
25
25
25
25
2
10
20
13
8
20
3
10
plant_name
scen_desc
address
city
state
zip
contact
telephone
appl_date
reviewer
no_streams
notes
USPS Code
0 - 999
A-i
-------
THERMAL INCINERATOR
INPUT PARAMETERS
ORGANIC VAPOR ONLY
Emission Stream Input Parameters:
Maximum Flow Rate (scfm)
Stream Temperature (deg F)
Oxygen Content (X)
* Moisture Content (X)
* Stream Pressure (mmhg)
HAP Data
Manual Type
Len Fieldname Range Values (default)
Qe
Te
02
N
N
N
N
N
8
8
5.1
5.1
8.1
flow_rate
temp
o2
moisture
pres
(77)
0 - 100
0 - 100
Design Related Input Parameters:
Desired Destruction Efficiency (X)
Combustion Temp (°F)
Residence Time (sec)
Heat Exchanger Efficiency (X)
Reference Temp (°F)
Heat Cap. of Air at Comb. Temp (Btu/lb°F)
Cost Related Input Parameters:
Duct Cost ($/linear ft)
Length of Duct (ft)
Total Pressure Drop (in H20)
Average Equipment Life (yr)
Operator Labor Requirements (hrs/shift)
Maintenance Labor Requirements (hrs/shift)
Operator Labor Wage ($/hr)
Maintenance Labor Wage ($/hr)
Operating Hours (hrs/yr)
Site Preparation Cost ($)
Building Cost ($)
Interest Rate (X)
Price of Natural Gas (J/1000 cu ft)
Damper Cost ($)
MESSAGES TO USER
NONE
INTERMEDIATE CALCULATED RESULTS
calc_de = calculated destruction efficiency
Od = dilution air requirements
The = temp of emission stream after heat exchange
Of * natural gas flow rate
Qfg = calc flue gas flow rate
Vc = calc combustion chamber volume
Fp = electricity requirement
fuel = fuel usage
he « heat content
DE
Tc
tr
HR
Tr
Cpair
P
n
olr
mlr
olwr
mlwr
HRS
spc
bldg
i
ngc
Pdamp
N
F
F
N
F
F
N
N
N
N
N
N
N
N
N
N
N
N
N
5.1
8.7
8.7
5.1
8.7
8.7
8.2
8.1
8.1
8.1
8.1
8.1
8.2
8.2
8
8
8
8.2
8.2
8
dest.eff
comb_.temp
res_time
heat exch
t_re?
heat_air1
duct cost
lenJSuct
pres_drop
eqpt_life
olabor_req
mlabor_req
olaborwage
mlaborwage
op_hrs_yr
site_cost
bldg_cost
int_rate
gas_cost
dampers
0 - 100 (98)
0,35,50,(70)
(77)
(0.265)
(10)
(0.5)
(0.5)
(12.96)
(U.26)
(6000)
(10)
(3.30)
CAPITAL COSTS
spc = site preparation cost
bldg - building
PEC = purchased equipment cost
+ DC = direct installation costs
Tdc = total direct costs
+ Tic = total indirect costs
Tec = total capital costs
A-2
-------
OPERATING COSTS
Fc « fuel cost
AEC « electricity cost
Olc » labor
Svd » supervisory cost
Mlc » maintenance labor cost
+ Ntc » maintenance materials cost
Tdac = total direct annual costs (operating costs)
OH . * overhead
adm * administrative cost
Pt = property taxes
In = insurance
+ CRC = capital recovery cost
Tiac = total indirect annual costs
* total annual costs
Tac = Tdac + Tiac
A-3
-------
CATALYTIC INCINERATOR
INPUT PARAMETERS
ORGANIC VAPOR ONLY
Emission Stream Input Parameters:
Maximum Flow Rate (scfm)
Stream Temperature (deg F)
Oxygen Content (X)
* Moisture Content (X)
* Stream Pressure (romhg)
Design Related Input Parameters:
Desired Destruction Efficiency (X)
Heat Exchanger Efficiency (X)
Heat Cap. of Air at Comb. Temp (Btu/lb'F)
Space Velocity (per hr)
Reference Temp (*F)
Catalytic Oxidation Temperature (°F)
Cost Related Input Parameters:
Duct Cost ($/linear ft)
Length of Duct (ft)
Total Pressure Drop (in H20)
Average Equipment Life (yr)
Operator Labor Requirements (hrs/shift)
Maintenance Labor Requirements (hrs/shift)
Operator Labor Wage ($/hr)
Maintenance Labor Wage ($/hr)
Operating Hours (hrs/yr)
Site Preparation Cost ($)
