United States
Environmental Protection
Agency
Water Engineering Research
Laboratory
Cincinnati OH 45268
 Research and Development
EPA/600/S2-86/007  May 1986
Project  Summary
Computer Assisted  Preliminary
Design  for  Drinking  Water
Treatment  Process  Systems
Robert Smith
  A  computer program  known  as
 WATE R MAI D was developed for use in
 estimating the performance and costs
 of existing and proposed drinking water
 treatment systems. Design procedures
 and  cost-estimating relationships for
 25 individual drinking water treatment
 processes are contained within the com-
 puter model. The  unit processes were
 selected on the basis of their applica-
 bility to the removal of contaminants
 included in the National Interim Primary
 Drinking  Water Regulations or to the
 treatment and disposal of sludges and
 brines  produced  by these treatment
 processes.
  This Project Summary was developed
 by EPA's Water Engineering Research
 Laboratory,  Cincinnati. OH, to  an-
 nounce key  findings of the research
 project that is fully documented in a
 separate report of the same title (see
 Project Report ordering information at
 back).

 Introduction
  Estimating the performance efficiency
 and cost of water  supply systems is of
 considerable  interest to Federal, State,
 and  local agencies, as well as to con-
 sulting  engineers and planners. The
 computer program developed as  part of
 this project can be used to calculate the
 expected contaminant removal perform-
 ance and associated construction and
• operation/maintenance costs of drinking
 water treatment systems consisting of
 various unit treatment  processes ar-
 ranged  in multiple configurations. The
 technology used in sizing unit processes,
 estimating removal efficiencies, and de-
 termining treatment cost is the best that
is known to be currently available for
preliminary design. Since the technology
for each process is contained in individual
subroutines of the computer program,
improving and updating the technology
as it becomes available is easily accom-
plished. The structure of the program
allows the inclusion of additional unit
process models if desired. The final report
for this project also serves as a user's
guide for the computer program.

Scope
  The program name is WATER MAID,
with MAID being an acronym for micro-
computer  assisted interactive  design.
WATER MAID consists of a number of
support subprograms and a design/cost
subprogram for each of 25 unit treatment
processes.
  The user must provide the influent
concentrations or values for a list of 55
contaminants and other parameters that
characterize the raw water stream enter-
process is also displayed after each unit
processes to be used, which are arranged
in a specific flow diagram. The program
then  computes one or more effluent
stream vectors and cost estimates for
each  process based  on  design  input
decisions supplied by the user. WATER
MAID is  an interactive program, and
design decision parameters are entered
from the computer keyboard in response
to screen prompts.
  The following unit processes are in-
cluded in WATER MAID:

  1.  Sludge drying beds
 2.  Basin air stripping
 3.  Sludge centrifugation
 4.  Filtration

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  5.  Flocculation
  6.  Sludge filter pressing
  7.  Finished water pumping
  8.  Granular carbon adsorption
  9.  Ion exchange
 10.  Disinfection with chlorine
 11.  Sludge lagoons
 12.  Land disposal of sludge
 13.  Lime softening
 14.  Stream mixer
 15.  Presedimentation
 16.  Lime sludge recalcination
 17.  Rapid mixing (chemical addition)
 18.  Reverse osmosis
 19.  Raw water pumping
 20.  Sedimentation
 21.  Stream splitter
 22.  Clearwell storage
 23.  Sludge gravity thickening
 24.  Tower air stripping
 25.  Sludge vacuum filtration


  The following  water  parameters  and
contaminants are included in the stream
vector  (trihalomethane concentrations
are in units of fjg/L; all other concen-
trations are in mg/L unless otherwise
specified):

