Unites States       Office cf Air Qua!.;/
Environmental Protecron  Planning and Standards
A^encv          Research Triangle P?rk NC 27711
—  ——	
                                                EPA-450/3-84-017
                                                Novemcer 1 934
                  Evaluation of
                  Emission Controls
                  For Hazardous Waste
                  I reatment, Storage,
                 And Disposal
                 Facilities
                    ENVIRONMENTAL PROTECTION
                       JAN 24 1335

                    LIBRARY
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                                 EPA-450/3-84-017
 Evaluation of Emission  Controls
for Hazardous Waste Treatment,
 Storage, and Disposal Facilities
                  Prepared bv

              Arthur D Little, Incorporated
            Under EPA Contract No. 68-01 -6~1 60
                  Prepared for:

           U.S. Environmental Protection Agency
         Office of Air Quality Planning and Standards
         Emission Standards and Engineering Division
         Research Triangle Park, North Carolina 27711

                 November 1984

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                                       DISCLAIMER

This report has been reviewed by the Off ice of Air Quality Planning and Standards, U S. Environmental
Protection Agency, and approved for publication as received from Arthur D. Little,  Incorporated.
Approval does not signify that  the contents necessarily  reflect the views and policies of the U.S.
Environmental Protection Agency, nor does mention of trade names or commercial products constitute
endorsement or recommendation  for use. Copies  of this  report are available  from the  National
Technical Information Services, 5285 Port Royal Road, Springfield, Virginia 22161

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                            TA3LZ OF  CONTENTS



                                                                  Page

I.   SUMMARY AND CONCLUSIONS                                       1-1

II.  INTRODUCTION                                                 II-1

     A.   Objective                                               II-l
     3.   Framework for the Analysis                              II-l
     C.   Hazardous Waste Treatment, Storage and Disposal         II-5
          Disposal Facility—Definitions and Descriptions

          1.   Landfills                                          II-5
          2.   Land Treatment                                     II-6
          3.   Surface Impoundments                               II-6
          4.   Storage and Treatment Tanks                        II-7

     D.   Controls/Definitions and Description                    II-7

          1. . Pretraatment Controls                              II-7
          2.   Design and Operating Practices                    II-3
          3.   In-Situ Controls                                  II-3
          4.   Post-Treatment Techniques                         II-S

          References                                             11-10

III.  CONTROLS FOR SURFACE IMPOUNDMENTS                          III-l

     A.   Surface Impoundment Description                       III-l

          1.   Definition                                       III-l
          2.   Types,  Construction  and Uses                      III-l
          3.   Operation                                        III-2

     3.   Emission Sources and Models                           III-7

          1.   General Description  of Factors  Affseeing         III-7
               Emissions
          2.   Emission Models                                  III-9
          3.   Parameters  That Control  Emissions                 111-16

     C.   Potential Controls                                    111-17

          1.   Introduction                                      I~~-i
          2.    Pretraatmer.t                                     III-I3
          3.    Design and  Operating Practices                   111-13
          4.    In-Situ Controls                                 111-23
          5.    Post-Traatment                                   111-32
                                n

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                             TABLE  OF CONTENTS
                                 (continued)

                                                                     Page

V.    LANDFILLS                                                      V-l

      A.    Landfill  Description                                     7-1
      B.    Emission  Sourcas and Models                              V-2

           1 .   General                                             V_2
           2.   Emission Models                                     V-3
           3.   Controlling Paranetars                              V-7

      C.    Controls                                                  V-7

           1 .   Introduction                                         V-7
           2.   Pre treatment                                        V-3
           3.   Design  and  Operating Practices                      V-8
           4.   In-Situ Controls                   .                 V-15
           5.   Post-Traatnent                                      7-16

      D.    Effectiveness                                  '          V-17

           I.   Introduction                                        V-17
           2.   Effectiveness                                        V-17
           3.   Costs                                                V-25
           4.   Cost-Effectiveness                                  V-28

      E.    Suszary                                                   V-2 9

      F.    References                                                7-30

TTT    T * TH  **^ T * "**XT^T^i' "" «  «^T-- -*-»*-*"-^^                                     »r-^  ^
v j. .   L-nJU  i. J.jlAi.lZ..i - r.-iu ^._ J-.-ii                                     V i— i.
     A.   Descripcion                                             71- 1
     3.   Emission Sourcas  and Models                            71-2

          1.    General                                            71-2
          2.    Eaission Models                                   71-2
          3.    Controlling  Parameters                            71-5

     C.   Controls                                                VI -6

          I .    Introduction                                       71-6
          2.    Pretraatsent                                       71-6
          3.    Operating Practices                                71-6
          4.    In-Situ Controls                                   71-7
          5.    Post -Treatment                                     71-7

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                      TABLE 0? CONTENTS
                         (continued)
                                                            Page
D.   Effectiveness                                          VI-8

     1.    Introduction                                      VI-8
     2.    Emissions Reduction and Effectiveness             VI-3
     3.    Costs                                             VI-12
     4.    Cost Effectiveness                                VI-12

E.   References                                             VI-I3

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                      ^
                             LIST OF TABLES



 TABLE  NO.                                                         page

   1-1      RANGES  Or  EMISSION CONTROL EFFECTIVENESS                 1-3

  II-l      EMISSIONS  FROM HAZARDOUS WASTE TREATMENT,  STORAGE      II-4
           AND  DISPOSAL FACILITIES

  II-2      PRETREATMENT PROCESSES AND COSTS                       II-9

 III-l      EVAPORATION  SUPPRESSION BY SHADES                      111-25

 III-2      SPHERE  REQUIREMENT PER UNIT AREA AND  VOLUME            111-29

 III-3      MASS TRANSFER COEFFICIENTS                            111-37

 III-4      TYPICAL VALUES  FOR WASTE PARAMETERS                    111-41

 in-5      SURFACE IMPOUNDMENT SIZES                              111-43

 III-5      SITE AND IMPOUNDMENT  PARAMETER  VALUES                  111-44

 III-7      "TYPICAL"  INDIVIDUAL  k VALUES FOR SURFACE              111-45
           IMPOUNDMENTS  WITHOUT  CONTROLS

 III-S     MASS TRANSFER COEFFICIENTS  (lb-aol/f-2-hr) FOR         111-46
           SURFACE IMPOUNDMENTS  WITHOUT CONTROLS

 III-9      EMISSIONS  FROM  SURFACE IMPOUNDMENTS WITHOUT            111-47
           CONTROLS (Ib-aoi/hr)

 III-LO    CONTROLLABLE  PARAMETERS  TO  REDUCE EMISSION RATES

 III—1 1    EMISSIONS  REDUCTIONS  .-ND EF"-"rCI"r>rC~'rc O7 TN— "	
          CONTROLS

          UNIT MATERIAL COSTS FOR  SURFACE IMPOUNDMENT            111-57
          EMISSION REDUCTION  IN-3ITU TECHNOLOGIES
           ("Dollars per  Square Foot,  Su-zaer 1984 Dollars)

          ANNUAL COSTS  FOR SURFACE IMPOUNDMENT CONTROLS,         III-39
          5/YR (SuEnsr  1984 Dollars)

          RELATIVE INSTALLATION AND OPERATION/MAINTENANCE        111-50
          COSTS

111-15     CAPITAL COSTS FOR COLLECTION SYSTEM FOR POST-          111-63
          TREATMENT  'Su=;er 1934 Dollars)

          COMPARATIVE COST-EFFECTIVENESS  FOR  IN-SITU             111-65

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                            LIST OF TABLES
                               (continued)


TABLE NO.                                                        Page

 IV-1     RELATIONSHIPS DESCRIBING EMISSION LOSSES IN TANKS      IV-4

 IV-2     PARAMETERS FOR TANK EMISSION RELATIONSHIPS             IV-5

 IV-3     PARAMETER VALUES FOR TANKS                  -           IV-12

 IV-4     EMISSIONS REDUCTIONS AND EFFICIENCIES OF CONTROLS      IV-13
          IN TANKS

 IV-5     TOTAL COSTS AND ANNUALIZED COSTS FOR CONTROLS          IV-16
          (Sumner 1984 Dollars)

 IV-6     COMPARATIVE COST-EFFECTIVENESS FOR TANK IN-SITU        IV-18
          CONTROLS

  V-l     RANKING OF USCS SOIL TYPES ACCORDING TO PERFORMANCE     V-10
          OF COVER FUNCTION

  7-2     RELATIVE DIFFTSI7ITY AS A FUNCTION OF SOIL POROSITY     V-12

  V-3     UNIT EMISSIONS THROUGH 12-INCH SOIL COVERS FOR          V-18
          SOILS OF DIFFERENT DRY POROSITY

  V-<1     UNIT EMISSIONS THROUGH MEMBRANE CAPS                    V-21

  V-5     ANNUAL EMISSIONS                                        V-24

  v-6     ESTIMATED UNIT COSTS FOR SOME COVER LAYERS              v-26

  V-7     POST-TREATMENT COLLECTION SYSTEM COST ESTIMATES    '     V-27

 VI-I     ANNUAL LOSSES FROM 1 ACRE OF LAND TREATMENT            VI-10
                                 VI 1 1

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                               LIST OF FIGURES

FIGURE NO.                                                        ?ase

 H-1          GENERALIZED  FLOW OF VOLATILE EMISSIONS            H-l

III-l          CROSS-SECTION-SURFACE IMPOUNDMENT                III-3

m-2          SURFACE  IMPOUNDMENT CLOSURE KEY STEPS            nr-5

III-3          EFFECT OF TEMPERATURE ON  EMISSIONS               111-51
               (50th Parcantiie Size Icpoundnent)

III-4          EFFECT OF WIND  SPEED  ON EMISSIONS                111-52
               (50th Parcentiie Size Int
-II-5          EFFECT OF GEOMETRY CHANGE ON EMISSIONS            111-53
               (50th Parcsr.tila Size Impoundment')

III-6          COST-EFFECTIVENESS OF IN-SITU SURFACE             111-66
               IMPOUNDMENT CONTROLS

HI-"          COST -EFFECTIVENESS OF SURFACE IMPCUNDMZNT         III-67
               CONTROLS VERSUS THROUGHPUT
               (50th Percsntila Size)

III-8          CGST-EFFECTIVE:iES3 OF SURFACE IMPOUNDMENT         111-53
               CONTROLS VERSUS REDUCTION

 ''<"-!          EFFICIE:-rCIES OF IN-SITU CONTROLS FOR TANKS         IV- li

 ~-2          COMPARATIVE COST-EFFZCTIVZ:TZ33 OF IN-3ITU          17-19
               CONTROLS FOR TA^S
 I""-3           COST-EFFECTIVENESS OF CONTROLS ON TANKS            17-20
               VERSUS THROUGHPUT

 -V—           CQST-EFFECTIVE:-rE33 OF CONTROLS ON TA.\1-o            IV-2I
               VERSUS REDUCTION

  V-I           RELATIVE DIFFJSIVirr IN SOIL COVERS                V-ll

  V-2           EXAMPLE STANDARD COMPACTION CURVES FOR             V-13
               VARIOUS SOIL TYPES

  V-3           TYPICAL LAYERED COVER SYSTEMS                      v-^2

  V-«l           UNIT EMISSIONS THROUGH L2"  SOIL COVER OVER         T'~-19
               A  LANDFILL

               PERCENT OF VCLATILE5 LOST TO ATMOSPHERE           ?I-S

               REDUCTION EFF.Cir.ICY FOR SUBSURFACE INJECTION

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1                                    I.  SUMMARY AND CONCLUSIONS
                   Volatile  emissions  from hazardous  waste  treatment,  storage  and
              disposal  facilities  (TSDFs)  represent   a major  source  of  organic
              contaminants  entering  the atmosphere.   The  emissions contain  a wide
              range  of  organic  constituents,   which   contribute   to  both  oxidant
              generation  and   also   to  exposure  to   potentially  hazardous  air
              pollutants.  Previous studies prepared for EPA estimate that volatile
              emissions  from  surface  impoundments,  storage  and   treatment  tanks,
              landfills  and  land- treatment  facilities range from 1.6  to  about  5
              million  metric tons per  year.   The  lower estimate  represents  about
              one-third  of  emissions of  some  54 organic chemicals  from  all sources
              including  industry  and transportation.   These  54  chemicals  are  the
              most volatile  and toxic compounds  appearing  in wastes regulated under
              RCRA.

                   Surface   impoundments  are  the  largest   source  of   emissions,
|             providing  about  half of  the total.  Treatment and storage  tanks make
•              up  about one-third  of  the total, with  treatment tanks  contributing
              about 50 times as much as  storage  tanks.   Landfills  produce  about  12%
              and land treatment adds the remainder, about 3%.

                   TSDFs,  particularly  offsite  commercial   operations,   generally
              treat complex  mixtures of  wastes.   The wastes deposited in  landfills
              historically have included a wide  range  of  solvents,  PC3s,  industrial
I             wastes,   sludges   and  still  bottoms,  etc.   The  resultant  emissions
\             integrate  volatile  species  from   all  of  the  wastes  present  in  the
|             landfill.  Impoundments at large industrial facilities often  serve  the
2             entire complex,  receiving  wastes  of  many different  types.   Treatment
1             tanks and land-treatment  facilities,  on  the other hand, are more oftan
^             dedicated to a narrower mix of wastes.
a
i                  The  principal   focus   of   the current  Federal  ar.d  state TSDF
!             regulatory  program  has   been   on  the   prevention   of   groundwater
3             contamination during and  after the  active life  of disposal  facilities,
=i             the prevention of exposure from atmospheric emissions  of the  products
g             of  incineration,  and   the  prevention   of  accidental  exposures   in
3f             general.    There  has been  little  emphasis on  prevention of  exposure
3             from direct emissions of volatile  compounds in  the wastes.  This  study
5|.            examines  the  availability  of  controls   for  four principal  types  of
2             TSDFs and evaluates  the cost and effectiveness  of each.
|
3,                 Four different  classes of controls are examined.   These  are:

*i                  o    pretreatment
                   o    design  and operating practices
                   o    in-situ controls
                   o    nost-treatment  techniaues
                                               1-1

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 Pratreatment includes  technical controls and  administrative measures
 (bans)  that,  in essence,  prevent volatile  vastas  from  reaching the
 TSDF in the first place.  These types of controls obviously reduce the
 quantity of organics that  will ultimately be  emitted  fron TSDFs, and
 also reduce the rate of loss since the processes that control emission
 are proportional to waste  concentration.  The  volatile materials that
 have been removed must  be subsequently treated  or disposed, however.

      Design and operating practices and in-situ  techniques can  reduce
 the rate of loss from the facility.   These controls  include approaches
 such as floating covers for impoundments and  tanks,  improved temporary
 and permanent  cover design and moisture control  for'  landfills,  and
 subsurface  injection at  landfills.  The  use  of wind screens  to  lower
 wind speed  over impoundments in order  to  reduce mass  transfer from the
 surface also falls  into this class.

      Finally,   post-treatment  can  be   used   to  catch  emissions  that
 escape  even if  other   approaches are used.   This  type  of  system
 involves some  sort  of   collection system coupled  with' 'a process to
 remove or  destroy  the  volatile  components.   Air-inflated "structures
 have been installed at  several locations including an  aerated surface
 impoundment  (about  0.4  acra).   This   system  includes  a   carbon
 adsorption  unit designed to remove the volatilas  and recycle them to
 the aerated impoundment where  biological  degradation ultimately  will
 destroy the wastes.  Thermal  incinerators could  be used instead of
 adsorption  system to destroy the volatile compounds.

     The effectiveness   of   the  four  types   of  controls  ranges  from
 moderately  effective to very high, potentially 99* or above  (Sae Table
 !-!).    The  values  in   Table   I-L have been   generated   frc=  first
 principles  or  have  been taken  from  experience  at  raiatad  tvpes of
 facilities.   The validity  at  real hazardous  waste TSDFs  is unknown.
 The  values  shown  may  be  overly  optimistic  or,  in   some  cases,
 conservative.   Substantial  experimental  work   is  needed,  as  noted
 further  below,  co verify the estimates  developed and praser.tad herein.

     Pratraatment and posc-traatment can  achieve removal (and in  seme
 cases  destruction)   efficiencies  of  90".    Wasess  removed  but  not
 destroyed must  be  handled  in  additional  steps to pravant emissions
 from  occurring.  Recycling  as  feedstocks, reclaimed  solvents,  etc.
 represents essentially complete control.  The  figures  for oretraatment
 and  post-treatment  ara  quite  reliable  as  the  treatment technologies
have  been  demonstrated  on  process  straams  comparable to  hazardous
wastes.   Inflated covers  as  large  as  six acras  have bean  shown  to be
 practical.   Systems  of  this siza would fit most  existing  facilities.
Future  facilities  could be  designed with  operating units  compatible
with the largest cover then available.

     Pretreatment works  best on wastes  of reasonably  well-defined  and
constant  properties.  The  most  likely  opportunities  ara  at  on-sita
 industrial  plants   and  for  solvent recovery.   On  the  other  hand,
pratraatment may not fit  well  with :ha camplas wastes  going  off-site

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                          TABLE  1-1
                 OF  EMISSION CONTROL EFFECTIVENESS
Pretreatment      > 90%  (removal)

Post-Treatment    > 90%  (removal)

Operating Practices and  In-Situ Controls (rate reduction)

     Surface Impoundments

          Rafts/Spheres           '      80 - 90%
          Wind Screens                  10 - 15%

     Tanks (relative  to open tanks)

          Rafts/Spheres                 80%
          Fixed Roof                     90%
          Floating Roof (axtamsl)       90%
          Floating Roof (internal)     >  95%

     Landfills

          Improved Cover  Practices     >  90%

     Land  Treatment

          Subsurface Injection           20  - 90%


Source:  Arthur D. Little, Inc.