Building Cost ($)
Interest Rate (X)
Price of Natural Gas ($71000 cu ft)
Catalyst Replacement Cost ($)
Damper Cost ($)
HAP
Manual
Qe
Te
02
DE
HR
Cp1
sv
Tr
Tci
p
n
olr
mlr
olwr
mlwr
HRS
spc
bldg
i
ngc
Ccat
Pdamp
Data
Type
N
N
N
N
N
N
N
F
F
F
F
N
N
N
8
N
N
N
N
N
N
N
M
N
N
N
Len
8
8
5.1
5.1
8.1
5.1
5.1
8.7
8.7
8.7
8.7
8.2
8.1
8.1
.1
8.1
8.1
8.2
8.2
8.2
8
8
8.2
8.2
8
8
Fieldname
flow rate
temp"
o2
moisture
pres
dest..eff
heat._exch
heat~air1-
space vel
t_re1r
t~co
duct_.cost
len_eiuct
pres_drop
eqpt_life
olabor_req
mlabor_req
o labor wage
mlaborwage
op_hrs_yr
site_cost
bldg_cost
int_rate
gas_cost
cat~cost
dampers
Range Values
(77)
0 - 100
0 - 100
0 - 100 (95)
0.35, (50), 70
(.0254)
(77)
(600)
(10)
(0.5)
(0.5)
(12.96)
(14.26)
(6000)
(10)
(3.30)
INTERMEDIATE CALCULATED RESULTS
catc_de = calculated destruction efficiency
he = heat content
Qd = dilution air requirements
The = temp of emission stream after heat exchange
Qf = natural gas flow rate
Qcom » flue gas flow rate
Qcoma_a = actual flow rate
Vbed = catalyst bed requirement
Fp = electricity requirement
fuel = fuel usage
MESSAGES TO USER
NONE
A-4
-------
CAPITAL COSTS
spc a site preparation cost
bldg = building
PEC = purchased equipment cost
Oc • direct installation costs
Tdc * total direct costs
Tic = total indirect costs
Tec = total capital costs
OPERATING COSTS
Fc
AEC
CRCT
Olc
SVC
Mlc
+ Mtc
s
s
s
a
s:
s
fuel cost
electricity cost
catalyst replacement cost
labor
supervisory cost
maintenance labor cost
maintenance materials cost
Tdac = total direct annual costs (operating costs)
OH » overhead
adm = administrative cost
Pt « property taxes •
In = insurance
CRC = capital recovery cost
Tiac = total indirect annual costs
* total annual costs
Tac = Tdac + Tiac
A-5
-------
FLARE
INPUT PARAMETERS
ORGANIC VAPOR ONLY
Emission Stream Input Parameters:
Naxinun Flow Rate (scfm)
Stream Temperature (deg F)
Oxygen Content (X)
Moisture Content (X)
Stream Pressure (mmhg)
Design Related Input Parameters:
Flare Tip Diameter (in)
Temp of Flare Gas CF)
Flare Gas Heat Content (BTU/scf)
Supplementary Fuel Heat Content (BTU/scf)
Mean Molecular Weight of Stream (Ib/lb-mole)
Cost Related Input Parameters:
Duct Cost ($/linear ft)
Length of Duct (ft)
Stack Cost ($)
Total Pressure Drop (in H20)
Average Equipment Life (yr)
Operator Labor Requirements (hrs/shift)
Maintenance Labor Requirements (hrs/shift)
Operator Labor Wage (S/hr)
Maintenance Labor Wage ($/hr)
Operating Hours (hrs/yr)
Site Preparation Cost ($)
Building Cost ($)
Interest Rate (X)
Price of Natural Gas (S/1000 cu ft)
Cost of Fans and Motors ($)
Damper Cost ($)
HAP
Manual
Qe
Te
02
Dtip
Tflg
hflg
hf
> MUe
Pstack
P
n
olr
mlr
olwr
mlwr
HRS
spc
bldg
i
ngc
Pfan
Pdamp
Data
Type
N
N
N
N
N
F
F
F
F
F
N
N
N
N
8
N
N
N
N
M
N
N
N
N
N
N
Len
8
8
5.1
5.1
8.1
8.7
8.7
8.7
8.7
8.7
8.2
8.1
8
8.1
.1
8.1
8.1
8.2
8.2
8
8
8
8.2
8.2
8
8
Fieldname
flow_rate
temp
o2
moisture
pres
diameter
t_gas
heat._cont
suppjieat
avgjiM
duct cost
lenjiuct
stack:_cost
pres_drop
eqptjlfe
olabor_req
mlabor_req
olaborwage
mlaborwage
op_hrs_yr
site_cost
bldg_cost
int_rate
gas~cost
fan_cost
dampers
Range Vi
(77)
0 - 100
0 - 100
(300)
(882)
(29)
(10)
(0.5)
(0.5)
(12.96)
(U.26)
(6000)
(10)
(3.3)
MESSAGES TO USER
Condition
hflg < 300
hflg > 1000
Variable
DEflag
Deflag
Message
Based on hflg.
Based on hflg.