  1.  Design plant flow rate, mgd
  2.  Water temperature, °C
  3.  pH
  4.  Turbidity, ntu
  5.  Color, pcu
  6.  Coliform organisms, #/100 mL
  7.  Total dissolved solids
  8.  Total suspended solids
  9.  Volatile suspended solids
 10.  Carbonate alkalinity
 11.  Noncarbonate alkalinity
 12.  Calcium ion
 13.  Magnesium ion
 14.  Sodium ion
 15.  Copper
 16.  Ferrous ion
 17.  Ferric ion
 18.  Bivalent manganese
 19.  Quadravalent manganese
 20.  Chloride
 21.  Sulfate  ion
 22.  Nitrate ion
 23.  Total organic carbon
 24.  Nonpurgeable organic carbon
 25.  Pentavalent arsenic
 26.  Trivalent arsenic
 27.  Barium
 28.  Cadmium
 29.  Hexavalent chromium
 30.  Trivalent chromium
 31.  Lead
 32.  Mercury
 33.  Organic mercury
 34.  Quadravalent selenium
 35.  Hexavalent selenium
 36.  Silver
 37.  Fluoride
 38.  Endrin
 39.  Lindane
 40.  Toxaphene
 41.  2,4-D
 42.  Silvex
 43.  Methoxychlor
 44.  Gross alpha particle, pCi/L
 45.  Radium-226, pCi/L
 46.  Radium-228, pCi/L
 47.  THM formation precursors
 48.  CHCI3(THM)
 49.  CHBrClz(THM)
 50.  CHBr2CI (THM)
 51.  CHBr3(THM)
 52.  Aluminum hydroxide
 53.  Ferric hydroxide
 54.  Calcium carbonate
 55.  Magnesium hydroxide
Purposes and Objectives
  WATER MAID was developed to provide
an efficient, interactive process design
tool for consulting engineers, students,
etc. The primary purpose is to evaluate
any proposed system of drinking water
treatment processes  with respect to
treatment effectiveness and cost with a
minimum of  engineering  effort.  Tech-
nology used in the development of indi-
vidual process models is consistent with
the state of the art. However, in many
cases, the need for additional research is
clear.  Updating  the technology  when
improved performance, cost, and design
information becomes available can be
done by the user.
  Cost estimating data  used in WATER
MAID  came from technical  literature,
equipment  manufacturer's information,
previous  EPA research  projects,  etc.
Treatment plant capacity limits for these
data have been set at  1 to 200 mgd. A
secondary purpose of WATER MAID is to
provide a  more flexible, preliminary, cost-
estimating  tool than that provided by
graphical or tabular cost data.  Cost-esti-
mating procedures or data  bases  are
often presented at a number of specific
design parameter levels such as pumping
heads  or hauling distances for sludge,
thus limiting their general applicability.
When  a  cost-estimating  algorithm  is
known, it can be used in WATER MAID in
place of mathematical representations of
tabular data, thus providing more accu-
rate cost  estimates. Some of the design
procedures used  in the  program  are
limited by the availability of cost infor-
mation.
Approach to Program
Development
  WATER MAID was written in the BASI
computer language for use on the IBM P
microcomputer. Because of system men
ory requirements,  it was necessary  I
store the program on two floppy disks.
  The general philosophy used in deve
oping WATER MAID wastoallowthe usi
to input every possible design decision, 1
display the results  of each design  con
putation as it is made, and to inform th
user when design decisions are made t
the program. The  user  is  given th
opportunity  to  change the raw wati
stream vector or to change any of the co
variables or chemical prices when a ne
case is initiated. Recycling capability
provided. The raw  water  stream vect<
and process flow diagram are stored ar
can be used in the next case if desire
Stream vectors for  influent and effluei
streams are displayed after each proces
computation. A cost report for  eac
processs is also displayed after each ur
process computation. An overall cost ar
parameter summary report is display*
after each case. Design flow is used
compute construction  cost and buildir
energy requirements, and operating flo
is  used to calculate operation/maint
nance costs. The user  may also delete
unit process  from  the flow diagram
replace  any unit process with anoth
after each  process computation.  Th
allows  the user to consider alternate
processes without  rerunning the pr
gram.
Conclusions
  WATER MAID represents a matherm
ical modeling effort that is a significa
improvement on the  hand calculate
method of process design still commor
used today.  The principal deterrents
better  process  design  are  usually tl
manual effort required in computing t
expected performance and cost of alt*
native designs and the labor required
accumulate and correlate the lar
amount of experimental process desi
performance data that is often availab
The computer model can minimize t
computational work required for exami
ing alternative  designs, and  assumi
that the model has been correctly dev
oped, it will reflect the best experimen
and  scientific  information obtainab
WATER MAID provides the process t
signer with a tool for quantitatively sele
ing the most cost-effective system of u
processes to achieve any drinking wa

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treatment goal. The  use of computer
design techniques is a significant aid in
achieving better treatment at a minimum
cost.
  The full report was submitted in fulfill-
ment of Cooperative Agreement  No.
CR810267-01 between the University of
Central  Florida  and the  U.S. Environ-
mental Protection Agency.

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      Robert Smith is with the University of Central Florida. Orlando, FL 32816.
      Richard G. Eilers is the EPA Project Officer (see below).
      The complete report consists  of  two parts,  entitled "Computer Assisted
        Preliminary Design for Drinking Water Treatment Process Systems:"
        Paper copy only (Order No. PB 86-181 112/AS; Cost: $22.95}
        Software for Computer Program (2 diskettes) (Order No. PB 86-181 120'/AS;
          Cost: $90.00, this price includes the paper copy as  well)
      The above will be available only from: (cost subject to change)
              National Technical Information Service
              5285 Port Royal Road
              Springfield, VA 22161
              Telephone: 703-487-4650
      The EPA Project Officer can be contacted at:
              Water Engineering Research Laboratory
              U.S. Environmental Protection Agency
              Cincinnati, OH 45268
United States
Environmental Protection
Agency
Center for Environmental Research
Information
Cincinnati OH 45268
Official Business
Penalty for Private Use $300

EPA/600/S2-86/007
           0000329   PS

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