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 to conmercial TSDFs.  The volume  and  composition  of  the wastes may be
 so variable  chat  pretreatment would noc be  technically feasible, or,
 if feasible, would  cost  more  than the figures used in' this  and other
 studies.

     ^In-situ controls and improved design, and  operating practices are
 promising.   The values shown  in the table are, as noted above,  based
 on theoretical  principles  as  there are  little or no  data  extant  on
 emission  controls  at  these  types  of  facilities.'   Several  of  the
 in-situ technologies  (shades, wind  screens,   for  example)  have  been
 used in similar,  but  distinctly different settings.   The validity  of
 these   techniques  at  hazardous  waste TSDFs   should  be  established.
 Using   improved  soils  and controlling   moisture in   temporary  and
 permanent  cavers  at landfills  can,  according to  the  estimates  made
 below,  reduce  emissions  essentially  to  zero.   In practice, however,
 there  will be  limitations  to  achieving such efficiencies.  There  are
 no  data  available   to   determine  how  closely   this   limit   can  be
 approached.

     Pretreatment  appears to be  a cost effective control relative  to
 the other  types of  controls particularly  if  only small quantities  of
 volatiles  are present in  the wastes.  Pretreatment costs according  to
 another EPA  study  are about  $2-4,000 per megagram  (Mg)($l-2 per pound)
 of volatiles,   fSpivey   et  al.,   1984).   Post-treatment  costs  are
 considerably more.   Tae  treatment  portion  alone  ranges  from about
 $11,000 per^ megagram  removed  ($5  per  pound)  upwards.   The  lower
 figures are  for catalytic incineration  or regenerative adsorption.   If
 the recovered wastes have  market or  fuel value  the costs 'will drop
 substantially.    Thermal   incineration  without   heat   recovery  and
 non-regenerative   carbon  adsorption   cost   upwards  of  333,000  per
 megagran (315  per  pound)  of volatilas  rsaoved.  The collection svstem
 will add to  this  figure,  but for large facilities the added cost'will
 be incremental  to  the treatment case on a pound removed basis.

     The cost  effectiveness of in-situ approaches  can  ootanciallv be
    very  high  for  those  operating   practices  that  require  little
 additional  labor  or equipment.   Moisture  control at  landfills  or
 subsurface injection at  land treatment facilities  are  gccd  examples'
 The added  cost  of these practices is very small relative  co  cha'cost
 of  conventional practices,  so  that the control  potentially achievable
 per  dollar  would  be  high.    On  the  other" hand,   the   absolute
 effectiveness that is achievable in practice  may not attain acceptable
 levels.  In  these cases,  pre- or  post-treatment  may be  used "as  an
 adjunct.

     At  the  conclusion  of the  analysis there  remain many  unanswered
questions generally  as  a  result of the lack  of good  data  character-
izing  emissions or  the  performance of controls"at  hazardous vaste
TSDFs.    It   is  recommended  that  field and  laboratory  programs be
carried out  to  obtain  such  data.   In particular,  data 'describing  the
effectiveness of cover practices  at landfills;  injection,  cultivation,

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and  application density  practices  at  land-treatment  facilities; and
rafts, floating spheres and covers at impoundments and tanks should be
developed.

     The  estimates  developed  in  this  report  assume no  losses occur
through  degradative  processes  in  the  TSDF  or  equivalent!/  that
volatilization  and  reaction  are  uncoupled.   This  assumption  is not
valid  in  reality at  these  facilities.   Reducing emission  losses may
change the overall  degradative  efficiency  per  pound  of volatile waste
entering  the  system.   The  direction  of such  change is not  clear  at
this time.  Studies examining this coupling should be carried out both
in the laboratory and field and also through theoretical modeling.
Reference

Spivey,  J.J.,  et  al.,   Preliminary  Assessment  of  Hazardous  Waste
Pretreatment as an Air Pollution Control Technique.   Research Triangle
Institute for the USEPA (February 1984).

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                   A.   Objective
  5

  3
i
|
•
i
1






1
                             wastes.    For  each
                  management facility,  sources  of
                  and  controls  representing  di4e^ent
                  compared.   The evaluation  
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                                                                                                                                           X
                                                                                           Covers
                                                                                           Roots
                                                                                           Wotting Down
                                                                                           Raits
                                                                                           Wimlicreens
    Stripping
    AtJsoiption
    Condensation
                                                    Hansler £ llandlinu
                                                                                        I   Dust toy   \
                                                                                    •  Design & Opoiating
                                                                                       ('radices
                                                                                    •  in situ Treatment
•  Post Tifutment
                                      t;;
                                      i./
Sonri:«:   Artlmr  0. |,|tt le,  In,
                                                        TSOFs

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                                               , »'. rV*-'^l .-^••J.--'.;,.-
   once the  wastes  have  left  the  process boundary and move either offsite
   £C-M,V     na2ard°US  WaSte  di*P°^l   portions  of  the  generator's
                 to the other processes, and are not considered further
  in  eh  *  study.  Waste  piles,  containers,  and  transfer  and h
                      °miC-ad>   GCA haS  MCiM"d the relative
                                             Table II~1
  '083)   Ts
  soec fic?Iv^nSSCi0nh C£l7laCi°n  is  based °n sone 54 chemicals listed
  o? Ill voY;,-       hazardous waste regulations.   The total emissiors
  o. all volatile  organics  is  estimated  to be higher  as  is  ^D-'ad  by
  ov:rworh"/ascaheestr;i siven above-   surface ^nd-nt.  «pn
  over  hair   tne   total   emissions.    Treatment   tanks  rank
  contributing   about   one-third  of  the  estimated   emission"
                 ^ Small£SC          °f Che  "cities  indued.    he
                  e should be examined.                      "ons,  tk.e
 savpr?nCr01 °f  e"i3sions  from the TSDFs can be accoaDlished through
 several   means:   pretraatment   techniques,   design   and   operH^
 practices,   m-sicu   techniques,   and   oosc-crsaraenc   "ec
 Pretreatment controls are those administrative or technical' r
                 .                                  '          --
                 in caose treatment,  disposal,  and storaae faciliti
        ana  operating  practices  are  techniques wi=h±n  conc-ol  of
 aesigner ar.a .operator  that  can reduce  emissions  without <°^l-<
 d"^"!1' .S2nerally ?ri^^'  o^«ctivM.   In-situ  craamanVs
 oe. a«c as_ t.cnnologic means  ana  are  operating oractices  eao'cv
 '—!",_ anc as  a  part of the  TSDF,  that will reduce  emission "--
 t.iose  raciiities.   Finally,  post-treatment techniques ^ ^J

                                                                *
        a,e                                              .ras::
 a^oljhe^e      8  13FOS^:-0n  °' in-si"  creacaenc  technics  to  the


     To evaluate the effectiveness of emission control method*  < t 
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                               TABLE  II-l

                EMISSIONS FROM HAZARDOUS WASTE
                    STORAGE, AND DISPOSAL FACILITIES
      Facility TTB«                      Estimated Annual Emissions*
                                               *»
                                            C10J Metric Tons/Yr)

 Treatment Tanks
 Non-Aerated Surface lapoundaent - Storage          4?Q
 Non-Aerated Surfaca Impoundment - Treatment        310
 Landfill                                           19(J
 Non-Aerated Surface Iapound=ar.c - Disposal          66
 Aeratad Surfaca I-poundnent           '              g'
 Land  Applications         •                          4?
 Storage Tanks                                       1Q

      Total                                      1,635
  For 54 selecrad chenicals.
source:  3reton ec ai.. L983.
                                11-4

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  as  incineration,   then  such  an  administrative  control  can  be  ve in-
  effective.   If,  on the  other hand,  the  procedure  is  an alternative
  such as  extended  storage or  disposal in  a  surface  impoundment,  then
  a ban would not be so effective when  the  potential emissions from the
  entire chain of events is accounted for.

       As volatile materials move through the hazardous waste management
  process,  they must be  destroyed, accumulated, emitted or recycled to a
  prior  step   at each  stage.   This   report  examines  in  detail  the
  efrectiveness of design and operating practices  and  in-situ  treatment
  techniques,   and  also   the use  of  post-treatment  methods  to  reduce
  subsequent emissions.    A similar detailed  analysis of  pret-eatment
  methods is not  included.  The effectiveness of  pretreatment  controls
  has  been  the  subject of  a  study being  carried out at  Research Tr-angia
  Institute  for the EPA  (Spivey et  al.,  1934).  Results  of tha-  sf-dv
  have been  incorporated directly as a basis  to show  comparisons.

       The  studies  referenced  above approached  the  analysis  <=-om the
  perspective of the types of wastes, particularly the work of  Spivev,
  et al.,  (1984).  The approach  herein is different,  examining  controls
  from the  point of  view  of type  of facility.  The  choice of  control
  method  is  largely  dictated by  facility and environmental seefn*  not
  by waste  properties.   In  certain  cases,  however,   the  effectiveness
  depends on waste properties.  These cases are spelled out in the text.

      Effectiveness is measured primarily by degree of reduction of the
 £at£  ot emissions,  not  by  reduction  in  total  emissions over  lorg
 perioas of  time.  Many  controls  serve  only to  retard  this  rate  of
 emission;  for  example,  improved covers at  a  landfill.   Othe-s remo^
 the  volatile  materials  entirely,  for   example,  pretreatment   or  nost
 treatment,   although  the  wastes   removed   may  require   sub=e<-ue"C
 treatment  or  disposal.    Retarding  the  rate of  loss by volat'lizar'cn
 r-  tine   r,.  ,--  _0.
 possible to predict the "direction of the change, based on'present  -atl
 ana  tneory.  Mechanisms  leading co either an  increase o- de—>»se  -a-
 be  invoked.                                                     "    ~  "
c-   Hazardous  Tiaste   Treatment,   Storage  and  Disposal  :rac,••;-.•-,r	
     ^ecinitions and Descriptions  —^——~--	,—,	

     1.   Landfills

     Landfills are  disposal facilities  in which  hazardous wa.«fe« a—
placed in containers or in bulk form, covered over with soils and T^I
^iderinite^y   The  present  regulations  require that  free liauids must
be mixed with  a suitable bulking  agent.   Some state  regulations now
oan the disposal or certain  types  of  organic  liquids  enti--v   o<-he~
states   are   contemplating   similar bans.   ?re-RC?a  and  ear7" '?r?I
            permitted  the landfillin? of free  liquids.   Emissions from"

-------

                                                  t          .



  ulc^ziataiy  of  che  entire  landf^i    A  s-'-al*   -if

                                              '
                                       '       •
                                                                     -  20
            Land Treatmen
                                                                      «•
      Emissions   from  land  traacaenc   facil-'<--'aS  =--,-„

 volatilization  iron  che  wastas that have beer"-7—ad on  -h

 co  oeing  ir.corporacad  vichia che  COD  • avals'

 wascas  which have  basi a             '
                                 --.—i  -^  _„•••

 -leas, «u«l.                          •
 reach che surfaca.              "  '  "~~""~  ^."w
-------
----^•-'••^- ••=•--
               Surraca impoundments  can also be  aerated.   Aeration is  provided
          to ennance  oiological activity  within the  bodv of  the  impoundment"
          degrading_the  organic materials  contained.   The  princioal"mechanism
          ror emissions  remains  that of diffusion  at  the  surface!   The turbu-
          lence  created  by  the aeration  changes the  rate of diffusion at  the
              4.    Storage  and  Treatment  Tanks

              Treatment  and storage tanks come  in  a wide variety  of  sizes and

              Uv.     "• *"  -^ and CrSaCed  b°th in  °Pen Canks and ^ tanks
         with covers  ana roors.   In uncovered  tanks  the  mechanism of  loss  to

         !±at?°S??erVS  S-       C°  ^ iB SUrfaCe imP°u^ments.   Diffusion
         "om the liquid surrace to  the atmosphere  is  the  only  means of  esc*p-
         The details  or  dinusion  at  the surface,  like surface  impoundments',
         depend  on  wnetner  the  tank  is quiescent  or  is   being  mixed  bv  a
         speller.  The  mechanism for fixed  roof tanks is  primarily  the  s*~e
         mechanism.   Volatile materials diffuse  from the surface into the  head
         space  wove  the liquid,  and  then   in  general,  are released  to the
         atmospnere  thrcugn  some sort of vent.   Vents  are   necessary  in  ^ost
         storage   tanks  to  control  changes   in   pressure  due   to  ce-roeracu-e
         variations  and  volumetric  changes  due   to  filling   and  «mt,tvi--   Cr
         Pressure tanks  are  designed  to withstand  the  changes" of ' s^su^
         without  vents.  Mo losses  to  the atmosphere would take  D'UC- "»"-
         normal operations from  this type  of  tanks.
        n_,  ;"i0atin*  5oof   tfnks ,  commonly  used  to  store  bulk  petroleur
        or.aucts,  may be  used  for  the storage  of large  volumes of
        solvents.   In  these tanks a roof  floats  on the surface of  the
        and is  staoilized  by  means of  a seal along the circumference.   Lo
                                   laaka?s ac  che 3e^  ^d  bv  adherence  of
        3-   Controls/Definitions and .esc—'ot-c-

             L.    Pretraatment Controls

             Pretreatment  controls   include  administration   -rd  -~v---»
        measures.   Administrate  controls,  such  as  bans or  res't^c^ns"^
        the  disoosai  or  vo7at-"'a ma'-ar-fal =:  *i i-n^-n-r       -    01---	-^ di
           -,  •          -.1-°.'	-i^.wec_d_s  t.i ianariils,  surraca imooundr?"r*-s
          ^   •-,, ^raac~enc  Acuities have been  instituted bv  sev»-a'  «T""'
        ard  will be implemented  in  the future bv  the Federal  «4^"eV  "
        controls  have the  efface of  complete!,  elV-^afn-  "the -0V
        emissions  from the facility  in question.   In  evaluar^ %^J
        erractiveness  of  these  controls,  however,  the  U7-'»«»"*
        Treatment or disposal used must be  considered.

-------
        a?  *     «»«ols  include nethods  which separata  the volatile
            ?™     WaSCaS ^  either  reC7cle  the* back " the genera-
               ,  POCential  USers'  or des"°7  the potentially volatile
  include          §n   SUbse«UenC   tre.t«nt.    Separation   techniques
       o    Distillation
       o    Stripping
       o    Carbon Adsorption
       o    Solvent Extraction

  Each  of  these methods  can be used  to remove a fraction  of  the volatile
  materials  rrom  che  wasta straam.   Thg choice deoend      h particula,
  composition  or  the waste.    Once separated,  the volatile  fraction cln
  be  reused  or destroyed by  incineration with air  oxidation and other
  more  exotic  methods.   Some  emissions may  occur during t"e seoarat'n
  vou^d  hSlvTnC^?r°CaSS;  buCrth? Wil1 be less cha* e*« emissions that
    —        c-arraa it tne wastes  had Deen deoosiced or the Lard 
-------
     Wasta type
                                   TABLE II-2

                       PRETREATME7T  PROCESSES  AND COSTS
      Applicable
 Pretreatment process
     Example cost
   $/metric ton of
organic material re-
 moved or recovered
 Organic liquids

 Aqueous,  up to 20%
   organic

 Aqueous,  less than 2%
   organic
Sludge with organics
Some sludge in organic
  or aqueous stream
 Distillation

 Steam stripping
 Solvent extraction

 Steam stripping •
 Carbon adsorption
 Resin adsorption
 Air  stripping witY carbon
  adsorption
 Ozcnati on/radiolys i s
 Wet  oxidation
 Biological treatment

 Air  stripping with carbon
 adsorption
 Ozonation/radiolysis
 Wet oxidation
 Chemical oxidation
 Evaporation with carbon
 adsorption

Physical separation  (Wmetric
 ton  of wasta treated  for
 sludge removal)
          251

          151
           55

          151
        1,600
          310
        1,400

        1,300
        1,390
          63

        1,400

        1,800
        1,390
      91,000
         140
Source:  Spivey ec al, 1984.

-------
References




                                       -
                              11-10

-------
                  III.  CONTROLS FOR SURFACE IMPOUNDMENTS
  A.    Surface Impoundment Description

       1.    Definition

       Surface impoundment means a facility or part  of  a  facility which
  is  a natural topographic  depression,  man-made  excavation,  or  diked
  area  formed primarily of  earthen  materials  (although it may be  lined
  with  man-made materials),  which is designed  to  hold an accumulation of
  liquid wastes or wastes containing  free  liquids,  and which is not  an
  injection  well.    Examples  of  surface  impoundments  are  holding,
  storage,  settling,  and  aeration  pits,  ponds,  and  lagoons   (Fede-al
  Register,  May 19, 1980).   Exceptions  to  the above definition  include
  concrete-lined basins, which  are,  by definition, considered tanks.