DE
DE
98
98
INTERMEDIATE CALCULATED RESULTS
Of = supplemental fuel requirements
Uflg = flare gas exit velocity
DE = efficiency level
Qs = steam requirement
Theta_b = flame angle
H = flare height
fuel = fuel usage
Fp = electricity requirement
A-6
-------
CAPITAL COSTS
Spc * site preparation
Btdg * building cost
PEC a purchased equipment cost
+ DC = direct installation costs
Tdc = total direct costs
+ Tic = total indirect costs
Tec a total capital costs
OPERATING COSTS
Fc = fuel cost
AEC = electricity cost
Olc s labor
Svc = supervisory cost
Mlc = maintenance labor cost
Mtc a maintenance materials cost
+ SC = steam cost
Tdac = total direct annual costs (operating costs)
OH = overhead
adm = administrative cost
Pt = property taxes
In = insurance
+ CRC = capital recovery cost
Tiac = total indirect annual costs
* total annual costs
Tac = Tdac + Tiac
A-7
-------
CARBON ADSORBER
INPUT PARAMETERS
ORGANIC VAPOR ONLY
Emission Stream Input Parameters:
Maximum Flow Rate (scfm)
Stream Temperature (deg F)
Oxygen Content (X)
Moisture Content (%}
Stream Pressure (mmhg)
HAP Input Parameters:
Inlet HAP Concentration (ppmv or X)
Molecular Weight (Ib/lb mole)
Specific Heat Equation Constant A
Specific Heat Equation Constant B
Specific Heat Equation Constant C
Specific Gravity
Boiling Point
Refractive Index
Heat Vaporization (BTU/lb mole)
Design Related Input Parameters:
Design Type
Carbon-to-Vessel Ratio
Removal Efficiency (X)
Number of Adsorbing Beds
Number of Deadsorbing Beds
Stream Velocity Through Bed (ft/roin)
Operational Mode
Cycle Time for Adsorption (hr)
Cycle Time for Regeneration (hr)
Cycle Time for Drying and Cooling (hr)
Steam Ratio (Ib steam/Ib carbon)
Cost Related Input Parameters:
Duct Cost ($/linear ft)
Length of Duct (ft)
Stack Cost ($)
Average Equipment Life (yr)
Operator Labor Requirements (hrs/shift)
Maintenance Labor Requirements (hrs/shift)
Operator Labor Wage (S/hr)
Maintenance Labor Wage ($/hr)
Operating Hours (hrs/yr)
Site Preparation Cost ($)
Building Cost ($)
Interest Rate (X)
Equipment Factor
Carbon Cost ($/lb)
Steam Cost ($/lb)
Cooling Water Cost (S/1000 gals)
Value of Recovered Product ($/lb)
Damper Cost ($)
HAP
Manual
Qe
Te
HAPe
CVR
RE
NA
NO
Ue
Theta_a
Theta_reg
Theta dc
St
Pstack
n
olr
) mlr
olwr
mlwr
HRS
spc
bldg
i
Fm
Cc
PS
Pew
VRPC
Pdamp
Data
Type
N
N
N
N
N
C
F
N
N
N
F
C
F
F
F
F
N
N
N
8
N
N
N
N
N
N
N
N
N
N
N
N
N
N
Len
8
8
8.1
8.1
8.1
8.1
8.1
8.5
8.5
8.5
8.5
8.5
8.5
8.1
7
8.7
5.1
8
8
8.7
7
8.7
8.7
8.7
8.7
8.2
8.1
8
.1
8.1
8.1
8.2
8.2
8
a
8
8.2
a
8.2
8.3
8.2
8.2
8
Fieldname
flow rate
temp"
o2
moisture
pres
hap_conc
mw
cpa
cpb
cpc
SG
boil joint
refr_index
hvap
ad_type
cv_ratio
remove_eff
no_ad_beds
no_de_beds
st'vel bed
mode
ct_adsorp
ct_regen
ct_drycool
steam_rat
duct_cost
len_duct
stack cost
eqpt_li?e
olabor_req
mlabor_req
olaborwage
mlaborwage
op_hrs_yr
site_cost
bldg_cost
int_rate
eqpt_fact
carb_cost
steam_cost
water_cost
value prod
dampers
Range Values
77
(def
HORIZTL/VERTICL
0.25-0.40 (0.
0 - 100 (90)
(1)
(1)
(85)
333)
CONTINU/BATCH
(2)
(2)
(0.25)
(0.30)
(10)
(0.5)
(0.5)
(12.96)
(14.26)
(6000)
(10)
1 - 10 (1)
(2.00)
(0.006)
(0.20)
A-3
-------
MESSAGES TO USER
Condition Variable Message
S < 97 Sf lag "Calculated value for S is beyond equation accuracy -- Consult Manual
S > 2110 Sf lag "Calculated value for S is beyond equation accuracy -- Consult Manual
Bf > 4 Bflag ***Carbon bed is fluidized -- Recheck steam ratio or regeneration
theta a < Tflagl,
(NA *~theta_reg)/MO Tflag2 **** Ads. Cycle time changed to [<«* * th*tsyr*9?/li»] to allow for
continuous operation.
INTERMEDIATE CALCULATED RESULTS
Dtot = density of HAP pollutants
Mhap = inlet HAP loading
Uc = adsorptive capacity
Creq = carbon requirement
Ov = vessel diameter
Lv = vessel length
S = vessel surface area
Qs = steam rate
Ocw = cooling water flow rate
Bf = bed fluidization
Pb - pressure drop
hpsf = system fan power
theta dcf = power for drying/cooling fan
FRdcf" = bed gas flow rate
Pdef = electricity requirement for drying/cooling fan
hpcwp = horsepower required for cooling water pump
CAPITAL COSTS
Spc s site preparation
Bldg = building cost
PEC = purchased equipment cost
+ DC = direct installation costs
Tdc = total direct costs
•••Tic = total indirect costs
Tec = total capital costs
OPERATING COSTS
AEC - electricity cost
Ccw = cooling water cost
Olc = labor
Svc = supervisory cost
Mlc = maintenance labor cost
Mtc = maintenance materials cost
+ CS = steam cost
Tdac = total direct annual costs (operating costs.)
OH = overhead
adm = administrative cost
Pt = property taxes
In = insurance
+ CRC = capital recovery cost
Tiac = total indirect annual costs
- VRP = value of recovered product
* total annual costs
Tac - Tdac + Tiac - VRP
A-9
-------
PACKED COLUMN SCRUBBER (STRIPPER)
INPUT PARAMETERS
Note: Only one of the following stream types can be specified
Emission Stream Input Parameters:
ORGANIC VAPOR
Maxinun Flow Rate (scfm)
Stream Temperature (deg F)
* Oxygen Content (X)
* Moisture Content (X)
* Stream Pressure (mmhg)
INORGANIC VAPOR
Maximum Flow Rate (scfm)
Stream Temperature (deg F)
* Moisture Content (X)
* Stream Pressure (mmhg)
* Are Halogens Present? (Y/N)
* Are Metals Present? (Y/N)
ORGANIC PARTICIPATE
Maximum Flow Rate (scfm)
Stream Temperature (deg F)
Moisture Content (X)
* Mean Particle Diameter (Ug)
* Particulate Content (gr/scf)
HAP Input Parameters:
Inlet HAP Concentration (ppmv or X)
Molecular Weight (Ib/lb mole)
Specific Heat Equation Constant A
Specific Heat Equation Constant B
Specific Heat Equation Constant C
Antoine Equation Constant A
Antoine Equation Constant B
Antoine Equation Constant C
Heat Vaporization (BTU/lb mole)
Design Related Input Parameters:
Removal Efficiency (X)
* What Solvent is used?