       2.   Types,  Construction and  Uses

       As defined above, surface  impoundments may be  natural or mar-^ade
  depressions.   Acreages  range from less than an  acre to  hundreds of
  acres and depths  vary from  2  feet to as much as 30  feet below the land
  surrace  (EPA,  1982).    Impoundments are  generallv  built  above  the
  naturally   occurring  water  table.    Future   impoundments   handling
  hazardous wastes  will have  to be above  the water  table to  comply with
  federal and  state regulations.   Some may  be constructed on  the  land
  surrace using dikes  or  revetments.   Natural  topographical  features
  such  as valleys  or depressions  may  be  diked  on one or more  sides  to
 .orm  the   containment   area.   Dikes  may   also  be  required   fo-
 impoundments  in  areas  of high  water tables  or to  take  advance-  of
 impermeable surface soils  (EPA, 1982).  The  three major  categories  of
 impoundments  are:   (1)   totally  excavated;   (2)  filled;   and   (3)
 comoination.  Excavated impoundments are  those  dug  from a surface  so
 that  the  major portion  of the  capacity  is  below  the  a~ad-=>  o-="">• he
 surrounding land  surface.   Filled  impoundments  are  built" aoov* V-,"da
 such  that   the  majority  of  the  capacity  is  above the  immed^a^
 surrcuncings.   Combination  impoundments result  when mater-'ai is both
 excavaced    and    filled.     Most    impoundments    are   comhina^on
 excavation-.ill  impoundments.   Excavated  material  is used  to  build
 side   walls,  berms,  basal  areas,  and  for   other  miscellaneous
 construction needs (EPA,  1980).

     Surface  impoundments  are used  for  a  large variety  of purposes
       uses_ can be generalized inco  temporary holding,  treatment,  o-
      a^ or  wastes.  Surface impoundments  are used  for:  treatment bv
biodegradation,  stabilization, equilization,   oxidation,  evaporation",
sealing,   ana  ror  sludges,  tailings, and  cooling  water, among manv
vane. uses.   A  settling  pond  is  a very  common use  for a  surfac-
impoundment  as  a  means to  separate  suspended solids  from  ^auids  bv
gravity.    Chemical  additives  may  be  added  to   accelerate"  soT-'ds

-------
 coagulation   and  precipitation.    Settling   can   be   a   pre-   or
 post-treatment  operation.   Surface impoundments  may be  periodically
 dredged  to  restore  them  to  their  original  capacity.    Settling  is
 essentially a quiescent operation but emissions to  the  air can occur.
 Temporary storage of liquid wastes can be  from a  few days to quite an
 extended  period.  These  wastes  may  be  stored  before  appropriate
 treatment or stored as  a post-treatment  operation  before disposal.   As
 mentioned above,  treatment  operations  may be  performed in  a surface
 impoundment.   These   treatment   processes  may  involve  aeration   by
 mechanical  aerators  or may be  non-aerated.   Biode§radation may  be
 aerobic, anaerobic, or  facultative.

      3.    Operation

      There are three  phases  to the  Ufa of  a  surface  impoundment  after
 it  is  constructed.   These  three phases  are:   active',  closure,  and
 post-closure.   The operation  of a surface  impoundment  varies during
 each  phase of  its life-time  and  will be described  separately.

      3.1  Active

      The active  phase of a surface impoundment  encompasses  times  prior
 to  closure when  the facility is  accepting waste or is dormant  for long
 periods.   Because of  the varied  uses  and  large range  of  sizes   of
 surface  impoundments,  the operation  of  a  surface  impoundment during
 its  active phase will  vary  graatly from impoundment' to impoundment.
 The  surface  impoundment may  be receiving mainly  sludge  or mainly
 liquid hazardous  waste, or mixtures of both.  Each surface impoundment
 has a specified  capacity for containing wastes depending on the design
 and  en  the  volume  already  contained  in  the  impoundment as  shown   in
 Figure III-L.  The  operating surface araa,  that"is,  the  araa exposed,
 varies  with  che  depth  of waste in the  impoundment.   The  operating
 depth is  defined as che  distance from  che surface  to the lowest ooir.t
 of  che bottom  of  the impoundment, and the freeboard  is  cha death" from
 che  top  of  the  berm  to  the  liquid surface.  The  surface  impoundment
 may be  designed  with weirs, spillways,  auto  level controls "or other
 means  of  preventing  overtopping.   The  impoundment  may  be  lined  or
 unlined, and say  contain a laakaga detection system.

     Impoundments may  be operated  individually or interconnected  so
 that  the  flow moves  from one  impoundment to  another  in series  or
 parallel.  Depending on the  use  of an impoundment, it may  be operated
 under  steady-state  or  unsteady-state   conditions,   and'  it  may  be
mechanically mixad  to  encourage aeration  or  not  mixed  at  all.   A
 staady-stata operation is one in which cha rat a of inflow  is  aqua!  to
 che rate of  outflow and  losses through evaporation or removal (in che
case of solids).

-------
         Derm
Ordinal
 Griii lu
                                                                                    Operating Surface

 Source:  Arthur I). I.I L tie,  tnc:.,   I'JHA

                                  FIGUHE III 1  CROSS SECTION SURFACE IMPOUNDMENT

-------
 the  influent  wastes.   Dred-^a  <~-   £*       ,ana  C?a  comPos"-°r-  of
      U'U"S  a"  "aoved  from  surface  i^our.izer.ts par,od.ci,,
                                            of  lia-uids ard
 containing  h.zarou   v«t.,  ,usc         .       -
 Oi,charge  through  evaporation  i,  da?^dant  on   he   p
 che=,i=al proosrtiss of  the  vastas and  Che  «.=arologv tnl
restore   the   i.pounc.ent  to  full  ca.acl^,    o
     3.2  Closure

     Surface  ispoundsencs  are generally cenac-
contsinn.ent structures.  The service life of  to
                                                                   s
             procedures  aust  be inpi^anted to 3--:e     re'leTse of
                               III-4

-------
llcl !•, Inn
r
liii|>ouiiiliM>iit tla*>lcwJler
ilrtr/alri iu<| """ treatment
J - 1 	 	 	

uiiiiie 'jlud.je
. 	 *
Ujitiituier In iiiu Off
tiealMient Sl.M.|S U«-waU'ilii.j ilu.l,|e ilVi'oSil
i
~^" 1 luiir repair Sludue
-*• Due repair 1 Iner
reuiuva 1
r___JL___ ' 	 -r 	 '
	 . f
Kiiiiul Ida! iun ^""
^_ Water balann-
" (.unlroli
t
nun II or i iii) syMufi
r

«•>< Mill 4

*
( nvi-r
t
%lll l.ll !•
!<•> 1 .iin.i I Inn

Ir-




-
-
fr-



Wailcujlei
(IIS|IUij|



Sludge II ihd.ju
I Iner 1 t jn,.r
decouttlnullon * u.spola.



                                   111-2     Surface  Impoundment  Closure  Key Steps
Source: U.S. Environmental 1'roteeUon Age,u:y,  September 1982

-------
                      Sroundwacar'   s°^s.   and  the
        ,           °  Srounwacar'  s°^s.  and   the   atmosphere.  '  The
  remaining wastes  must  not  contain  free  liquids.   The  wastes  are
                                  d  the                      ™"
                    Some impoundments may  be  best closed by  removal  o-
  soils    ThTsr  3nd  reSidual3'  Deluding the  liners  and  contaminated
  soils.   These are  transported  and  disposed in  another acceotable  site.
  The  site  may  be  reclaimed by  filling,  leveling,  and revegetation
  Site closure procedures are varied.                           s^^^on.
                 "*P ^  A*  <=l°sure of  an  impoundment is dewatering,
                                                                     *
 reidu    SolM                                              e«"  *•
 residual  solids  can  be  removed  or  the  sediments  devatered.   The
 various methods of dewatering are:

      o    Decanting
      o    Pumping and settling
      o    Solar drying
      o    Infiltration
      o    Process reuse
      o    Chemical neutralization
      o    Absorbents

      Several techniques may be used to remove  the  dewatered  sedime-ts
 as  a  slurry  (wet)  or  as  a  dry solid  (dry).   Wet  methods are  to:
 resuspend as  an air  or water jet  and then  puma  the  slurrv;  or  to
 excavate  if  sediments  are  hardened  and   non-flowing.   Excavation
 techniques  are  high-pressure water  or air jets,  high-speed  rot^v
 cutter  or clamshell  bucket.   Dry methods  require that the  sed^mert be
 driea   by  evaporation  and  then  removed  by  vacuum  transport  o-
 excavation.   The liner and contaminated soil  may  be removed       °
 -apoundment  as  well,  using normal  ascavacion =aehod3.   Ta= si- 
-------
       3.3  Post-Closure

       Once  the  surface  impoundment  is  closed,  it  essentially is  a
  closed  landfill  and  has  to  be  maintained  as such  (see  section  on
  landfills).
  3.    Emission Sources and Models

       1.    General  Description of  Factors  Affecting  Emissions

       Emissions  to  the  atmosphere  may occur during  all phases of  the
  operation  of a surface impoundment.  Organic  gases and "fugitive  dust
  may be emitted  during the active  life of  a  surface  impoundment, durin^
  closure, and  after closure.                                           °

           Active

      Vaporization of  organics at  the  surface from floating immiscible
  layers  or  from the  bulk  aqueous wastes   is  the  main  process   for
  emission losses during  the active life of a surface impoundment.  Some
  losses  can  also   occur  through  vaporization  of  organics  from   the
  exposed walls  of  the impoundment  if  organics  have migrated  into   the
  soil or liners.  These  losses are not considered in this analysis.

      The rate of waste  volatilization in  impoundments  is dependent on
 tne physical and chemical  properties of the  waste  and  the surround-fee-
 environment.  The  natural factors  affecting  the rate of volatilization
 include wind, temperature, humidity,  and  solar  radiation.  The  rate of
 emission into  still   air  is   slower  than  evaporation  into the wind
 Vapor   pressures increase with  increasing  temperature  and   su-^ace
 turbulence,  either  by wind or by  mechanical agitation,  inc-aases  t-e
 rate  of volatilization.  The  characteristics  of  the waste affecting
 its  rate  or  volatilization  include  its  Henry's  law  constant   a-d
 solubility.

    ^ Gases  may  be   generated  by  reactions  within  the  impoundment.
 Sioxogicai   activity   may  decompose   organics   to  produce  me than-
 hydrogen  sulride,  carbon  dioxide,  or  other  gases.   These biolog-'ca*
 reactions  may  be  aerobic  or anaerobic depending  on  the conditions
witnin  the   impoundment.  These reactions  may  be  encouraged  by  the
operators of  an impoundment through the  addition of microorganisms "to
the impoundment  and  the aeration of the impoundment using mechanical
aerators or agitators.   Emissions would be increased in such cases due
to the generation of more  gases from  decomposition and  from increased
turoulenca  on  the  impoundment  surface.   Chemical reactions mav also
increase emissions  if gases are produced.   Mising used to increase  the
rata of reaction will increase emissions.

-------
               -"""- ^-'rnir In, i IHV
                                                        ^L=ai'«^F^ftia^;
       Another  source   of   emissions  during  the

                                                                       is
o
            dried surfaces or  crusts  can be  removed,  ve-t—z
            gasas and  creating a liquid surface,             *
           at,. acting gas venting  and production,

      o    turbulence of impoundment surface increasing vaporization,

      o    generation of spray fron  operations,

      Q    drying of dredged aaterial,


      0
           Closure
«ciT»tion,  fu!i:iv.  ius=  
-------

 :            through  the cover,  or through  cracks  in  the  cover  if  not properly
 *            vented.   More  details  of emissions  after closure  are given' in  the
             discussion on landfills.

                  2.   Emission Models

                  The  basic  relationship  describing  the  flow of  compounds  in  and
             out  of  a surface  impoundment  is  the  material  balance  around   the
             impoundment.  In the most general case,  this relationship is:
                       dw     -     -
                       -T—  «  W.  -W    -Q_,-Q     * 0
                       at      in    out   ^vol   xseep ~  -react


             where      w =  quantity of a waste compound in the impoundment at
                             time t (Ib)

                      *in =  quantity of compound entering in influent  (Ib/hr)

                     ^out =  a-uantit7 leaving  in discharge (Ib/hr)
                    QVQl   =  quantity volatilizing (Ib/hr)
i                      """
1                   Qseep =  G.uanti-7 seeping  through liner (Ib/hr)

1                 °react =  a.uantit7 lost  or  gained through  reaction (Ib/hr)



|           Each  of  the  separate  terms  is   a  function  of  concentration.   The
*           solution  is  expressed as  the function of  concentration  over time".
            Evaluation of  the effectiveness of  evaporative controls in the <"nerai
            case  would  involve solving  the equation  for  two  cases, one  with and
            one without  controls,  for  a  unit mass of volatile compound  entering
            the system.  Comparison  of  the volatile emissions integrated over time
            would provide  the desired measure of control efficiancv.

                 In  the  general case,  the equation is  complex and difficult  to
            solve.    Non-aerated   impoundments   are   pcorlv   mixed   so   that
            concentration  varies  throughout   the  system.  "in  this   case,   the
            equation shown is  not  quite  proper;  a partial  differential  ecuafon
            should  be  used.   Aerated   ponds  behave  more  like  mixed  systems'
            Reaction   loss  due   to   biological  degradation   is   non-linear!
            -vaporative  loss  in  the  general   case,  depends  not  or.lv   on   "he
            etticiency of  control,  but  on the  relative  rates  of  the  other  loss
            mecnanisms.

                For  evaluative purposes, it   is convenient   to   simpl-'v   the
            analysis  by   neglecting  seepage   and   reactive   (for '  example
            cioaegradation)  losses  and  assuming  steady-state.   This  set" of
            assumptions  reduces the  governing  equation  to the simple  form be'cw"
            -ass  is  expressed  in  Ib-mols.   Under this  set of  assumptions, "the
            e-.ectiveness or a control  is  the reduction  in instantaneous  rate or

-------
 Missions  relative  to the 30  control  case.   But,  giver. Che no  other
                                    n>  *u °-  the
      The basic relationship governing emissions ?rom the surface of  an
 impoundment is the instantaneous mass flov equation.



                Q'   *    KoaA (XL -X*>

      where     Q'   »    mass flow (lb - mcl j

                                          2
                A    *    exposed area (ft )

                Koa  *    overall nass transfer  coefficient  (Ib-aol/f t2-hr

                XL   -    mol  fraction of diffusing  component  in liquid

                 *
                X    «    mol  fraction in equilibrium with gas  phase
                          concentration

 The  same functionality aay be  expressed in a  different format us--
 other variables  in place  of moi  fraction.                        - -"=__

     Several  additional'  relationships  can be  introduced  to   reflect
 dependence  on  specific properties  of the diffusing component and o*
 the  overall system.   One  useful  form  of  relationship' between  the
 equ-librium aol fraction  and the concentration in the gas phase is:

                           *
               y    -    Kx

     wnera     y    -    moi fraction of component in gas phase

               K    »    equilibrium constant,  dimensionlass


For dilute aqueous solutions,  the equilibrium constant  in  this format
is approximately related to the  conventional  Henry's Law constant  as :
     where      H    -    Henry's Law constant   (a   -  f=3}
Ib-soi  ;

-------
 I                                                                     7
 i                             P     -    density of liquid water (Ib/ft )
 3
 J                             MWw   »    molecular weight of water
 -t
 |                             Pj    =    total pressure  (atm)

 |                  At one atmosphere,


                              K     »    3.47E


                   The  overall  mass  transfer coefficient,  K  , can  be expressed,
              using the conventional two-film  theory of mass  transfer, as:

J
I                                     -L-  -    _L.  +   i
I                                                "L     ^K
                   where   '  k_   =   liquid film mass transfer
                                                               'ftT-hr;
}                                    coefficient
s
^

|                            k   *   gas-film mass transfer coefficient (^b~ao -,
\                                                                        ft"-hr
I
?                  Expressions  for the individual  liquid  and gas  film coeffici«Uu-
=            ?Q!I\ bean derived  fron theoretical  and  experimental bases  (See~GCA~
|            1983).   The  appropriate  choice  depends  on  the  similarity  of  the
|            situation being modeled to  the conditions in the laboratory  or  theory
\            rrom  which  the  formula was  derived.  For  surface  impoundments,  two
;            regimes are important,  aerated  and  non-aerated.
!                       Gas film, non-aerated
i                       '     "	
                  In  the  non-aerated  case,  the  liquid  surface  is  re^at-'veiy
             quiescent, although  waves may  be  created by wind  action,  inc-eas
-------
                                                       .--^.^.-.»-..>-J-^.^^.^-^.»»«.
                   effective pool diameter (fc)
        N    =    Schmidt  number
   where:    u   -  gas absolute  viscosity

                                             ft-sec
             Di,air  "  diffusivity  of  ith component in air (ft2/hr)
             Pg      -  gas density  (lb/ft3)
   above,
        To  convert  k   to units  consistent  with  the  basic  definitions
       where      R  -  gas constant Cft3-atm/°R-lb-aol)

                  T  -  temperature f'S)
       At one  atmosphere  and 77°? (254C) ,  the resultant ecuatic


                 k  =   1.1  s 10'4  u'78   D "-11  (N  r-67
                  U                         P        5C
            Licuid film, non  aeracad
       Tae  liquid phase  coefficient,  k, ,   is   taken
  (1964) as aodifiad by Swang  (1982).    L
                                           from  Owens  ec  al
\
                      3.12 (1.024)6-20 u
                                                          D
                                                           0 ,  H 0
                                                            7    "!
A Anhur D. Linie, Inc.
                                      rii-12

-------

 i
 i
 I
 I
                        k_
                         L,
                        H
                     liquid phase coefficient (Ib-mol/fc2-hr)

                     ambient temperature (°C)

                     wind speed at surface (ft/sec)

                     effective depth of impoundment (ft)
I
i
      The  wind speed at the surface may be approximated  as  a factor of
 the   normal   wind  speed;  the  factor  0.035  is   cited  in  the  above
 references.

      The  original  form of  Owens  relationship was  applicable to flowing
 streams  and  showed  a dependency  on  stream  velocity  and depth.   The
 form  used in this  study,  as modified  by Hwang,  accounts for  upper
 layer movement  induced by  wind over  the  surface.   The  correlation
 developed  by  Cohen et al., (1978)  is perhaps, more applicable but  was
 not used.   The choices of Hwang's fora of  the  Owens relationship  is
 consistent  with several other  studies related  to volatile emissions
 from  hazardous waste  TSDFs  (Breton et al., 1983;  Spivey  et  al.,  1984).

          Ga-s-fila,  aerated

      For aerated portions  of  impoundments,  the coefficients are  quite
different, reflecting  the  highly turbulent nature of mass transfer  in
this  kind  of system.   The gas-film  coefficient  follows the  work  of
Reinhardt (1977) as reported by Hwang (1982).
I
e
I
  k.  =  .00039 \Dl',air)  (N  )1'42(N. )-21(N )'4(N  )°'5
                                re       rr       D     sc
                G
                 where      k..
                                    .
                                D,, MW
                         gas fi'lm coefficient/
                                      gas  density  (lb/ft3)
                                                            Lb-mol
                                                            hr-ft
                      Di,air
                           DT
                         diffusion  coefficient  of ich component in air
                         (ft2/hr)

                         diameter of  aerator  turbine  or  impeller (ft)
                           Mff.
                        molecular weight of ith  component

                                                     2
                                     gas Reynolds number
                                                O  D_
                                                 g
                                                                 S

-------
       vhere
gas abolute viscosity (—
                                                     Ib
                                                2
                           Froude Number   =  _"  Dt

                                                i

                           gravitation constant (32.2  ft/sec2)


                           power number  =   p  2
                                             - r
      uh o T* e»    t>     _
               *r         P°wer  "  impeller  (ft-lb/sec)


              PL     *    liquid density  (lb/ft3)


              JTSC    -    Schmidt Number  -       u»
                                                  DI,air
                          °"
 models,  the  aerated region   sco
 c«eralf  highly turbulent -onvx-C,a "?, 1°  hf8  'V°  Potions,  a
 and  a  second region outs'd."^.  ^7r       boundar? of the  aerator,
 outvard  fLaanev %/ai    7                 2   ara flow aovas
                  '
sufficient  to  illustrae    .  —-    f dSlas>lifred  —-- -ec  is
on a variety of potential wnCrVniVg t^STes! °= V°laC"a  2^si3ns


          Liquid fila, aerated


     The liquid phase  coefficient  *0-  the  a«^-^
trom Thibodeaux (1973).                     ae.a^ed portions  is  taker.
                                          (106)   j Di'  H 0
                             av7
    vnere:


         fc-   -    liquid phase coefficient |~
                                111-14

-------
  s
  3

  4
                                   oxygen transfer rating of aerator  .lb~°2

                                                                      hr-hp



                                   efficiency of power conversion  (n a .65 - .90)



                                   oxygen transfer correction factor (as .3 - .85)



                                   surface  area  to volume ratio  (ft"1)




                                   volume of  impoundment  within  the  effect  of the


                                   aeration (ft  )
              fraction  'of"*! P°rtl°n»  of  an  ^Po«ndm«t  generally  cover  onl


              '
              aerated and non-aerated portions.




                   Referring  back  to  the  two  film theory  eauation  combinine  the

              concretions of both gas and liouid film coefficients, it can be
                   and
I
                            k.    «   K kr
                             "           (a
                  then K
                        oa
                  That  is,  if  mass transfer  through the  gas  film  ±a


                                           ni-15

-------
       Floating Imlscibla Organic
                                       fil°'  —raced  coeffic
                                                                 ient
  to thf organic"
                                  °f the P°lluC*nC
                                                               layer ne
                    -   ?vp/?T
      Where     Pvp   "   vaP°r Pressure of pollutant, ata.

                ?T    -   total pressure - I ata.

      At atmosphere pressure  measured  in atmospheres,

                5T       "Q
                 oa  "   via   G
      3.    Paraaetars That Control Emissions
 for  dr                                 *» 
-------
 a.e the »md speed at the surface (u )  and the effective death

                                  can b
                         is, deeper impoundments have,
                         -ts. The choice of depth is

 s-a. 'J?sZs3s£ ?s£f£'-;ii

      are
ssa.
               as a dilute aqueous soluf'on   I^ -'
                                     '
c-  lotantial Controls

   1.  Introduction

       etc.
                     -             ,
                   ssions can be collected and treated

-------

1984)
                              is  control „
                                            a  (see
                                                         y  ec
                   svstam  costs.
         .cost of recovery of
         condensation, ,Cc.).
                                    /
                                    (a-S" carbo^ adsorption,
'*   DeS±Sn ttd Operating ?rac=ica£

C the ors
                                             a
                        ni-13

-------

  «

  i
  j
  i
  i
I
                                                                                 -
                                he section ou landJilS        ?°st-closure practices
                    This  discussion
       3'1       Design


       3.1.1.    Surface Area Minimization
impoundments, the
operating surface        to
impoundment,  minimization of  surface
decrease air  emissions    But

                                         *±T   emissions

                                            •  KC8rtain  capacity surface
                                           Wlth ras?*ct to deoth would

                                                                 %



                                     H?
or increased  depth.           §   °U"d  ba  ra^uc
                                                            in efficiency because
                 3.1.2
                           Freeboard Depth
                      ^Utilization,
           in-sicu controls).   The most  iaDortanr       *   7  (see   secc"n  on
           errectiveness  of  the  d«.0«-  *-S°  ?    paraaeta-  in  determiain.

-------
   cost factors are:
                                                     — -----  be  increased
                                            an  average  smaller depth.   The
        o
        o
              cost  of  material for berm
              labor costs

              costs for more  frequent  draining of impoundment
                                              *
  60 <-,  ft  rraI5  *"*** Guidance Document (July   1932}  «,
  ou ca  (2  feet)  or freeboard  to  orevpr,,- „          ;  su§Sestea at least
  rreeboard is  to minimize  run-on intc? th* f^"1?8*   A Way to ^"asa
  a run-on control system.  For Tar.e  laeoQ lapou?dB«c  ^  incorporating
  break the wind  may be more  effective ?C.  *      ^'^ C°ntr°ls *°
  be necessary to achieve enough wind-breaking  ^   rSa  fraeboa^  ^>*
        3-1.3
                 Inflow/Outflow Drainage ?i?e Locations
                                  o
  discharging  above  the  liquid su-ace
  and may also cause spray formation *
  be  destroyed.   This dry  crust °s
  creating a barrier or a cover  on'
  designed to  discharge  belo^ ^ the
  as  possible,  into  the  bulk  o
                                                          °« the surface
                                              .cru«/n ^« ««fac. will
                                                  ^ducing emissions  bv

                                                        ?i?eS  Sh°uld  b^
                                              "             and «
      3.2

      3.2.1
                Operating  Practices  -  Active

                Temperature of  Influent
     The vapor pressure of a 1-?Quid ---^-
-en  tvo  Uquida  of  dif f er^c tm^                ««««.   Also,
currents  are  induced  vh-'ch causa  °?!r     ^ ara  ai-"ac'  convecciva
system win increase vciatili2aC4^0tS;,  iiliS- di«art«"  °='  cha
emissions, the influent should  t. ^s^       3^-«.   To  reduce  air
to the bulk of the  liquid^             gaa " " Cl°Sa
                                                    be in
                                                     '°*
                                                   .
                                               7 °Z
     Ic is unknown how effs
emissions in actualitv. ~z\,
impoundment for  application sxnce  the
be reoucaa.  Another consideration 
-------
             Costs are expected from cooling influent befor* dischar-inz inm
          an impoundment.  A heat exchanger may be needed.    Charging mco
 I            3.2.2   Dredging, Draining, and Cleaning Frequency

         slSsSIa—s-


|
|            3.2.3    Handling of Sediments and Sludge
                        .                       .
         methods for dewate-i™ anH  ji* aiS.P°sai ^ an°ther facility.  Some
            There may be increased costs due to:


            o   energy usage (solar drying has zero ene-av
            o   equipment costs                  °"
            o   labor costs


            3.3     Operating Practices - Closure


            3.3.1    Dewataring
               _ a different method for dewater-'rz waste du—'no. -v,
        process can altar the amount  " -'-     •     au^_ng the closure

        pumping and disposal with the «a ~" am _.s.J"ons*  ^~3ssurized  liquid

        contain emissions. Rao id dewacerin*  can limir5'-,-8^^"1
                        "     — •• •— *. .^iA ^  \_ d.it j—in j_ ^ 3^Oi02C
          closure     ' " U"d f°T r5?id devat"-i vill increase the
cost

-------
      3.3.2     Proper Consolidation

      Proper  consolidation  before   final   cover  reduces   settling
 Differential settling can  cause  the  disruption of the  integrity of tfc
 cover leading to uncontrolled emissions of  gases from underneath th
 cover.   Settling nay  be  significant if remaining wastes  are  high  i
 organic  content  or  if  organic  sorbents  are  used  to  solidify  th
 wastes.    Inorganic   chemical  fixation  processes  are  not  prone-  t
 significant settling  (EPA,  July  1982).   Wastes  should be compacted  a
 ouch  as  possible before installation of the  final cover.  This  woul
 reduce  the  possibility and  extent  of settling once  the  cover  i.
 installed.

      3.3.3      Fugitive Dust Abatement

      There  are  two common control techniques to  reduce fugitive  dust
 emissions:   wetting  and stabilizing.   Wetting  is the  application  01
 water as  a short-tarm method  to control  dust  in  a  confined  sice.
 Stabilization methods  isolate  dust sources from  wind  erosion and may
 be  physical,   chemical,   or   vegetative.    Physically,  a  cover   of
 stabilizer  materials,  e.g.,  rock, soil,  crushed  or  granulated  slag,
 bark,  and  wood chips, prevents  the  wind from disturbing  the  surface
 particles on the impoundment.  Chemical stabilization involves  the use
 of  binding materials   that cause  smaller  dust particles  to  adhere  to
 larger surface particles.  Many types are available,  many of which are
 proprietary  developments.  They  are  applied  in  conjunction with water
 or  separately.  Host stabilizers  work for a limited period of time,  in
 general, no more than  a few months.  Vegetative  stabilization provides
 permanent dust suppression, but the surface must be well prepared with
 "utilizers,  organic   matter,  etc.  Vegetative  stabilization  is not
 applicable  to fugitive dust abatement during  closure  (I?A, L982) .

     The  affactivenass  of wetting  and  stabilizing  tachaiaues  are
 highly variable  and  depend greatly on  site  specific  characteristics.
 Generally,  these  techniques would  not be  frequently  applied  during
 excavation  since  surface  impounded  waste materials  usually  possess
 sufficient  moisture.   Efficiencies  also  depend  en   the  type  of
 stabilizer  used.   Chemical  stabilizers ara  extremely  variable  and
 particularly difficult to evaluate because  of proprietary information.
More information on fugitive dust statement is given  in the section on
waste piles.

     Wetting is a  cheap  short-term method  of dust control.   Physical
covers have  high associated  costs in their application,  particularly
if  transportation is required.   The costs of  chemical  stabilizers are
variable.

-------
                      4.    In-situ Controls

                      Technologies applied  at an  impoundment  site  during  the active
                 phase of  its  lifetime  can  be  used  to  change one  or  more of  the
                 parameters   that  affect  emission  rates  from  the  surface  of  the
                 impoundment.   Some of these parameters are exposed  surface  area,  wind
                 speed,  mass   transfer   coefficient,  etc.   The  in-situ  technologies
                 described  below are:  rafts,  barriers,  shades, floating  spheres,  and
                 surfactant  layers.

                      4.1  Rafts

                      Rafts  reduce the surface area.  They must be designed  to remain
                 afloat  and must also be  kept  from being  flooded  by waves  on  the
                 surface of  the impoundment.  Flexible membrane  covers may  be  made  into
                 ratts by attachments  on  to a frame  that  is  sufficiently high  to  keep
                 the rart from being  flooded.   However,  the higher the  frame,  the more
                wind  the  raft  catches,   and   therefore,  the  stronger   it  has  to be
                structurally.

                     A "moat  raft" consisting of  a  small frame inside  a  large frame
                with  the frames  connected  at  the  corners  is  a  design that can reduce
                wind  shear  and   also   reduce   flooding.     The   inner   frame   is
                membrane-coverad  and  serves  as  the vapor  barrier.   The  open  area
                between  the  2 frames traps  the  waves  and prevents  flooding  (Cluff,
                1967).

                     Rafts   may  lead  to  an   increase   in  the  temperature  of  the
                impoundment  and  thus  a  reduction  in their  effectiveness.   A hi»hlv
                rerlective  top surface,   for example,  a  surface of aluminum  bonded to
                polyethylene  or  Styrofoam  painted  white  on top  would   help   in
                mitigating  this problem.   Crow (1973) showed  that unpaintad  Stvrofoam
                with  +3  percent coverage  reduced evaporation by 35 percent.   Wnen  th»
                top was painted white, a  45  percent coverage gave a reduction of 43-49
                percent.  Styrofoam not  only floats and sheds rainwatar  but  serves  as
                insulation on  the surface of the impoundment.   Experiments have shown
                t..at   one-inch  thick  Styrofoam  panels   significantly  reduced  da-'lv
                variation in stored thermal  energy  (Crow,  1973) .
                    Floating covers or rafts have been used on smal1 wate^-  "-
               to  reduce  evaporation.   Tnese  rafts  are  small  (around  8  fast" by"8
               feet)  ana  can  fit any  size or  shape reservoir.   They are  easy'  to
               install and  do  not have  to  cover  Che  entire surface of  the pond   A
               raxt_can be  made  of  any  kind of material.   Styrofoam,  polyethylene,'
               aluminum bonded  to polyethylene,  butyl rubber, and floating conc-ete
               (mace  rrom cement, sand,  and Styrofoam)  have all  been  field tested
               wnen used  on a hazardous waste  impoundment,  the raft material would
               nave to oe  chemically compatible with the waste components
Iff 131:
*fi*-!££:•*>-;-

-------
      Another
 coated  with
               	— -•» wfc/wj.jr iu
-------
   i
   m
   a
                   4.2  Barriers


                              spacing to the barrier height (L/H)
  §                       	   uiuj-ail= j-inings rastened to the pickets.
             =2                               ""™-
                     chemical compatibility of wasts vich barrier.
            area to be controlled"). ""'  """  ^  '**  °*     impoundment (surface
I           and  floating spheres                "cnnoxog^es,  tor example,  rafts
2                       '
2               A T  0, -
g               *.J  Snaaas
5

           together with a  cren-'cai  --'1m  -           ^  density.   When used
           percent.         ^-^  .Urn.  the  recuction was increased  to  46

-------
                             TABLE III-l
                   EVAPORATION SUPPRESSION BY SHADES
     Material Tested
Evaporation Reduction (oercar.t)
Polypropylene Mesh
  6 percent shade (natural)
              26
Polypropylene Mesh
  47 percent shade (black)
              44
Source:    Crov and Manges,  L967

-------
                •yafgj^^ig^^

                B£^^5jgSgagyLffix'^^rj5«iviaL.fcg^j;j=jfcL -if v. .>~-5r~..- •..-_~--.u-"--~  . •• -•- <;-v v>^-^-'> ?%V?,1'.^;r,iJ-*(iA'^iS-V^^«<'?'.'
                _^J.--s<^.-.-^£m^|^^^a£5^gM^a~i-^«£S^..^«-v?_4 -•>—^ -.>._:i.--;-^ J>. •--...-...-  ,•„.'.„. -» -.-,-:--•- -•-«•- ---^.^ *-..--ii-'.---*\^-*V*.4-.-JX-i
                                  '"••••^•••••g'aBg'gsa-"—  ^-'ii»-TTiiti»i<*iyiftiir..»^ij^g^aCTi^g^^g^^_^.jr^rvf3v^
  II
                           iy  coupled  to
                                    for
                                Synthetic Covers
                   =or,tair.in8  the   emissions
7,7
                                                                                              red«=es


                                                                               Communications,   April,
"«»'-_ ;
Natural  Gas   in  Seu'ah    V
        '  P
                                                                                            by
                     CZCODOHE.