Slope of the Equilibrium Curve
Absorption Factor
Schmidt number for HAP/Emission Stream
Schmidt number for HAP/Solvent
Density of the Emission Stream (Ib/ft3)
Density of the Solvent (Ib/lb mole)
Average Mole Wt of the Stream (Ib/lb mole)
Mole Ut of the Solvent (Ib/lb mole)
Solvent Viscosity (centipoise)
* Packing Material
Packing Constant a
Packing Constant b
Packing Constant c
Packing Constant d
Packing Constant Epsilon
Packing Constant Y
Packing Constant s
Packing Constant g
Packing Constant r
Fraction Flooding Velocity
Number of Beds
HAP
Manual
Qe
Te
Qe
Te
Qe
Te
Rhum
HAPe
RE
m
AF
Scg
Scl
Dg
Dl
MUstm
MUsol
mu
F
F
F
F
e
F
F
F
F
f
Nbed
Data
Type
N
N
N
N
N
N
N
N
N
C
C
N
N
N
N
N
F
F
F
N
C
F
F
F
F
C
8
8
8
3
F
8
8
3
8
8
N
Len Fieldname
8 flow rate
8 temp"
5.1 o2
5.1 moisture
8.1 pres
8 flow_rate
8 temp"
5.1 moisture
8.1 pres
1 halogens
1 metals
8 flowjrate
8 temp"
5.1 moisture
8.3 diameter
8.3 part_cont
8.1 hap cone
8.1 mw
8.5 cpa
8.5 cpb
8.5 cpc
8.5 ante
8.5 antb
8.5 ante
8.1 hvap
5.1 remove_eff
13 solvent
8.7 slope_curv
8.7 absorption
8.7 schdt_strm
8.7 schdt_solv
8.7 dnsty_strm
8.7 dnsty_solv
8.7 avg_mw_stm
8.7 avg_mw_sol
8.7 solv^visc
1 packjnat
.7 packing_a
.7 packing_b
.7 packing_c
.7 packing_d
8.7 packing_e
.7 packing_y~
.7 packing_s
.7 packing_3
.7 packing r
.7 flood_vel
8 no beds
Range Values
(77)
0 - 100
0 - 100
(760)
(77)
0 - 100
Y,(N)
Y,(N)
(77)
0 - 100
0 - 100 (95)
(water)
(2)
(1.6)
(62.4)
(29)
(18)
1 - 3 (1)
(0.60)
1
A-10
-------
Cost Related Input Parameters:
Cost of Packing Material ($/ft3)
Cost of Fans and Motors ($)
Duct Cost (Vlinear ft)
Length of Duct (ft)
Stack Cost ($)
Average Equipment Life (yr)
Operator Labor Requirements (hrs/shift)
Maintenance Labor Requirements (hrs/shift)
Operator Labor Wage ($/hr)
Maintenance Labor Wage ($/hr)
Operating Hours (hrs/yr)
Site Preparation Cost ($)
Building Cost ($)
Interest Rate (X)
Damper Cost ($)
Steam Cost ($/lb)
Cooling Water Cost ($/1000 gals)
Key for PACKING MATERIAL
1 = rachig rings
2 = pall rings
3 = flexisaddles
Pcost
Pfan
Pstack
n
olr
mlr
olur
mlwr
HRS
spc
bldg
i
Pdamp
PS
Ccw
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
8.2
8
8.2
8.1
8
8.1
8.1
8.1
8.2
8.2
8
8
8
8.2
8
8.3
8.2
pack_cost
fan_cost
duct cost
lenJJuct
stack cost
eqpt_life
olabor_req
mlabor_req
olaborwage
mlaborwage
op_hrs_yr
site_cost
bldg~cost
int_rate
dampers
steam_cost
water_cost
(10)
(0.5)
(0.5)
(12.96)
(14.26)
(6000)
(10)
(0.006)
(0.20)
MESSAGES TO USER
NONE
INTERMEDIATE CALCULATED RESULTS
ABS - flooding correlation
Garea = gas stream flow rate
Gmol = gas stream flow rate (Ib mole/hr)
ImoI = liquid stream flow rate (Ib mole/hr)
Igat = liquid stream flow rate (gals/min)
Acol = column area
DeoI - diameter
HAPo = HAP outlet concentration
Nog = no of gas transfer units
Hg = ht. of gas transfer unit
HI = ht. of liquid transfer unit
Hog = ht. of overall gas transfer unit
Httot - total ht. of column
Vpack = packing volume
Pa = column pressure drop
Ptot = total colum pressure drop
Fp = electricity requirement
CAPITAL COSTS
Spc = site preparation
Bldg = building cost
PEC = purchased equipment cost
+ DC = direct installation costs
Tdc = total direct costs
+ Tic = total indirect costs
Tec = total capital costs
A-11
-------
OPERATING COSTS
AEC * electricity cost
Olc - labor
Svc = supervisory cost
Mlc = maintenance labor cost
Mtc = maintenance materials cost
+ ASC = annual solvent cost
Tdac = total direct annual costs (operating costs)
OH = overhead
adm = administrative cost
Pt = property taxes
In = insurance
+ CRC * capital recovery cost
Tiac = total indirect annual costs
* total annual costs
Tac = Tdac + Tiac
A-12
-------
CONDENSER
INPUT PARAMETERS
ORGANIC VAPOR ONLY
Emission Stream Input Parameters:
Naxioun Flow Rate (scfm)
Stream Temperature (cleg F)
* Oxygen Content (X)
* Moisture Content (X)
Stream Pressure (mmhg)
HAP Input Parameters:
Inlet HAP Concentration (ppmv or X)
Molecular Weight (Ib/lb mole)
Specific Heat Equation Constant A
Specific Heat Equation Constant B
Specific Heat Equation Constant C
Antoine Equation Constant A
Antoine Equation Constant B
Antoine Equation Constant C
Heat Vaporization (BTU/lb mole)
Design Related Input Parameters:
Removal Efficiency (X)
* Coolant Used
Condensation Temp (*F)
Overall Heat Transfer Coeff (BTU/hr-ft2-"F)
Avg Specific Heat for Coolant (BTU/lb/'F)
Heat Cap. of Air (Btu/lb/mol'F)
Heat Cap. of HAP (Btu/lb mol'F)
Condenser Type
Length of Tube (in)
Cost Related Input Parameters:
Value of Recovered Product ($/lb)
Duct Cost (Vlinear ft)
Length of Duct (ft)
Cost of Fans and Motors ($)
Damper Cost ($)
Stack Cost ($)
Total Pressure Drop (in H20)
Average Equipment Life (yr)
Operator Labor Requirements (hrs/shift)
Maintenance Labor Requirements (hrs/shift)
Operator Labor Wage ($/hr)
Maintenance Labor Wage ($/hr)
Operating Hours (hrs/yr)
Site Preparation Cost ($)
Building Cost ($)
Interest Rate (%)
Key for CONDENSER TYPE:
1 = fixed tubesheet
2 = floating head
HAP
Manual
Oe
Te
Pe
HAPe
MWhap
anta
antb
ante
RE
Tcon
> U
CPcool
Cpair
CPhap
CON type
tubelen
VRPC
Pfan
Pdamp
Pstack
P
n
olr
mlr
olwr
mlwr
HRS
spc
bldg
i
Data
Type
N
N
N
N
N
F
F
F
F
F
F
F
F
F
N
C
F
F
F
F
F
C
F
N
N
N
N
N
N
N
8.
N
N
N
N
N
N
N
M
Len
8
8
5.1
5.1
8.1
8.1
8.1
8.5
8.5
8.5
8.5
8.5
8.5
8.1
5.1
13
8.7
8.7
8.7
8.7
8.7
1
8.7
8
8.2
8.1
8
8
8
8.1
1
8.1
8.1
8.2
8.2
8
8
8
3.2
Fieldname
f low_rate
temp"
o2
moisture
pres
hap cone
DM ~f
cpa-
cpb
cpc
anta
antb
ante
hvap
removl_eff
coolant
t_coolant
heat_coeff
ag_sh_cool
heat_air
cphap
contype
tubelen
value_prod
duct cost
len_duct
fan_cost
dampers
stack_cost
pres_drop
eqpt_life
olabor_req
mlabor_req
o labor wage
m labor wage
op_hrs_yr
site_cost
bldg_cost
int_rate
Range Values
(77)
0 - 100 (90)
(water)
(20)
(D,2
(8), 12,16
(5)
(10)
(0.5)
(0.5)
(12.96)
(H.26)
(6000)
(10)
MESSAGES TO USER
NONE
A-13
-------
INTERMEDIATE CALCULATED RESULTS
Otlm
Ppart
Tcon
Hload
Aeon
Qcool
Ref
Qrec
log mean temp difference
partial pressure
condenser temp
condenser heat load
condenser size
coolant flow rate
refrigeration capacity
recovered product
CAPITAL COSTS
Spc
Bldg
PEC
+ DC
Tdc
Tref
+ Tic
site preparation
building cost
purchased equipment cost
direct installation costs
total direct costs
refrigerant capital costs
total indirect costs
Tec = total capital costs
OPERATING COSTS
AEC * electricity cost
Olc = labor
Svc * supervisory cost
Mlc * maintenance labor cost
+ Mtc = maintenance materials cost
Tdac * total direct annual costs (operating costs)
OH * overhead
adffl = administrative cost
Pt » property taxes
In = insurance
+ CRC = capital recovery cost
Tiac = total indirect annual costs
RC = value of recovered product
* total annual costs
Tac * Tdac + Tiac - RC
A-14
-------
FABRIC FILTERS
INPUT PARAMETERS
INORGANIC PARTICIPATE ONLY
Emission Stream Input Parameters:
Naxinun Flow Rate (scfm)
Stream Temperature (deg F)
Moisture Content (X)
Mean Particle Diameter (Ug)
Particulate Content (gr/scf)
* Drift Velocity (ESPs only, ft/s)
S03 Concentration (ppmv)
HAP Input Parameters:
Inlet HAP Concentration (ppmv or %)
* Molecular Weight (Ib/lb mole)
* Specific Heat Equation Constant A
* Specific Heat Equation Constant B
* Specific Heat Equation Constant C
* Antoine Equation Constant A
* Antoine Equation Constant B
* Antoine Equation Constant C
* Heat Vaporization (BTU/lb mole)
HAP Data
Manual Type Len
Qe 1
Te 1
Me 1
Dp 1
Partcon 1
1
S03 1
HAPcon f
= 8.7
'• 8.7
1 5.1
: 8.7
= 8.7
= 8.7
: 8.7
8.1
8.1
8.5
8.5
8.5
8.5
8.5
8.5
8.1
flow_rate
temp
moisture
diameter
part_cont
velocity
so3_conc
hap_conc
mw
cpa
cpb
cpc
ant a
antb
ante
hvap
Fieldname Range Values (default)
(77)
Design Related Input Parameters:
Filter Cleaning Method
Mat. Type (polyester, propylene etc.)