-------
       4.5  Floating Spheres





























 siaply poured  onto  the surface  of  the  Ucu-d  u-,r<7 -• -        -    :

 covered.   The  approve   number  of  Vpte'sreVuiAd"0!^'^7
 application is shown in Table  III-2       sPae-as  required   tor   an

ian.  a11 "l*Uceca  Iri
                            111-28

-------
 A
 S
 m
s

                                       TABLE III-2

                       SPHERE  REQUIREMENT PER UNIT AREA AND  VOLUME
                          20 ^           38 mm           45 mm        150 mm
                         (3/4 inl          (l*i in)       (1-3/4 in)      (6 in)
             Quantity /m2    2,500-3,000       750-800         500-575      45.50

             Quantity/ft2     230-280          75-35           45-55        4-5
I
|            Quantity/m3  165,000-167,000  24,000-25,000    14,500-15,000   350-500

g            Quantity/ft     4,670-4,730        690-710          410-425       10-11
            Source:  Capricorn Chemicals Corporation,  Secaucas,  NJ,  1
984
                                          111-29

-------
       -tors involved in the  choice of spheres arg:

        chemical characteristics of Waste.
                              .
                to a0st chemicals         ta°la) '   The s?^reS
   0    size of sphere.
   °    numfaer o« spheres required
 This
     Surfactant Layer
     catagory  irc^
                     -' surface.
wlna-concroUad dispense
                                  ssrs- jj
                                on rafts, vick drippers,"
t
       that tnere
                             the
                                     nuicv Of
                                    * ^ -
                     111-30

-------

3
2
                                                                            technology
              impoundment.   A

              in  one   situation

              increases  the   diff

              ^Plication that  is  surc

              layer  on  the impoundment " u"rfa«
                                                                       imP°undmenc  to

                                                                      V * •<"*«*«
                                                                   another-    It   also
                                                                         *   ««   of

                                                                        *
                      active i.pound.ents
                                                               nof
                                                                              var7
                                  n      or
   the  layer reduces the mass transfer  col^   7  ^S~£^ controlled.  If

   control  to  the liquid side, then the  ^"M*"  SUfficientl7 to shift

   reduced  significantly.   This  is the «ituar    "" ? emissions can be

   reservoirs.   For dilute  solution j  of or,     aC Ch"  SUrfaCe °f wat"

   general  rests  in  the   liauid-liL    Lfi     ^  WaCer'  the  Concro1
   resistance will  not,  in  general ^1^ ,  8  .addicional  iiquid  side

   the overall rate  of 'e^sfon "al'ch^gh a S^^flCanC  »*>«ions  ^
  innnxscible liquid, such  as  mineS  o!l ****<*: *lo?**8  layer  of  some
  to be significant.          m^.al  oil,  ^y aad sufficisnc resisc.nca





  would have Co\e ^lose lyP pitied at ^he 1^^' -^ a
-------
      Important consideration  in designing  a  surfactant  layer  systa
 for the reduction of  evaporation from surface  impoundments ara:

      o     chemical characteristics  of waste.

      o     choice  of a suitable surfactant  based  on the  waste.   This ii
           most likely to  be best  resolved  by  tests  with the  actual
           waste on the top  of  the impoundment.

      o     thickness of  surfactant  layer.  This  factor  may  not  be
           significant.    McCoy   (1982)    found   that    the   rate   of
           evaporation  is  independent of layer thickness.  The thicket
           the  layer,  the  more effective it  is  likely  to  be, although
           there  is  probably  a  critical  thickness  above which  the
           marginal reduction of  evaporation  is very  insignificant.

      o     wind speed over  the  impoundment.

      o     temperature  profile  in the impoundment.   The  use of a  layer
           over an  impoundment  is  likely to increase  the  temperature  on
           the  top  of  the  impoundment  and change the  temperature
           gradient  in  the impoundment  (Bartholic,  1967).   This  would
           somewhat  decrease  the  actual   evaporation   reduction  when
           compared  to  expected effectiveness.

      The  cost  of  using surfactant  layers  depends on  the  surfactant,
 the rate of application,  the equipment and labor requirements.

      As  mentioned  above,  the  effectiveness  of  a  surfactant  layer  is
 dependent  on  the  ability to maintain a continuous  film.   This  means
 that  a  surfactant  layer  would  not  be very  effective  on an  aerated
 impoundment  since  the   surface  is   continually  disturbed.    This
 technology looks simple at  the  outset, but the  choice  of an effective
 surfactant would be a much lass simpla matter, considering the complex
 nature  of hazardous  waste  impoundments.   Surfactant  layers ara not
 included  in  further discussions of  in-situ.  controls because  of   these
 uncertainties   and   possible    limited    applicability    in   surfaca
 impoundments.

      5.    Post-Treatment

     As discussed  above in the section on synthetic membrane  covers,
 collection and post-treatment of  emissions have  been used  by  at  least
one facility,  Upjohn in New  Haven, Connecticut.   In  this case,  an air
 structure  with a  vent and  post-treatment using  ragenarative  carbon
adsorption was usad.

     Basically,  a  post-traatment   control  requires   a  means   of
collecting the emissions by means of a cover  and  a vent, and  traatment
unit(s)  at  the vent.   Other forms  of traatment may be used  besides
carbon  adsorption,  including   afterburning   and  condensation.    De-
scriptions  of  two approaches,  carbon  adsorption  and  afterburners
follow.
                               TTI-32

-------
  g                 5.1  Gaseous Carbon Adsorption

  § -                Removal of volatile compounds from a  gas  stream by adsorption is
               fa widely used process.  Adsorption is a process  in which the volatile
               components  retained  on  the -surface  of  granular  and  highly  porous
  |             solids.   Activated  carbon  is  most commonly  used  as  the  adsorbent,
  |            although other materials  are available for specialized applications.
 .§            In che  process,  the  gases  to  be  treated  are  sent  through a bed  of
  §   -         adsorbent.   The components to be removed adhere  to  the  surface  of the
  |            grains  and,  in addition,  diffuse into  and are trapped in  the pores  of
  a             the material.

 I
                    The process  can be reversed so that  both the  adsorbent material
               and  the  vapors  that  have  been retained  may  be  recovered.  Carbon
               adsorption   systems  are  available  as  complete  package  units   from
 |             several  manufacturers.   These units can be installed with  the minimum
 |             of on-site operations.  Custom designed systems are  also available for
 !"•             larger or special purpose applications.

                   The cost per unit quantity  treated is generally considerably less
 p             in  a  regenerative  configuration than  in  a non-regenerative system,
 |             even  though  the capital costs are higher for  the former type.  If the
 I             recovered material can be reused and has a high market value, recovery
 §             in carbon  adsorption  systems can produce positive  cash  flow.  If the
               recovered material, on the  other hand,  has  value only in terms of the
              heat content used as a fuel,  then  the  overall  costs will generally be
              higher.

                   In  hazardous  waste  applications,  particularly  at  commercial
              facilities which  receive  a  wide  variety  of  wastes,   the  recovered
|j            materials would not be  expected to have  appreciable market  or  fuel
as            value.  In this case generation and recovery will be considerably mora
6            expensive.    If the  recovered  organic wastes  must be  subsequently
1            disposed of by incineration or even by  land  disposal, then the overall
Ji            costs  may  approach those  of operating  in a  non-ragenerative  node.
              Although the  capital  costs  of  non-regenerative  systems ara  smaller
              than  those  which recover  carbon  and  adsorbed materials,  cost per  pound
              of material removed are very  much higher because large  quantities  of
              expensive carbon adsorbent  would  be  required.

                  Adsorption is a  very  effective process.   When  gases  containing
              organic  vapors first contact  fresh  adsorbent the vapors are  quickly
              and  efficiently removed from  the gas stream.  Efficiencies of" up to
              95% are  commonly achieved.  As the gas being treated  continues to flow
              over  the  bed of carbon,  its  adsorfative capacity  gradually  decreases.
              At  some  point,  the  adsorbent  will become 'saturated  and  no  materials.
              will be  removed.   In operating systems,  the process  is stopped before
              this point,  called the breakthrough point,  is  reached and"the carbon
              is Cither replaced or generated.  Regenerative systems employ  multiple
              beds so  that  gases can be continuously treated while one of  the beds
              is being  replaced or regenerated.  Alternate approaches use moving bed
              adsorbers  in  which  fresh  carbon  is  continuously   replaced.   Spent
                                           111-33

-------
 sorbent  is removed  at  one  end  of  the  system,  passes  through  tl
 regenerator,  and  is  replaced  at  the gas  inlet  end.   This  type  <
 system, in  theory, has a more  efficient  utilization than does a  fix«
 bed  system using  alternate units.   Moving  bed  adsorbers  are  moi
 expensive to construct and operate and more difficult to maintain.

      In  conventional  treatment   applications,  carbon  adsorption   i
 generally  more  economical  than  the  technique  described  below, in
 cineration, at  lov  concentrations  below  about 100  ppm.   In appli
 cations for the recovery of volatile  emissions  from hazardous wastes
 the economics may  be reversed  if the  costs  of secondary  disposal  o
 the recovered waste components  is included.   Incineration destroys th
 materials  and  no  further  disposal  costs   are  required.   If  th
 recovered materials  can  be raturned  to  a  treatment system,  then th
 carbon adsorption may retain its  advantage  for very diluta gases.

      5.2  Afterburners

      Afterburners are also called vapor incinerators because they an
 used to incinerate gases and vapors.   Sources of  information used  ii
 this description are  Ehranfald and Bass,  1983; USEPA,  1978;  USDHEW.
 1970.  Diluta  concentrations   of  organic  vapors  are burned  together
 with additional fuel  to  ganerata a high temperature of up  to 870aC.
 The fuels used include natural gas,  L?G,  and' distillate  and rasidua]
 fuel oils.  Incoming  gases and vapors ara  decomposed and  oxidized as
 they pass through the afterburner.  Combustion products  include carbor
 dioxide,   water  and   others,   depending  on  the  composition  of   the
 incoming gases.   The  residence  time  at temperatures lass than 8703C is
 between 0.5 to  1.0  seconds.    Generally, afterburners  should  only  be
 used on those pollutants  that  will  not produce undasirsbla oxidation
 products.

      Lower oxidation  temperatures may be  obtained with the usa  of  a
 catalyst.   Catalytic  afterburners oparata  at  temperatures  of  between
~5^0" to  S7Q3C,  although aost combustion catalysts cannot  be  operated at
 temperatures  greater  Chan  between   540  and  650°C.   Catalysts  used
 include platinum,  platinum  alloys,   copper  chronita,  copper  oxide,
 chromium,  aanganasa,  'nickal,  and cobalt.  When a  catalyst is usad,
 cara must be  takan  to prevent poisoning of  the catalyst by  limiting
 the concentration of  incoming  organics to  prevent  overheating of the
 catalyst.    Most   combustion   catalysts   cannot   be   operated    at
 temperatures greater  than 5<*0  to 650aC.  The  maximum concentration  of
 volatile   organic  carbon   is   limited  to  25   percent   of  the lower
 flammabiiity limit.   Catalysts begin  to  lose  their  effectiveness  as
 soon as they ara used and used to be replaced when they ara worn  out.
 Catalyst  life  is usually between  1 and  5 years.

      Afterburners  can be operated with a heat  recovery system.   The
 hot combustion gases  can be used  to preheat process gases entering the
 aftarburner.  Lass   simpla is  secondary  heat  recovery   with   heat
 exchangers to  transfer the  heat energy  elsewhere.
                               111-34

-------
a

I
i
3
!
                  In designing an afterburner system, the following  parameters  must
             be specified:

                  o    gas  and  vapor  volume,   both average  and  extremes,   also
                       variations due to changes in seasonal  temperature.

                  o    identify of contaminants in gas.

                       concentration of contaminants in gas stream.
      o

      o
                       expected  destruction efficiency  of  the afterburner,  from
                       bench or pilot tests.
      Afterburners  can be  designed to  handle a  range of  gas inflow
 rates.  The constituents of the gas stream must be restricted  to those
 that will  not  produce undesirable combustion  products,  and must also
 not  contaminate  the  catalyst  if catalytic  oxidation  is   used.   If
 corrosive  oxidation  products  are formed, the  afterburner may have to
 be constructed  from  special materials.   The  contaminants  in  the  gas
 stream must be  destructible to  required efficiencies at the operating
 temperatures and residence time of the afterburner.

      The efficiency of an afterburner system depends on:

      o    residence time of the  gases in the  combustion  process;  the
           efficiency  increases with residence  time for times less than
           1 second.

      o    temperature  of   combustion;   efficiency   increases  with
           temperature.

      o    degree of mixing  of  chamber; efficiency  increases  with flame
           contact and oxygen concentration.
                 o

                 o

                 o
           nature  of  waste  gas.

           concentration  of contaminants  in waste  gas.

           catalyst type  in the case of a catalytic  process.

     o     active  surface area of catalyst which depends en how  long
           the catalyst has been used.

     Organics  have  been  destroyed at  efficiencies  greater  than 98
percent with well-designed and properly-operated afterburners.

     The  afterburner  is  a well  established method  for  destroving
volatile   organics.    It  is   a   conventional  and  well-demonstrated
technology.  In its  use  in hazardous waste  applications,  the changes
-n gas ZJ.QW rate and composition may decrease the operating efficiency
or the afterburner when compared to the design efficiency.

-------
       1.1  Selection of Parameter Values


  from T° Comments?                 a
  (environmental)  parameters  nicessa-v far
  derined.  Some  typical  vastas  Jound  7
  selected.   The  vaJUM  fl£  p"^/**
  calculating  emissions  vere tabulated for
  of  surface impoundments  vere  etllua ted
  from  WZSTAT  data  and impoundmlnts     '
  capacity percentiles vere  se!ac°!d  for
  surrace  areas  and  depths  at  ful    °
                                             ia, Deducing  emission.
                                        Lmp°ament>    and    sita
                                                 9  missions  vera
                                                impoundments   vere
                                           P"P"ties  needed  for
                                           *"*'**'   Three si2es
                                       .?' ^i2eS  W"e  de"rmined
                                       "    10Ch   5°Ch'  atld
 surface  area,  diameer  and
 symmetrical  i^pour^euts  with
 vxnd speed and  e.mp.racur.  vere as^ed
 25 C respectively.
                                                       of  ex?os
                                                  Calculatsd   for
                                                      "*"'    ^
                                                     per hour  and
1.2  Calculation of Mass Transfer Coefficients and Emissions
£•
impoundments  vith  a  floating
percentile impoundment assume!
size.   Small  aerated  instap
CanL.  The  e.uations
repeated in Table III-3 .
                                                 -  to  represent
                                                 '   2araCad'   acd
                                 Qe   ,          yer*   rne  10ch
                                    aeratec because  of  isa  smail
                                          d  *  «»?««  IV  under
                                       .ransrer  coefficients  are
                                    «lculac.d  for each
                                                               of  che
                      -  X
                               - aol/hr
 Chan
 less  than  1
 emissions calculated here
 the impoundment.   '_
aethodoiogv.
                   "lcal"«d
                             ce
                               "
                                        chat 2. vas =uch  -
                                     » ^.^^t.  I,  S
                                     1*t*a -°7 aulciprying   the
                                        -  os  vaste component  in
                                emissions  are  orovided 
-------
   i
   I
                                             TABLE  IH-3

                                     MASS  TRANSFER  COEFFICIENTS
               Individual

                    Non-Aerated:
                           1.1 x 10
                           3.12 (1.024)
                   Aerated:
                           J (Prn) (1.024)9-2" „  H0»j    /Di>H0     0.5
                   Floating Immiscible Layer:



                   kG  -   1.1  x 10"4 U'78 D --OJ
                                                   sc
             Overall

                N'on-Aeratad:
e
                  ror a dilute aqueous  solution  at  1 ataosphera,



                  -^-  -   -I  -         I          .
                  £Q£      k,   '    fc   (3.47 H)   wnera H = Henry's Law

                    *                ^            Constant (ata-£r3/ib-nol)
                  Aeratad:


                                   A
                          (K  )     -£
                                            ^oa7T   A
c   A    '  ^--'-T.   i
                  Convective  Zone





                                                        vhera K - 3.47H

                                           111-37

-------
                     TA3LZ IH-3 Continued

 Turbulent Zone


   1               ]     +     i
                           K(k_)        vhere


 Floating Immiscible  Layer:


 K-,       -     P   k_/P_
Source:  Arthur D. Little, Inc.

-------
   1.3  Emission Reduction and Efficiencies of Controls




   The reduction in emission rates is defined by:
                                                - X,*,
                               and assumed  e° be
 Al -
                    A2'
      wo

(Xoal
                                 V
 . .•*  Cost-Effectiveness of Controls
          ----
In-situ:



A
     constant  =  vR (S/yr)

-------
wnera   y  -  cost per pound raduction
        7  "  A  ($/lb-reduced)
              R
     Post-treatment:

     A   -   F  -I- pR  ($/yr)



whera  F  -   cose of  collection  system per year
       P  -   cost per pound of post-treatment  system
       y  -  A  -  F  4- p   ($/lb-reduced)
             R     R


     In terms of throughput (T) and efficiency  (E) :

     In-situ:

     A   -  yET   ($/yr)
     7   «  A/ET  (5/lb-reduced)

     Pos t-treatmant :


     A  -  ?  + pET  ($/yr)
     7  -  F   T- p    ($/lb-raduced)
           ET
      Pratreatment costs  var*/
 volatiles   removed
                                                          r  P°URd  °£
dn- C«™-f°ir ?reCraaPerit: we-a-  obtained from  Sniv
                                                                1Q8A)
=or post-treatment by carbon absorption arc
from E?A (1932).                  "


     2.   Parameters
                                                         -e-   •  ,
                                                        .era ootaz.naa
                                                   the
                        d  3  ordars "
                            111-40

-------
/Inyl  Chloride
lathyleue  Cli
I'r 1 ch 1 orue thy 1 eno
i-Xylene
It-'thyl Ethyl K^tone
el ijicliloroetliylone
Lliyl benzene
-Butyl  Alcohol
roiuobeiizcnu
irbon Tturachlorldo
    Alcohol
'erage
west
                                                                     TABLE  11 f-/»
                                                          TYIMCAI.  VALUES  FOR WASTE  PARAMETERS
                         Liquid
                                     Liquid    Henry's Law   Molecular  Olffuaivity
                                                                                          Gas
                       J^15l£iL   V|«ic<>sit)r    Conun.nt
          of oxygen In water ut 18"0
urce:   Arthur D.  I. It tie,  Inc.
                                       (^  || (,) . 0.5y x
(Ib/ft )

56.8
82.8
91.6
54.9
50.6
53.7
50.3
101.3
54.1
54.1
50.6
93. J
99.5
69.0
49.3
49.3
66.33
101.3
49. J
(lb/ft-at:c) (dtui-ft /
lli-iuol )
1361.42
3 xlO 129.79
3.9x10 145.75
4.4x10 U8.09
3.9xlfl"A
-4
4.2x10 83.29
2.8x10"'' o.70
6.0x10 132.94
4.0x10"'' J05.71
4.5x10'''
2.0xl()"3
a.oxio"4
6.5x10"'' 368.38
5.4xlO~'' 5«j 26
a.ixio"'1
0.4
6.05x10"^
2.0xlO~3
2.8x10"''


62.5
84.93
131.5
78 11
100.2
106.16
72.1
165.83
92.1
106.17
74.12
157 02
153.8
112 56
46.07
58.08
100.08
165.83
46.07
                                                                          In Water     Viscosity
                                                                            (ft /hr)    (Ib/ft-sec)
                                                                        6.23x10
                                                                        6.23x10
                                                                               -5
                                                                               ~5
                                                                                       3.02X10
                                                                                              '5
                                                                                       3.5X10
                                                                                      1.9X10'
                                                                                      6.05X10
                                                                                      4.37X10'
                                                                                             '5
                                                                                             '5
                                                                                      3.77xlO
                                                                                      6.05X20
                                                                                      1.91X10
                                                                                             ~5
                                                                                             "5
                                                                                             '5
Gas
IHtlust-
vity
(ft2/hr>




0.29




0.26

0.27
0.26
0.24
0.24
0.38

0.28
0.38
0.24

Schmidt Gas
Number Density
Ob/ft3)

0.17
0.24
0.37
1.71 0.22
0.28
0.29
0.20
0.46
1.86 0.26
0.29
1.88
1.71 0.44
2.13 0.43
2.13 0.31
1.30

1.82 0.30
2.13 0.44
1.30 0.17


A II

g-mol
6263
7572
8315
10254

9904
8150
9241
9369
9309

10158
8272
10098
9674
7642
8872
10254
6263

Vapor

• ressure
(utm)

3.5(25°C)
0.46(20°C)
0.079(20°C)
0.1(20°C)

0.0079(20°C)
0.102(20°C)
O.Ola(20°C)
0.029(20°C)
0.092(20°C)

0.043(20°C)
0.15(25"C)
0.016(25°C)






-------
       The  impoundment  sizes  chosen  are shown  in  Table  III-5.    The
  values for site and  impoundment parameters are  shown in Table ITI-6
  Small impoundments are usually not  aerated,  and  so the impoundment  at
  the  tenth  percentile  is  considered to  be a non-aerated' imuoundmer.t
  only.