Air to Cloth Ratio (ft/min)
* Neg. Baghouse Operating Pressure? (Y/N)
Cost Related Input Parameters:
Site Preparation Cost ($)
Building Cost ($)
Cost of Cyclone ($)
Cost of Bag ($/ft2)
Life of Bag (yr)
Waste Disposal Cost Factor ($/ton)
Duct Cost ($/linear ft)
Length of Duct (ft)
Cost of Fans and Motors (S)
Damper Cost ($)
Stack Cost ($)
Stainless Steel Add on (Y/N)
Insulation Add on (Y/N)
Total Pressure Drop (in H20)
Average Equipment Life (yr)
Operator Labor Requirements (hrs/shift)
Maintenance Labor Requirements (hrs/shift)
Operator Labor Wage ($/hr)
Maintenance Labor Wage ($/hr)
Operating Hours (hrs/yr)
Interest Rate <%)
** Key for CLEANING METHOD:
MSI - Mechanical Shaking, Intermittent
MSC - Mechanical Shaking, Continuous
PJFCH - Pulse Jet Filters, Common Housing
PJFM - Pulse Jet Filters, Modular
RAF - Reverse Air Filters
C8F - Custom Built Filters
FCM
clean meth
ACrat
spc
bldg
Pcyc
Bagc
nb
Wdcf
Pfan
Pdamp
Pstack
SS
INS
P
n
olr
mlr
olwr
mlwr
MRS
i
C
F
C
N
N
N
N
N
N
N
N
N
N
N
C
C
N
N
N
N
N
N
N
13
8.7
1
8
8
8
8
8.1
8
8.2
8.1
8
8
8
1
1
8.1
8.1
8.1
8.1
8.2
8.2
8
3.2
material
air_cloth
bag_conf i g
site_cost
bldg~cost
cyc_cost
cost bag
bag_life
disp_fact
duct~cost
len_duct
fan_cost
dampers
stack_cost
stainsteel
insulation
pres_drop
eqpt_life
olabor_req
mlabor_req
olaborwage
mlaboruage
op_hrs_yr
int rate
(polyes
(2.5)
(Y), N
(.59)
(2)
(200)
(N)
(N)
(5)
(20)
(3)
(1)
(12.96)
(14.26)
(6000)
<10)
** (MSI),MSC,PJFCH,
PJFM,RAF,CBF
A-15
-------
MESSAGES TO USER
NONE
INTERMEDIATE CALCULATED RESULTS
Anc = net cloth area
Ate = total cloth area
CAPITAL COSTS
Spc * site preparation
Bldg = building cost
PEC * purchased equipment cost
+ DC = direct installation costs
Tdc = total direct costs
+ Tic * total indirect costs
Tec • total capital costs
OPERATING COSTS
AEC • electricity cost
Olc = labor
Svc = supervisory cost
Mlc * maintenance labor cost
Mtc = maintenance materials cost
Wdc = waste disposal cost
cca = compressed air cost
crb = cost of replacement bags
Tdac = total direct annual costs (operating costs)
OH = overhead
adm - administrative cost
Pt = property taxes
In = insurance
+ CRC = capital recovery cost
Tiac = total indirect annual costs
* total annual costs
Tac = Tdac + Tiac
A-16
-------
VENTURI SCRUBBER
INPUT PARAMETERS
ORGANIC PARTICIPATE ONLY
Emission Stream Input Parameters:
Maximum Flow Rate (scfm)
Stream Temperature (deg F)
* Moisture Content (X)
* Mean Particle Diameter (Ug)
* Paniculate Content (gr/scf)
* Drift Velocity (ESPs only, ft/s)
* S03 Concentration (ESPs only, ppmv)
HAP Data
Manual Type
Qe
Te
Len Fieldname Range Values (default)
8
8
5.1
8.7
8.7
8.7
8.7
flow_rate
temp"
moisture
diameter
part_cont
velocity
so3 cone
(77)
Design Related Input Parameters:
Required Collection Efficiency (X) CE
Sat. Moist. Content (Ibs H20/lb of dry air) Lws
Actual Moist. Content (Ibs H20/lb of dry air) Lwa
Stream Saturation Temperature (*F) Tes
Material of Construction Mat
Cost Related Input Parameters:
Site Preparation Cost ($)
Building Cost ($)
Cost of Cyclone ($)
Duct Cost (S/linear ft)
Length of Duct (ft)
Cost of Fans and Motors ($)
Damper Cost ($)
Stack Cost (J)
Total Pressure Drop (in H20)
Average Equipment Life (yr)
Operator Labor Requirements (hrs/shift)
Maintenance Labor Requirements (hrs/shift)
Operator Labor Wage ($/hr)
Maintenance Labor Wage ($/hr)
Operating Hours (hrs/yr)
Interest Rate (X)
Key to MATERIAL OF CONSTRUCTION:
0 = Carbon Steel
1 = 304 Stainless Steel
2 = 316 Stainless Steel
MESSAGES TO USER
Condition
P > 80
Oea < 10000
Qea > 150000
5.1
8.7
8.7
8.7
1
contrl_eff
satjnoist
actjnoist
sat_temp
material
0 - 100 (99)
** 0 - 3 (0)
spc
bldg
Pcyc
Pfan
Pdamp
Ps tack
P
n
olr
mlr
olur
mlwr
MRS
i
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
8
8
8
8.2
8.1
8
8
8
8.1
8.1
8.1
8.1
8.2
8.2
8
8.2
site_cost
bldg_cost
cyc_cost
duct cost
len_duct
fan_cost
clampers
stack_cost
pres_drop
eqpt_llfe
olabor_req
ml abor_req
olaborwage
mlaborwage
op_hrs_yr
int_rate
0 - 80 (40)
(10)
(2)
(1)
(12.96)
(14.26)
(6000)
(10)
Variable Message
Pflag **Venturi Scrubber may not be applicable with this pressure drop
Qeaflag ***Cost Value may not be accurate for this flow rate
Qeaflag ***Cost Value may not be accurate for this flow rate
INTERMEDIATE CALCULATED RESULTS
Qea = actual flow rate
Qes = saturation flow rate
A-V
-------
CAPITAL COSTS
Spc
Bldg
PEC
+ Oc
Tec
site preparation
building cost
purchased equipment cost
direct installation costs
Tdc « total direct costs
Tic - total indirect costs
total capital costs
OPERATING COSTS
AEC
Olc
Svc
Mlc
Mtc
+ WCst
electricity cost
labor
supervisory cost
maintenance labor cost
maintenance materials cost
water cost
Tdac = total direct annual costs (operating costs)
OH = overhead
adm - administrative cost
Pt « property taxes
In = insurance
+ CRC = capital recovery cost
Tiac * total indirect annual costs
* total annual costs
Tac » Tdac + Tiac
A-13
-------
ESP (Electrostatic Precipitator)
INPUT PARAMETERS
ORGANIC PARTICULATE ONLY
Emission Stream Input Parameters:
Maximum Flow Rate (scfm)
Stream Temperature (deg F)
* Moisture Content (X)
* Mean Particle Diameter (Ug)
Participate Content (gr/scf)
Drift Velocity (ESPs only, ft/s)
S03 Concentration (ppmv)
HAP Input Parameters:
Inlet HAP Concentration (ppmv or X)
Molecular Weight (Ib/lb mole)
Specific Heat Equation Constant A
Specific Heat Equation Constant B
Specific Heat Equation Constant C
Antoine Equation Constant A
Antoine Equation Constant B
Antoine Equation Constant C
Heat Vaporization (BTU/lb mole)
Design Related Input Parameters:
Control Efficiency (X)
Liquid Rate (gals/min)
Fluid Head (ft of water)
Cost Related Input Parameters:
ESP Type
Nozzles? (Y/N)
Hopper Auxiliary? (Y/N)
Weather Enclosure? (Y/N)
Structure Support? (Y/N)
Insulation? (Y/N)
Material of Construction
Site Preparation Cost ($)
Building Cost ($)
Cost of Cyclone ($)
Duct Cost (S/linear ft)
Length of Duct (ft)
Cost of Fans and Motors ($)
Motor Efficiency (%)
Damper Cost ($)
Stack Cost ($)
Total Pressure Drop (in H20)
Average Equipment Life (yr)
Operator Labor Requirements (hrs/shift)
Maintenance Labor Requirements (hrs/shift)
Operator Labor Wage ($/hr)
Maintenance Labor Wage (S/hr)
Operating Hours (hrs/yr)
Interest Rate (X)
Waste Disposal Cost Factor ($/ton)
HAP Data
Manual Type Len
Fieldname Range Values (default)
Oe
Te
Partcon
Ud
S03
HAPcon
RE
01
Z
N
N
N
N
N
N
N
F
F
F
F
F
F
F
F
F
N
F
F
8
8
5.1
8.3
8.3
8.3
8.3
8.1
8.1
8.5
8.5
8.5
8.5
8.5
8.5
8.1
6.2
8.7
8.7
flow rate
temp"
moisture
diameter
part_cont
velocity
so3_conc
hap_conc
mw
cpa
cpb
cpc
ant a
antb
ante
hvap
contrl_eff
liq_rate
fluid head
0 - 100 (99)
Dtyp
C
7 esp_type (PWESPB),PWESPE,FPESPB,
FPESPE , TSPESP , TSBSESP . WESP ,
C
C
C
C
C
spc
bldg
Pcyc
Pfan
nm
Pdamp
Pstack
P
n
olr
mlr
olwr
mlur
HRS
i
Wdcf
C
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
*
TESP
1 nozzles Y,(N) for PWESPB.FPESPB
1 hopper aux Y.(N) for PWESPB.FPESPB
1 wthr encl Y,(N) for PWESPB.FPESPB
1 stnfsupp Y,(N) for PWESPB.FPESPB
1 insulation Y,(N) for PWESPB.FPESPB
1 mat_const ** 0 - 6 (0)
8 site_cost
8 bldg~cost
8 eye cost
8.2 duct cost
8.1 len_duct
8 fan cost
5.1 motor_eff (65)
8 dampers
8 stack cost
8.1 pres drop 0 - 80 (5)
8.1 eqpt_life (20)
8.1 olabor_req (0.5)
8.1 mlabor req (0.5)
8.2 olaborwage (12.96)
8.2 mlaborwage (14.26)
8 op_hrs_yr (6000)
8.2 inl_rate (10)
8 disp_fact (200)
only
only
only
only
only
A-19
-------
** Key for ESP TYPE
PWESPB
PUESPE
FPESPB
FPESPE
TSPESP
TSBSESP
WESP
TESP
Plate Wire ESP, Basic
Plate Uire ESP, Enhanced
Flat Plate ESP, Basic
Flat Plate ESP, Enhanced
Two Stage Packaged ESP
Two Stage Basic System ESP
Wet ESP
Tubular ESP
** Key for MATERIAL OF CONSTRUCTION
Carbon Steel
304 Stainless Steel
316 Stainless Steel
Carpenter 20 CB-20
HoneI - 400
Nickel - 200
Titanium
MESSAGES TO USER
NONE
INTERMEDIATE CALCULATED RESULTS
Qea = actual flow rate
SCA = specific collection area
Ap = overall collection area
CAPITAL COSTS
Spc * site preparation
Bldg = building cost
PEC = purchased equipment cost
+ DC = direct installation costs
Tdc = total direct costs
+ Tic = total indirect costs
Tec = total capital costs
OPERATING COSTS
AEC = electricity cost
Olc = labor
Svc = supervisory cost
Mlc = maintenance labor cost
Mtc = maintenance materials cost
Wdc = waste disposal cost
CS03 = S03 cost
Wtcst - water treatment cost