       3.    Mass  Transfer  Coefficients and Emissions

  TT_ /Th* average,  high,  and low values  for  waste  parameters from Table
  IIi-4 were  substituted  into  the   relationship   for  Individual  mass
  transfer coefficients.   It was  found,  that  individual mass  transfer
  efficients  did  not  vary  greatly  with changes in  values  of  wasta
  characteristics  (within  only about one  order  of magnitude).   Since the
  primary   intarest   is   ralative  emissions  under   different  control
  situations, the  average  values for  the waste characteristics given in
  Xclu Ifi  XI X"*» v7-3 -r"a  I* & ~i*3 *•**  j — .TJ _ _ if..	  .  *  M  .  ..  ..  _       °
  coefficients.
T,t,,   TTT  ,          -,    	—  —- -=•-"-= *-.ia.i..3.<-i-st_3w_c5 given  in.
Table  III-4  wera used  to define  "typical"  individual  mass crarsfe-
         nfe
      The  calculatad individual  mass  transfer coefficiants  for  non-
 aerated  Impoundments,  aerated impoundments,  and  impoundments  w-th  a
 floating immiscible layer  are  shown in Table III-7.  These values  may
 be used ror most wastes with errors within one order of magnitude.

      Overall mass transfer coefficients and emissions, for X, -  1,  are
 shown in Table III-8 and III-9 respectively for a range of Henry's  Law
 Constant and vapor pressure-   In  non-aerated impoundments with H much
 less than around O.L atn-ft /Ib-mol, the waste volatilizes slowly at  a
 rate dependent  on  H.   The  gas-phase  resistance  dominatas  over  the
 liqu.c- pnase  (i.e.  gas-phase  controlled).   For  H much  greater than
 0.1 atm-rt /lo-nol,  tne volatilization is  liquid-phase  controll-d  and
 reaches a  maximum of  k,   for  wastes with  very high  E.    From  ~afaie
 L.J.-4,  very few  chemicals  have low values  for Henry's Lav Constant.
 The ^values tor   acetone   and  methyl  ethyl  katona  ara  around   0 5
 atm-rt  /la-owl..  3-3romo-l-?ropanol and dialdrin ara verv  non-volaf1-
 compounds   wish  Eanry's  Law  Constant  around  SxlO"-1  at— f tVb—

-------
                                            TABLE III-5
                                     SURFACE IMPOUNDMENT SIZES
                                     (Full  Capacity)  	(757, Capacity)	
                                      Surface
              Pereantile    Capacity    Area   Depth  Volume   Surface Area  Deoth
                             (ft3)      (ft2)     (ft)    (ft3)      (ft2)        (ft)
                          _  1,340     600      5     1,005        432       4

                50%         73,260   2xl04      9    54,945     16,635     7.6
§               90%          4xl05   3xl05     15     3xl06    259,112      12
i
g            Source:  Arthur D. Little, Inc.
                                            111-43

-------
                                TABLE III-6

                   SITS AND IMPOUNDMENT PARAMETER VALUES

  Site
  Wind Speed,  U ft/hr                          52,800
  Wind Speed at Surface,  UQ - 0.035 x U ft/sec  0.513
  Ambient  Temperature,  9  aC                        25
Impoundment

(At 75%-capacity)
Effactiva pool diameter, D ft
p
Effective deoth, H ft
o
Number of aerators
Diameter of aerator, D ft
Impeller rotational speed, u rad/sec.
Power to imaellar, ? ho
r *
Oxygen transfer rating of aerator,
J lb-02/hr-h?
Efficiency of power conversion, n
Oxygen transfer convection factor, a
Turbulent surface araa to turbulenc volume
Percentile of Impoundments
10Z 502
24.77 145.54
4 7.6
6
1.97
126
15.4
3

.73
.325
.09
90%
574.33
12
6
6
126
100
3

.73
.325
.0555
   ratio a  ft "
 Volume affactad  by aerators,  V ft3              -      3,119    39,710
   per aerator
 Effective surface  area  of  turbulent  zone,       -      1,704.0  13,236.0
   Aj  ft"  (x  number of aerators)
 Effective surface  area  of  convection  zone,*     -      14931.2  245376

 'Assuming that surface  impoundment is operating  at  752 capacity.
Source:  Arthur 0.  Little,  Inc.
                                tII-44

-------
                                            TABLE III-7





                     "TYPICAL" INDIVIDUAL k VALUES FOR SURFACE IMPOUNDMENTS


                                        WITHOUT CONTROLS
             Non-Aerated
                                         10%
                                    50%
                                                                     90%
1
I
Ib-mol/ft -hr      0.254
                   lb-mol/ft"-hr      0.654
0.205
                                 0.379
                                                0.177
                                                                  0.257
1
I
I
            Aerated
               k  Ib-!nol/ft2-hr
               1-   Ib-aol/ft-hr
                                0.42




                              703.53
                                                                  1.78
                                                                531.37
            Floating  lamiscible  Lavar
                           9

              k   lb-moi/ft~-hr      0.254
                                0.205
                                                                 0.177
           Source:  Arthur D. Little, Inc.

-------
                                            TAUl.li 111-8
                                              2

                    102
Vapor Pressure
 (Atmosphere)
        ''
   7X10
   7xlO~3
   7xlO~2
     0.7
     7

Henry's Law Constant
  (atiw-ft /Ib-moJ)
                          Non-Aururuil
50%
                                          90%
                                                               Aerated
                                                            50%
                                        90%
                                                                                      Floating Immiscible  Layer
                                                                                      10%
                                                                  50%
1.75x10"
                                                                                              1.44x10
                                                                                                     -4
                                                                                   1.75xlO~3  1.44xlO~3
                                                                                   1.75x10
                                                                                   0.175
                                                                                   1.747
                                                                                          ~2
                                                                1.44x10
                                                                0.144
                                                                1.438
                                                                       ~2
                                                                                                             90%
                       1.24x10
                       1.24x10
                       1.24x10
                       0.124
                       1.236
                                                                                   -4
                                                                                                                 ~2
It.
 V '
 JL'.
 fc
 ii:
10 J
I0~2
O.I
1
10
100
1000
10000
8.65x10"'
8.55xlO~3
7.65xlO~2
0.3726
0.6080
0.6490
0.6534
0.6539
7.11x10 ''
7.00xlO~J
6.00xlO~2
0.2474
0.3598
0.3770
0.378H
0.3789
6.11x10"^
5.99xlO~3
4.95xlO~2
0.1811
0.2467
0.2560
0.2569
0.2570
                                                         7.87x10"
                                       8.96x10"
7.76x10 J
6.09xlO~2
0.3702
1.777
12.64
48.80
68.97
8.83x10
7.85x10
0.4840
3.086
15.54
27.37
29.65

-------
                                             TAI1LE Ifl-'J
                        NJiJ''K< W ^^^                                            1 / lir )'
                               Non-Aerated
               Aerated
                                    50%
90%
50%
 Vapor Pressure
     (Aim)

        -4
-2
7x10
7x20
7x10
   0.7
   7
                                                                      90%
                                                                       Floating  Immiscible  Layer

                                                                        10%      50%         90%
                                                                               0.084
                                                                               0.844
                                                                               8.435
                                                                              84.35
                                                                             842.05
                                           2.392
                                          23.921
                                         239.214
                                        2392.14
                                       23921.418
                                       32.03
                                        3.203x10
                                        3.203x10'
                                        3.203x10,
                                        3.203x10'
                                                                                                   2
 Henry'u  Law Constant
   (atm-ft  /ll
IO-2
10
0.1
1
10
100
1000
1 0000
0.4169
4.1211
36.8730
179.5932
293.0560
312.8180
314.94
315.18
11 .8276
116.4464
998.1 120
4115.5485
5985.3450
6271.4704
6301 .41
6303.08
158.3174
1552.0809
12826.044
46925.18
63922.93
66332.67
66565.87
66591 .78
13.0919
129.09
1146.17
6158.35
29560.75
210268.93
811797.76
1147329.74
232.164
2287.96
20340.29
125410.21
799619.63
4026600.48
7091895.44
7682670.80
  Uaing  (X(  -X*)
Source:  Arthur I). Uttle, Tin:.
                                                                                                                        I
                                                                                                                        ti

-------
 impoundments,  all  the   controlling  parameters  are  aerator  relate
 except  for  ambient  temperature  and  Henry's  Law  Constant.   Th
 temperature  however,  cannot  be changed  by  in-situ control  withou
 impairing  the  effectiveness  of the  aeration treatment.   Henry's La
 Constant in this case can only  be decreased  by  pretreatment and/or b'
 limitation  and exclusion  of  volatile wastes.   The  alternative  1
 collection and post-treatment of emissions.   For the impoundment witi
 a  floating  immiscible  layer,  the   vapor  pressure  of  the  volatile
 component  in  the  layer and  wind  speed   directly   affect K  .   Thi
 effective pool diameter  inversely affects  X      Vapor pressure* can b<
 reduced  by pretreatment and/or  by  exclusion* and"  limitation,  or  b^
 decreasing  the temperature  of  the  impoundment surface.   For  ver]
 non-volatile   waste   (H  «   0.1    ata-fcj/lb-mol,   decreasing   tht
 temperature would reduce K    for non-aerazed  impoundments, but  most
 chemicals have  H  greater tnan  0.1   atm-ftJ/lb-mol.    In summary,  the
 controllable parameters  for each type of emission controls  is  shown ir
 Table  111-10.

     The  Henry's Law Constant  decreases with decreasing  temperature.
 At  any temperature,  the Henry's Law Constant  of  a  compound  is  the
 ratio  of  the partial pressure (P) and  the  solubility of "the compound
 at  that temperature.  The solubility could  increase or decrease  with
 temperature,  but the sensitivity of  solubility  to  temperature is  not
 as  large  as  that of  vapor pressure to temperature which are  related by
 the Clausius-Clapeyron equation:
          d In P              AH
                                 v
            d T             A Z RTZ

where:    £Z   -  1 for ideal gas (vapor)

          AH^  -  heat of vaporisation, (cal/aol)

          ?    •    vapor pressure (ata)

          5.    -  gas constant,  (cal/mol-'S)
          T    -  temperature,  (3I<)


     Neglecting  the  change  of   H   with  temperature,  the  simplest
solution to the above relationship Is:


          In ?  -  A -  3/T


     where    A and 3 are  constants;


              dHv    AH
      3  *    ITzSi *  -=p     (for  ideal  gases)
                                111-48

-------
                                ' TABLE III-10
                CONTROLLABLE PARAMETERS TO REDUCE EMISSION RATES
                      FOR CATEGORIES OF EMISSION CONTROLS

                              Q'  - KoaA (XL - X*>
           Parameter
                           Proportionality    Effective  on Impoundment Type
 Pretreatment
Mol  fraction  of  diffusing      direct
   component,  X.
Design

  Effective depth, H
  Effective pool diameter, D
  Wind Speed, U and U      P
  (by increasing freeooard)
  Surface area, A

Operating

  Temperature, 3
Wind speed, U and U
  (by increasing frieboard)

Surface area, A
In- Situ
  Temperature,  5
  Wind speed,  U and U
  Effective  pool  diameter, D
  Surface  area, A
                              H
                              U
   -.85
 o -.11
 p. 78
   .67
                            (1.024)
                                   9-20
U
U
                                  .78
                                   .67
                                  A
                            (1.024)
                                     3-20
                              u -78
                                 .67
                               •A
                                               aerated,  non-aerated,  float.
                                                 immiscible  layer
 non-aerated
 float, immiscible layer,non-aerated
 float, immiscible layer,non-aerated
 non-aerated
 non-aerated,  float,  immiscible
   layer
 non-aerated
 float,  immiscible  layer, 'aeraced

 float,  immiscible  layer, non-aeratad
 non-aerated

 non-aerated, float,  immiscible
   layer
non-aerated
float, immiscible layer, aeracad

float, immiscible layer, non-aeratad
non-aerated

float, immiscible layer, non-aeratad
non-aeratad, float,  immiscible
  layer
 Sourca:  Arthur D. Little, Inc.
                                 111-49

-------

       In ?l - In ?2  -



       Using an average


             P
                              8872 cal/g-mol and R =  1.9872  cal/mol-'K

                              T,-T,
                                          (T in °K)
                      exp  [4465  (T-^)/ (T^
      Neglecting   the   sensitivity  of  solubility  vith   temoeratu-e
 aenrv's Law  Constant  at TI  is  related to Henry's  Law Constant acT^
                   esp [4465  (T
                                                    (T in °K)
 VTV*  ^"5  "S «laciansrii?3  of  controllable parameters ^tamDaratur^
 ^nd .peed ana geometry^  to emissions, the reductions in amissiot- a-d
 "L   ;!:C1"S  °r   ChanSing   an7   °f  Che  ?«»»«•«  -era  calc^'at^
 Geometry  changes  vere  made  by  keeping   capacitv  cor.st=n-    ^
'!;r^rr:SS °: Ches.a, Ch,an?ss OQ "issicn  raductions from non-aerat-'
 and  -ioauing:xamisci.ola-layer impoundments  ara shcvn in F'*ur-s ^?-"
 ^1^  anc  :__-; cor che 5Cch percantila  impoundmanc.     "=     ---- '

     The figures  above  shov efficiencies  wichour  ra^acins them to -.»•
 controls.   Using  tht  medians  for  Henri's   Law  Constan-  and
                                                      ""
                                           s   aw   onsan-
pressure  (100  atm-flb-mol  and  0.07  «»   r^«ece?"?T)"  as-ors
reauctions  and  efficiencies  were  derived  for  'each  "7 the ^st-u
controls   as   described   belov.    The   emissions   r"duct?ons   an"
emciencies are shown in Table III-U.

          Rafts
     The efficiency of rafrs  is  approximately eoual to the pe-
area covered.  Vhite  Styrofoam rafts 4 s  8 faec,  0.5  and f
thick vera  chosen.   It  vas  assumed  thac  90  3ercant of  the
surrace area or an impoundment is covered  by  rafts  at anv time
                                                                    of

-------
 20
17.5
15
                  Float, limn. Luyor, 0.07 ami. v.|».
                  Non Acruiud. 100 iiliu (i3/IU inol
                                                                    Source: Arthur  D.  Little, Inc., 1984
                                              23                    22
                                                 Temperature (deg. C)

                               FIGURE 1113   EFFECT OF TEMPERATURE ON EMISSIONS
                                             (tiOih I'ERCENTILE SIZE IMPOUNDMENT)
21
                      20

-------
Efficiency %
                                                   '--^•'•^

-------
    80  __
    60  _

-------
                                                 TAHLE III-11
                         EMISSIONS M-mi
                                                                           CONTROLS
  Iri-Sttu Control a

Non-Aerated:
    Uafla
    Harr leva
    Floating  Spheres

 Floating  Immiscible Layer:
    Ituftb
    Harr lei a
     Floating Spheres
*
Uciluct Ions
(lb/yr)
10% 50% 90%
2.468xlOU
3.0l7xlO;
1.207x10°
2.468x10
6.655x10
8.l34xl05

6
9 r -,o/ IA10
4.948x10 5.234x10
6.048xI08 6.397x10°
2.419x10° 2.559xlOl°
4.948x10° 5.234x10
I.887xl08 2.529x10°
2.307xl07 3.089xlOa
9.228xl07 1.2 36x10°
I.887xl08 2.527x10°
Efficiencies
(%)
10% 50%
90 . 90
11 11
44 44
90 90
90 90
11 11
44 44
90 90

90%
90
11
44
90
90
11
44
90
                                                                                                                           '(•! 1
                                                                                                                           -"• t
* ll,, I „(. llemy's Law  Constant  - 100 alm-f t3/ Ih-mol , vapor pressure
  molecular weight = 100.08.  X -X  - I
                                                    '  '•)!!
  Source:   Arlhur 1). I.I tt le.  Inc.                   ;  ;l'i
                                                                       0.07 atm,

-------
 of  the  area  will  be  exposed  due  to  difficulty  of  cutting  the  Scvrofoam
 to  fit  the exact  shape  of  the  impoundment.  The percent reduction will
 be  assumed as  90  percent.   Additional reduction  may  result from any
 effects  on lowering  wind reiocity over  the  remaining open surface that
 are induced  by  the raft system.

          Barriers

     The reduction  of wind  speed over  an  impoundment  is  dependent  on
 the height:, length of  grid   ratio   (H/L).   Using  flat   Styrofoam
 (expanded polystyrene)  barriers  1x4 inch  in  a 8  x 8  feet grid  (i.e.,
 H/L =  1 inch/8  feet -  1.042 x  10   ),  Crow and Manges (1967) obtained
 11  percent  evaporation  reductions  in test ponds containing water.   It
 is  likely  that  the efficiency of a  barrier also  varies  with the  wind
 speed  above  the influence of  the  barriers.   An  11  percent  reduction
 was assumed  for   both   non-aerated   and  floating-immiscible-layer
 impoundments.

     The Crow and Manges  studies were  carried out on water reservoirs
 where  diffusion  is  controlled  in the  gas  phase.    The  relative
 effectiveness  of barriers   on  liquid  phase   controlled  impoundments
 would  depend on the  difference  in  dependence  on  wind  velocity in  the
 trjo regimes..   The  exponents on  the wind  velocity term in  the  t"o
 relationships used in this study are not  very different  (0.78 in  the
 gas film,  Mackay  and Matsuga; 0.67  in  the  liquid film,   Owens/Hwan?).
 To  the  extent   that  these   relationships  are  valid,   barriers   for
 impoundments should behave similarly to water  reservoirs.

          Shades

     The  efficiency  of  a   shade   in   reducing   emissions   from  an
 impoundment  is  proportional  to the percent shade of the material used,
 i.e., the amount  of  sunlight shaded out.   Woven "black"   polypropylene
 usad in  horticulture  is chosen  as  the  material for the shade.  IT. pan
 tests,    42   percent   shade  black,   woven   polystyrene mesh  reduced
 evaporation  of  water  by  44 percent  (Crow and  >fanges,   1967* .   The
 reduction  is  due both  to  wind  speed  and  temperature reduction.   Ar
 efficiency   of    44   percent   was  assumed    for  non-aerated   and
 floating-iraiiscibla-layer impoundments.

          Floating Spheres

     The efficiency of  floating  spheres is  approximately  equal  to the
percent area covered.  On a fully covered surface,  the  covered area is
91  percent.   According  to  vendor  literature   (Capricorn Chemicals'*,
efficiencies over  38 percent  have  been  obtained experimentally  for
open tanks.  An  efficiency of 90 percent was assumed.

-------
 >Vp->-£»x;-'i-~i'"1*~f-i. "-..^"••X-•-'**= ,.i'-*-'>*~- -S —f'- "-t^" "..-.--->  " -•-'_:-* '" - X:. ' -t-"1-'- <~ '-*.- •* " ''' ' ^'•'7--^-' y •J-"-^-•-•'•v •• -f'~ •*'••-*- ^.^—" :^J*.r:.-'. J^ ---^rgj^r^^a^aa^^ajSa
Vf-.--Jt7^:-;,>•-.-? 4—.  :  ^--"...--.  - ,^ _ :_^ ;-Y^;r .-1. ,.-.-"-r^^^;i^Jk^rlS^:^-^zi^^^^"'^"'^''^'''''r^'''*"*"
^v-^'JU^'vl^.-^rfjCr-vU^^'^'^^-'^- '	^*~-	^  ^J-'^J—«- -'
                            ?ost Treatment

                       The rate of emissions  is  affected by the collection  system since
                  Che collection  system protects the  impoundment  from  the  environment.
                  Emissions are  drawn out of  the system by  fans  tnrougn  a vent  to be
                  post—treated.
                  efficiency of 95 percent  and  afterburning at 98 percent.

                       5.   Costs

                            Pre treatment

                       Pr-t-earaenc  costs  taken from  Spivey  et  al  (198M  «ere in  the
                  o-der  o~* Tl 00 ?er  oound  of volatiles removed  from  a wastastream
                  %WO/W.  Cost's for pretraatment  depend  «- «»taStr.ao prop.rc,-s
                  rr-atmen-   trrpe,   system   design   and  size.    .he   cosu  va^ae  cnosar
                  presented Ihe  Jnge  of most  pre-treat,ent  technologies  wxth,n  a
                  factor of  2.

                             In-situ Controls
                                                        "
                   TTT_"I   xhe  rationale used  in  obtaining material,  instaj.-at.sr
                   ooiracicn/xaiacacaaca  costs  for  each  technology i5 dascnoeu ^^
                                  Rafts
                        TWO   thicknesses,   0.5   and  1.0  inch  of ^,:panded
                                ve->  chosen for  the  costing  or  rarts.
lation  costs  are  expected  to  be  re.
   is  si-^e,  involving   little  labor  in  cloating  the
                     n«alcton   s  s-e,
                                          "
                              ss rr^st.

                    1-inch thick 'Scvrofoam panels  ara used.

-------
                                            TAIJUS 11 r-12
            UNIT MATEKTA1. COSTS  FOIl SUUFACE IMPOUNDMENT EMISSION REDUCTION 1N-SITU TECHNOLOGIES
                              (Dollars per  Square  Foot,  Summer  1984  Dollars)
EPS
Sheets
       Size
   4'  x 8'  x 1/2"
   4'  x 8'  x 1"


EPS(1) Strips (8'x 8'  grids)

       Size

   4" x 8'  x 1"
   4" x 8'  x 2"

   8" x 8'  x 1"
   8" x 8'  x 2"

  12" x 8'  x 1"
  12" x 8'  x 2"
                                  10th Percentile
                                       0.08
                                       0.13
                                                   50th Percentile
                                                       ($/ft2)
                                                        0.06
                                                        0.12
                    90th Percentile
                        ($/ft2)
                         0.05
                         0.10
0.04
0.08
0.08
0.17
0.13
0.25
0.04
0.08
0.08
0.15
0.12
0.23
0.03
0.06
0.05
0.11
0.08
0.17
Shade Cloth
           (2)
   Percent Shade

        21%

        57%

        92%"
                                0.07

                                0.11

                                0.20
0.07

0.10

0.18
                                                                                         0.07

                                                                                         0.09

                                                                                         0.17
(1)  Expanded polystyrene
(2)  Woven "black" polypropylene

-------
                                           TAIll.E 111-12 Continued
                             (Doll art, per Square Foot.  Summer 1984 Dollara)
Spherea

  Polypropylene

     Diameter  1  3/A  Inchea

     Diameter  6  inchea


   High Denslcy Polyethylene

      Diameter 1  3/4 inches
                                   10th Percent-He
7.55
                  50th Percentlle
                      (I/ft2)	
                        6.75
                                                                                    90th Perccntile
6.55
U.69
5.05
7.50
4.65
7.50
                                                  6.75
   Snurcea: Hcllabl e Pluatlcu, NewatU, N.I. 1JBA
            X. S. Smith Company,  Kalonlown. N.I. 1 ->»"
            Capricorn i:liemU-ulu Corporal ion, Secaucua.  N.I,  J

-------
In-Sltu
                     ANNnAL
                      TAHI.E 111-13

   V'OR SUIU-'AEH TMPOUNDMKNT CONTROLS.  $/YR  (Summer  1984  Dollars)
   Kafts
   Barrlers
   Shades
   Floating Spheres
I'oat-Treatment
   Collection
              **
jOth Percent lie

38.56  -  62.66
      19.28
      53.02
514.00 - 682.00
50th Percentlle

  998.11  -  1996.22
         665.41
        1663.52
13672.00 -  20305.00
                                   24000
90th Percent lie

12955.60  -  25911.20
        7773.36
       23320.08
196087.00 - 316270.00
                                                                                               250000
I
»':f
 *' J
 u- •
 ii
ViJi

I
 i
   Installation, 0 and M, and other costs not Included.
   Treatment costs are variable costs depending on the amount of
   emissions treated.  These costs are discussed In the  text.  The
   coats shown here Include basic structures and installation.
                                                                                        f:':
                                                                                        B ..'
   Source;   Arthur n.  Little, Inc.
                                                                                                                        j
                                                                                                                       I

-------
                                             TAHl.E
                        UK I .AT I VJl J MSTAI ^XJU

                                          OF IN-STTU CONTUOI.S
                                                                                                                       I
                                             Installation
                                                50%
                           90%
                                                                              Operation/Maintenance
                                                                          10Z
                                                    50%
                                                                                                  90%
Uaftu
  0.5-1 inch Styrofoam
Low
             Lou
                          Low
                                      Lou
                                                   Lou
                                                               Lou
Itarrlera
  a1 x 8' grJda of Styrofoam
  atrJps

Shadea
  Black woven polypropylene
Medium
                                               High
                                                   .
                                                Hlgli
                          High
                           High
                                                                         Lou
                                                                         Lou
                                                                                     Lou
                                                                                     Low
                                                               Lou
                                                                                                  Low
   I'olypropylene/IIDPK
                                   Lou
                                                Lou
                                                             Lou
                                                                         Lou
                                                                                      Lou
                                                                                                  Low
Source:  Arthur  D.  Little,  Inc.

-------
                Barriers

      A 8  x  8  feet  grid made  of  Styrofoam strips  4" x  8'  x  1"  was
 chosen for the costing of barriers.   The barriers may be 4 inches or 1
 inch high.  These barriers are expected  to  last  a year.   Barriers  are
 expected  to  entail  relatively high  installation  costs  because  the
 Styrofoam strips  have  to  be  constructed  into  a  grid formation  and
 installed en  the impoundment  surface.   For  small impoundments,  the
 grid is small  and  consists  of  relatively few  strips.  The  design  and
 installation  of  the   grid  may  be  relatively   easy.    For.  large
 impoundments,  the design and installation  of  the grid may have  to be
 sub-contracted and will be  expensive.  Operation  and maintenance costs
 are  expected to be low under  normal  conditions.  However,  strong winds
 may  effectively destroy a grid.  Heavy snow may  also  damage  the  grid.
 The  volume of  Styrofoam generated that  have  to  be disposed is  lower
 than in the  case of  rafts but  is  another element of  the  costs  in  the
 use  of wind  barriers.             - —

                Shades

      Black woven  polypropylene shade cloth used  in  horticulture   is
 chosen as the shade material.  There  is  not much difference in  price
 within a small variation of  shade value so the  cost  of a 57 percent
 shade value  is used for that of a 47  percent  shade value of the same
 material.   The   installation   costs   of  shades  are  expected   to   be
 relatively high.   For small impoundments, the  shade  may be stretched a
 few  inches over the impoundment and  secured at the  edge.  Shade  cloth
 is sold in pieces and  pieces need to be sealed  together  to obtain  a
 large enough  piece  to  cover  impoundments.   Larger impoundments  may
 require   the  use  of  floats  spread  out  over  the  surface  of   the
 impoundment  to prevent  the shade  from dropping below the impoundment
 surface.   In horticultural  use,  the  shade  cloth  is  used for-  the  3
 summer months  and lasts  between 7-9 years.   For year around use over  a
 surface  impoundment,  the  lifetime  is  estimated to  be  between  1-2
 years.   Operation and maintenance  costs  are expected  to  be  low under
 normal conditions.   However,  strong   winds  and heavy  snow may damage
 the  shade  or cause  the  shade  to drop below the  surface.  The volume  of
 shade  cloth  that  needs  to be disposed of  at  the end  of its useful life
 is smaller than in  the  cases of rafts or  barriers.

               Spheres

      Polypropylene  spheres of diameters  1-3/4  inches and 6 inches  are
 used  to  provide  a  range  of  costs   for  spheres.   The  polypropylene
 spheres are  cheaper  than the  high  density polyethylene (HDPE) spheres
 for  the  same   size   spheres  and   are  available  up  to 6 inches  in
 diameter.  HDPE  spheres are  available in only  one  size  (1-3/4  inches
diameter) .   Installation   costs   of  spheres  ara  expected   to  be
 relatively very  low.   Depending  on  the chemical(s)  present in   the
 impoundment,  spheres  are expected  to  last a  relatively long  period  of
use.   An estimated lifetime of  10  years was  used to annuaiiza costs  at
 10 percent per  year.   Operation and  maintenance costs  are  expected  to

-------
be ve-y low, or zero.  The volume of spheres that need to be disposed
of per  year  and at the end  of  its  useful life  is  much  smaller  than
Sytrofoam barriers or rafts.
          Post-Treatment
     Costs for oost-treatment consists of the costs  for  the  collection
svstem  and the' treatment.   The  collection  system  cost is  a  fixed
an^a!  cost  for the design  size as shown in  Table «^-  tt"  «£
was  estimated  by Air Structures International,  Inc. (Tappan, NY)  .or
^o  air structures covering 17,000 square feet and 260,000 square feet
corresponding   to   the  50th  percentile  impoundment   and   the   90tn
pe"entile  impoundment  respectively.   The  10th  percentile impoundment
was  too  small for  the  installation  of  an  air  structure.   The  a .
structure for  the 50th percentile impoundment was I/O  feet ,l°ng.  100
feet wide and  36  feet  high made  of  translucent  rabnc wita a  cable
system  ard anchors for support.  It has an  exit  door and an entrance
door  a  "10^ BTU  heating  system,  a  24,000  W  lighting system  ana  a
vehicle  air   lock  system.   The  90th  percer.tile  impoundment  .«
 structure vas  260 feet wide, 1,000 feet long,  and  /5 ieet  high, made

   ;ra±r^^
  1 wers3.*  Th°e Bating sys'tem was  a  12.5 *  L0ff  BTU  *«-   ^.'J"
 lighting ar.d  the  vehicle  air  lock system were not  estimate because
 these  varied   greatly  depending  on  the  requirements.   Installation
 costs  we~e estimated  to  be   between 31-2  per   square root,  wnich
 includes foundations.  For  this  analysis,  installation «s estimated
 to  be  SL.50   per  square  foot.   The  costs  snown  do  not Delude
 maintenance (which is low)  and  energy costs.  Costs ror  the co.lec ion
 system are shown  in  Table  III-I5  with costs annualizec at 10 pe.ce..t
 in  LO years.
       -eat-e*"-  costs  are  variable  costs   dependent  en   the  total
        ns Veated.   To   estimate  the  treatment  cost  per  pouna  or
       ons  removed,   a  10,000  cubic  feet  per  minuta   wastestrean
     a'-ning  50 oom  trichloroethylene  was chosen  as  a raprasencate
         through 'the post-treatment  systam.   Tb. emissions  tr.r
  system would  be  around  10,000  pounds  of  ICa  per  year.   _ An-uai
  ^stalled  capital costs for both  carbon  adsorption anc  ar.a.su. .
  Gere  at  least one order of magnitude lower than annual operating  cos.,
        198").  Total  installed  costs  for carbon  adsorption was  a3/,00u
        ed to an  annual operating cost  of 3870,000.  Total  instaliec
        'or  afterburning  was 3230,000  and annual  operating  cost was
  costs
                                  S45'and sVo "respectively (SlOO.OOC/Mg
  ar-e-ou—e-s ara'also less  expensive  than  non-catalytic  systems.   If
  these 4o "roes of post-treatment systems are included,  the treatment
  costs for post-traaLent would be between 35-10 per pound TCE ramovea
  (311,000-22,GOO/MS).

-------
                              TABLE III-15

                   CAPITAL  COSTS  FOR  COLLECTION  SYSTEM

                FOR POST TREATMENT  (Summer  1984  Dollars)


                         50th Percantila        90th Percentila

Structure                     70000                985000
Heating                       24500                175000
Lighting                      15000            Not estimated
Air lock vehicle         15000  -  24000       Not estimated
Installation                  25500                390QQQ
     Total                 " 150000              "IbUUOOO

Annualized                 *  24000              ' 250000
(10%, 10 years)
Source:  Air -Structures International, Inc. Tappan, NY, 1984
                                111-63

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      6.   Cost-Effectiveness of Controls

      Table 111-16 expresses the cost-effectiveness of in-situ controls
 in terms  of the  cost  per  percent  of reductions  per square  foot  of
 impoundment.  Figure III-6  illustrates  these values  on a  graph  that
 compares the cost-effectiveness  with impoundment  size.   Each  sat  of
 points  represent  the  effectiveness  for   the  10th,  50th,  and  90th
 percentile impoundments.   The  figures show  some slight economies  of
 scale.  Of  the  in-situ controls, rafts appear   to be the most  cost-
 effective.   Shades are more  cost-effective than barriers in  terms  of    	
 the pounds  of  emissions  reduced.   Floating spheres are  the  least
 cost-effective   of  the  in-situ  controls.   When   installation  and
 operation/maintenance     costs     are    included,    the     relative
 cost-effectiveness  ranking  of   in-situ  controls  will  not   change,
 because  rafts   have low   relative   installation  and  operation  and
 maintenance  costs.  Shades and barriers have higher values for  these
 costs  but the material  costs for  spheres ara so  much higher that the
 relative cost-effectiveness  of  spheres  is  still expectad  to  be the
 lowest.