+ West = water cost
Tdac = total direct annual costs (operating costs)
OH = overhead
adm = administrative cost
Pt = property taxes
In = insurance
+ CRC = capital recovery cost
Tiac = total indirect annual costs
* total annual costs
Tac = Tdac + Tiac
A-20
-------
APPENDIX B
COSTING METHODOLOGY
The following is a discussion of the methodology used to develop costs for controlling emissions of
hazardous air pollutants or HAPs. The approach and cost data are those used in the EPA Manual, Control
Technologies for Hazardous Air Pollutants (June 1991)(EPA 625/6-91/014). The possible control devices include
thermal incinerators, catalytic incinerators, flares, carbon adsorbers, packed column scrubbers, condensers,
fabric filters, venturi scrubbers, and ESPs. AH of the default costs in HAP-PRO are based on 1988 dollars.
TOTAL CAPITAL INVESTMENT
The total capital investment can be broken down into the direct and indirect costs shown below:
Direct Capital Costs:
Control Device
Auxiliary Equipment
Instrumentation and Controls
Taxes
Freight Charges
Direct Installation Costs:
Site Preparation
Foundation and Supports
Erection and Handling
Electrical
Piping
Insulation
Painting
Indirect Capital Costs:
Engineering and Supervision
Construction and Field Expenses
Construction Fee
Start-Up
Performance Test
Model Study
3-1
-------
ANNUAL OPERATING COSTS
The annual operating costs are also broken down into direct and indirect costs:
Direct Operating Costs:
Utilities
Natural Gas
Electricity
Steam
Water
Operating Labor and Maintenance
Operating Labor
Supervisory Labor
Maintenance Labor
Maintenance Materials
Replacement Parts
Replacement Labor
Indirect Operating Costs:
Overhead
Property Tax
Insurance
Administrative
Capital Recovery
Summing the direct and indirect operating costs yields the total annualized operating cost. The net annualized
cost is determined by substracting the solvent recovery credit, where it applies.
3-2
-------
TECHNICAL REPORT DATA
(Please read Instructions on the reverse before completing.)
1 REPORT NO 2.
EPA-453/B-94-038
4 TITLE AND SUBTITLE
HAP-PRO User's Manual, Version 1.2
7 AJTHOR(S)
Joseph E. Steigerwald
9 PERFORMING ORGANIZATION NAME AND ADDRESS
Control Technology Center (CTC)
Emission Standard Division, MD-13
U.S. EPA
Research Triangle Park, NC 27711
12 SPONSORING AGENCY NAME AND ADDRESS
Emission Standard Division, MD-13
Office of Air Quality Planning and Standards, U.S. EPA
Research Txiangle Pajik, NC 27711
3 RECIPIENTS ACCESSION NO
S REPORT DATE
May, 1994
6 PERFORMING ORGANIZATION CODE
8 PERFORMING ORGANIZATION REPORT NO
10 PROGRAM ELEMENT NO
11 CONTRACT/GRANT NO
68-D1-0116
13 TYPE OF REPORT AND PERiOD COVERED
Final
14 SPONSORING AGENCY CODE
15 SUPPLEMENTARY NOTES
16 ABSTRACT
The primary purpose of the Hazardous Air Pollutant I
permit engineers in reviewing applications for control o
the capital and annual costs for up to six different vol<
and three participate control devices, including selectee
Calculations used by the program mirror those presented
Technologies for Hazardous Air Toxics (June 1991) (EPA-62!
purpose of HAP-PRO is to generate reports that list all 1
specified pollutant in thoir emiacion ctrcam(c or 2) at
stream (e.g., organic or inorganic vapors and particular
Version 1.2 includes the addition of an expert revi«
thermal incinerators, catalytic incinerators, and carbon
gram will review the design results generated, make recor
allow for design sensitivities to be easily evaluated.
3rogram (HAP-PRO) is to atii^t
E air toxics by calculating
atile organic compound (vOc.i
i engineering parameters .
.n the EPA Handbook, Control
5/6-91/014) . A secondaiy
Facilities containirui 1} n
.specified typo of eniift.'iuii
ss) .
sw system for the desian of
adsorber systems. The pro-
nmendations for changes, and
17 • KEY WORDS AND DOCUMENT ANALYSIS
1
4
a DESCRIPTORS b iOEflTieiERS/OPEN BJDEiD "ESMS c .,:-••, , • > .. ;
i
Hazardous Air Pollutants Air Pollution
Tontrol Technology Canter Control j
Air Pollution Control Equipment Design
•.
i
1
i
i
4
Avaliable f rnm
Un c 1 ac o i f i c; "I
EPA Form 2220-1 (R«v 4-77) PREVIOUS EDITION 'S OBSOLETE
------- |