     Figurss  III-7 and  III-S show the  hyperbolic  functions relating
 cost  per pound of emissions  reduced  or  ramoved  to  the  throughput  of     """""
 volatiles  per year and  the total pounds  of  volatilas  ramoved per year      ""_
 respectively. 'The horizontal curves  represent  the pretraatment cost
 per pound of  volattiles  ramoved.  There are  some economics of scale for  '-/. ^A^
 pretraatment, but  these have been neglected.  Each  of the hyperbolic  -"- - ^—
 curves are at a  constant  annual cost of  in-situ controls.  The curves          ;
 for post- treatment are  not shown  because  collection  and  treatment
 costs  for post-treatment  ara very high and are over  in  the  top right          '=
 hand  corner  of  the  figure.  For  the most  part,  the  post-craacment
 curves do not appear within Che rang a of Che other ccr.trol.5.

     Figura   III-7   incorporates   the  efficiency  of  each  control
 technology by considering  the throughput of volatilas.  On the bottom
 left   of  the   figure   whara   the   horizontal   linas   represer.tir.s
 pretraacment  ara below  and  to cha  left of  the curves, ?ratreatment is          I
 more   case-effective.   Whara the  horizontal  curves  ara  abova  cha          ;
 hyperbolic curves, the  in-situ  controls  ara  more case-erfactive.   As
 aay be seen,  pratraattient is mora cost-effective for small svstams,         ~-
 i.e.  low emissions  reduced  and  low  throughputs.  In a medium  siza          :
 impoundment,   at  pretraatment  costs  of   S2.00  per pound  removed         ^
 ($4,£00/Mg) or less,  throughputs of less than 1,000  Ib per year would          l
 favor  pratraatmant.   At   higher   throughputs  of  volatilas',  in-situ         2
 controls ara  more  cost-effectiva.   In terms of throughput,  rafts  ara         ,i
 still  the most cost-effective of the  in-situ  controls  and spheres  ara         ^
 the  least.   Shades  when  compared  in tarms  of   throughput' ara  more         S
cost-sffactive than barriers.   This  same .comparison  of  effectiveness         5
applies  to small and large  impoundments as  well.  Unless  pratraacment         f
costs  for a  wastastraam ara extremely low  (much  less than $0.50  per         J
Ib), in-situ  controls  ara  generally  more   ccst—affactive  of all  the         I
controls.                                                                      J.
                                                                              fS-

-------

                                                                           ; -t^ f~:' • i rv-i"* -•
                               TABLE 111-16

                     COMPARATIVE COST-EFFECTIVE^

                     FOR  IN-SITU EMISSIONS  CONT^nTg
 Rafts
 Barriers
 Shades
 Floating Spheres
                                    Z Reduction
                                                per  ft2  ($/ft2)
                             8.9  -  14.4
                               36.4
                               25.0
                             118 -  157
  (xlO"4)

 6.7 - 13.3
   36.4
   22.7
91.3 - 136
5.6 - 11.1
   27.3
   20.5
84.1 - 136
ara annualized  for ,Dhea at
of installation, 0  and M   and othJr
the relative cost-ef?actlvenes^  rc
see text.)            ^-tiveness  ranking
                                                          S'  C°SCs
                                                 year3' The inclusion
                                                  aX?eC=ad C° ch«Se
                                          r each technology.  (pie=se
Source:  Arthur D. Little, Inc.

-------
Rafts      Barriers      Shades
                 Controls
                                                               Spneres
'Only material costs are used. Installation
 0 and M, and other costs are not included.
                                            SURFACS .MPOUNDMENT CONTROLS'
                               lii—OO

-------
n
H
M
                                                                                                             Post-Treatment, p = $45/lb
                                                                                                             Carbon Adsorption
                                                                                                             Post-Treatment, p « $16/lb
                                                                                                             Post-Treatment, p • $5/ll>
                                                                                                             Adsorplion wild ReQeneration
                                                                                                             Pretreatment $2/11
                                                                                                                 0
                                                                                                                 Pretreatment
                 10
                 Source:  Arthur I).  UiLlu,  Inc.,   1984
                                FIGURE III 7
                                                                     ™ SURFACE .MPOUNDMENT CONTROLS VERSUS THROUGHPUT

-------
                                                                                                                          I
                                                                                                                          I
                                  111 rtnlucutl (removud) per
Sonrct-:  Artliui- I). I.I I Lie, liu:.,  1'JH/t


          FIGURE III 0    COST EFFECTIVENESS OF SURFACE IMPOUNDMENT CONTROLS

                        VERSUS REDUCTION

-------
      Figure III-8  shows  the  cost-effectiveness  picture for  various
 annual costs  and  a  wide  range  of  pounds  of volatiles  reduced  or
 removed per year.  Each of the hyperbolic curves  represents  an annual
 cost.   As an example,  for an  in-situ  system  that costs $1,500 annually
 and if pretreatment  is $1.00  per Ib  ($2,200/Mg),  a removal  rate  or
 reduction of emissions of greater  than 1,500  Ib per  year would  favor
 the in-situ control.   If pretreatment  cost was  increased to  $2.00  per
 pound  ($4,400/Mg),  a  rate  of  greater than  about  800 Ib  per year
 reduced (removed) would  favor  the in-situ control costing $1,500  per
 year.   The $17,000  annual  cost   curve  which  corresponds  to  using
 spheres  in  a  50th  percentile   situation  illustrates the  point.
 Floating  spheres  in this  impoundment  would be more cost-effective than
 pretreatment if  the emissions  reductions achieved  was more  than 17,000
 Ib  per year and pretreatment was  $1.00 or more per  pound  ($2,200/Mg)
 of  volatiles removed.

 E.    Summary

      In-situ controls  are  generally experimental and  in  many  cases are
 taken  from  some  other  different kind  of  applications.   For example,
 rafts   were  experimentally  studied   in  reservoirs  as evaporation
 controls.    Spheres  are  more   directly transferable  than  the  other
 in-situ  controls,  since  they  are used  in emissions   control  from
 treatment  tanks.    On  the whole,  data on  in-situ controls  are  very
 poor.   There also  appears to  be  limits  on  the use  of some  in-situ
 controls  on large impoundments.

     In any in-situ control,  there is  some  point  at  which  it becomes
 more  cost-effective than pretreatment.  This  tradeoff  point  is  very
 sensitive  to pretrsatment costs.   For a small change  in  pre-treatment
 cost,  the  trade-off point  will  shift  relatively far to  the  left  (with
 greater pratreataent  cost)  or  to the  right (with smaller pretraatment
 cost).  Estimates of  emissions  from uncontrolled surface impoundments
 are  of the  order of 300,000  metric tons per year  (GCA, 1982).  This
 reference   also   estimates  that   thera are about  2,000   operating
 impoundments.  On the average,  then,  emissions ara  about  ^00  metric
 tons per year per impoundment.  At  this rata, in-situ  treatment should
 be considerably more cost effective than pretreatment.

     Post-craatment,  including  collection  and  treatment is  the  most
 expansive control technique.  The curves for post-traatment  would fall
 above  and  to the right of  the  in-situ controls in Figures III-7 and
 IIT-3.  If   the only  concern  is the  rate  of reduction  of  emissions,
 post-treatment would  never be  cost-affective.   However, if  thera  is
 concern  about the  absolute  level of  removal,  the  tradeoff  to  be
 considered is between pretraatment and post-traatment.  Post-treatment
 is  more  expensive  than  pretreatment  for  each  pound   of volatiles
 removed primarily because very dilute  mixtures in. a gaseous  medium ara
 treated.  For example, for carbon adsorption  assuming no  regeneration,
 the cost per pound  (not including  collection) post-treatad  is $45.   A
regenerative system would cost  around  $5 compared  with a regenerative
carbon  adsorption pretraatment  of  around  $1  per pound.   If,  however,

-------
                                        -CTJ.^4&;£4S^
 the waste  cannot  be pretreated,  post-treatrient may be the only way  to
 remove  volatiles  even though the cost is between.  $10  - 50 per pound,
 excluding  collection  coses.   If  there  is  a market  to   encourage
 recovery  following post-treatment,  this  alternative may  become  less
 expensive.    Also,  the   post-treatment   alternative  may   be   more
 attractive if, as  in the Upjohn case, the volatiles can be replaced  in
 a  treatment impoundment.

     If  the  design objectives offer  any  flexibility,  there  may  be
 opportunities  to  reduce  emissions  by  altering   the1 design  of  an
 impoundment.   Operating  procedures  also  present  possibilities   in
 emissions reduction.
F.   References

Air Structures  International,  Inc.   Tappan,  NT.   July 1984.  Personal
Communications.

Bartholic, J.F., J.R. Runkles, and S.B. Stenmark.  1967.  Effects of a
Monolayer  on  Reservoir  Temperature and Evaporation.   Water Resources
Research, 3:173-179.

Beraett,  U.K.,  L.A.  Halper,  N.C.  Jarvis,  and  T.M.  Thomas.   1970.
Effect of  Adsorbed  Monomolecular  Films  on  the  Evaporation of Volatile
Organic  Liquids.   Industrial and Engineering  Chemistry Fundamentals,
9:150-156.

Breton,  H.  et al,  1983.  Assessment  of Air Emissions  from Hazardous
Waste  Treatment,   Storage,  and   Disposal   Facilities   (TSDF's)
Preliminary National Emissions Estimates  —  Draft Final  Report  - GCA
Corporation  for  the  USEPA.   GCA Resort  No.  GCA-TR-33-70-G  fAu*ust
1983).                      "  *

Capricorn Chemicals Corporation.  Secaucus,  NJ.   June  1984.  Personal
Communications.

Cluff, C.3., 1967.  Rafts:  New Wav to Control  Evaporation.  Crops and
Soils >!agazine,  20:7-9.

Crow,  F.R.  and  H.L.   Manges,  1967.   Comparison  of  Chemical  and
Non-Chemical  Techniques  for   Suppressing  Evaporation   from   Small
Reservoirs.  American Society of  Agricultural Engineers, Transactions,
10:172-174.

Crow,  F.R.,  1973.   Increasing   Water  Supplies  by  Suppression  cf
Reservoir  Evaporation.   OWRR  A-I04-OKLA.    Oklahoma  Water  Resources
Institute, Stillwater,  OK.

Shrenfeld, J. and J.  Bass.   1983.   Handbook for Evaluating  Remedial
Action   Technology  Plans.    SPA-6CO/2-33-076.   U.S.   Environmental
Protection Agency, Cincinnati,  OH.

-------

                                              '                       ~
 Federal Register.  May 19, 1980.   Vol. 45, No. 98, D.  33075
                          '
    ;'                -     ;~r  •••<••«
for Che D.S. Environmental  Protection A/»    'a"/-  Re'orc-   ?reparad
Washington,  D.C.            "election Agency, Ofrice of Solid  Wasta,
                                         Und  Oi
                                                        facilities.
              s,  Presented at  1984
   I»«l»« of Chemical Engineer'^
                                ^
                                          Coerflclent5  for Surface
                                               , =££? ', ,
                    ' on
   Enginearing,. 51:434-439.
                                              Journal of Chenical
                                                     ta« tavers.
     .  8.   P
            argacon Press
                                          AIr
                                                       Pollacion
      r»cin. University of Arnsaayet


              tics.  ;:e,ar,, „.   ;une IM4.

             v   /*• o  TT- •

              Vloci;'FrS--m>  '"'  '  G
 Missions."   ,e?rint
                                            ,er  Coe.icie

                                         i  e, If"""'
 Air  Pollution  Control  Techr-'
 Triangle  Institute,   •.M^'.
 — Cental Protection Agancy,  rai.-
                                       -  "  -«-««=•.«« as an

                                                   *-   Je3e"=h
                                                   '  ""  B-S-
              rocengs
*«er V**.   Chicago, Illinois   L7
       Cheaical Corporation,"
Personal Conmunicanions.
                                          Confa«a"


                                  n   r
                                   '  Connecticut.   April  1984.

-------
U.S.  Department  of Health,  Education, and  Welfare.   1970.   Control
Techniques  for  Hydrocarbon   and  Organic  Solvent   Emissions   irom
Stationary  Sources.   National  Air Pollution  Control  Administration
Publication No.  A2-68.  .U.S.  Department  of  Health,  Education,  and
Welfare,  Public   Health  Service,  Environmental  Health   Services,
National Air Pollution Control Administration,  Washington,  DC.

U.S.  Environmental Protection Agency.   1978.   Control Technologies for
Volatile Organic Emissions from Stationary Sources.   EPA-450/2-78-022.

U.S.   Environmental   Protection  Agency.    1980.   Lining   of   Waste
Impoundment and  Disposal  Facilities.   SW-870.  Office  of  Water and
Waste Management, Washington, DC.

U.S.  Environmental  Protection  Agency.   June  1982.   Handbook  for
Remedial Action at Waste Disposal Sites.  EPA-625/6-82-006.  Office or
Emergency and Remedial Response, Washington, DC.

U.S.  Environmental Protection Agency.  July 1982.  Draft RC3A Guidance
Document   Surface   Impoundments  Liner  Systems,   Final   Cover,  and
Freeboard Control.

U S.  Environmental Protection  Agency.   September  1982.    Closure  of
Hazardous Waste  Surface  Impoundments.   SW-873.   Office of  Solid Waste
and Emergency Response,  Washington, DC.

"W.L.  Gore  and  Associates,  Inc.   Nevark, DE.   June  198*.   Personal
Communications.

X.S.  Smith  Co. Eatontown,  MJ.   June 198*.  Personal Communications.

-------
                          IV.  CONTROLS FOR TANKS
  A.    Tank Description
       1.    Definition
             means  a   stationary  device,  designed   to  contain   an
  accumulation of  hazardous  waste  which  is constructed  primarily  of
  non-earthen materials  (e.g.,  wood,  concrete,  steel,  plastic)  which
  provide  structural  support (Federal  Register, May  19,  1980).

       2.   Types,  Construction  and Uses

       The  types  and construction of  hazardous waste tanks are  similar
  to  those used  for  the  storage  of  petroleum  liquids.  The  types  of
  tanks  are:   open  tanks,  fixed  roof  tanks,  floating   roof  tanks,
  variable  vapor   storage   tanks,  and  pressure  tanks.   The  minimum
  accepted  standard for storage of petroleum liquids is the fixed roof
  tank.   In  the  hazardous  waste  area, open  tanks  are still  in  use.
  Since detailed  descriptions  of tanks may be found in several readily
  available  sources (U.S.  EPA,  1977;  U.S. EPA,  1978;   U.S.  EPA, 1980;
 American Petroleum Institute,  1962;  196^; 1980), we will only describe
  them briefly here.

      Open Tanks are essentially  tanks without a roof.  Concrete-lined
 basins are  by definition considered  tanks (Federal Register,  May 19,
 1980).  They are examples of open tanks.

      Fixed Roof Tanks have a fixed  roof  equipped  with   some  type  of
 vent.

      Floating Roof Tanks consist of  tanks with a roof  that  is  frae  co
 float  on  the  surfaces of  the  stored- waste.   External floating"roofs
 are  exposed en the surface.  Internal floating roofs  are covered  by  a
 fixed  roof which protects the roof  from the weather.

     Variable Vapor Storage  Tanks work  by storing  expanding  vapors
 emporarily  in  a  gas  holder.  Venting  occurs  or.lv when  the  holder
 capacity  is  exceed.   During  periods  when  vapors  are contracting, the
 stored vapors are  transferred back to the  storage tanks.

     Pressure Tanks  can  withstand  higher pressure variations befor»
 incurring  emission losses.

     Tank  material,   configuration  and  auxiliary   equipment  must
 correspond to and  be compatible with  the  stored waste. "  Materials of               11,1.1
 construction   include   carbon   steel,   stainless   steel,   corrosion               Jf
 resistant  alloys,   aluminum,  concrete,   or  fiberglass   reinforced           '    l'
 plastics.  Tanks vary widely in configuration,  fabrication techniques
materials  and operating  conditions.   Small tanks  (between 1,300  to
 -1,000   gallons)  nay   be  shop-fabricated.    Larger   tanks   ar=
 rield-erectad (Corripio et al,  1982).

-------
                            .       tothoe  .
tte uses of tanks  are  very  simlai  w  tt       o£ uasces.   Besides
except  that  tanks «.  ««   «7otto treatLr.t   by   biodegradation,

nentraUzatiofoxidation, anons *any other  uses.

     3 .   Operation

         operations  of                     "
     ^  operations  of -*"" ddld"^?  «U  S2(
treatment   tanks,  reaSents  ««7  be  ^  'Each tank has  a  specified

        •£ SS.'Lp'SSS^'S^* - » - — al"ldy
contained in the  tat*.


                   of

    ,
 treatment.  The influent  could be            ^
 Lsta  could be added from ^"^f^^^'cank per year is called
 T^e total volume or wasta processed  thro S            ^^  by  tha
 the throughput  per year. ,   Tht  ^       £ tiEes per year vastas
                                 c                            ed *.
 turnover rate.

          ,    A  of  their lifetime,  or when  operations  have  ceased,
      At the end  of  tiieir *•->•*—  '
 tanks are disassembled ana disposed o..


 3.   Emission Sou~^ and y.odels_


      !.   General Description of Factors Affecting Emissions
       ^ssicns to the atmosphere occur when the

  or its  contents withdrawn and  aiso wai-e .n- -an.  -


                          i c-» i •.•-flCJ on  is dependent on tn«

           rata of_jw*a"*70^."tVa"ts"  and  the  surrounding
                    -
  those affectir.g wasta volati^at on ^n  ^          a i=?ouadmenc  but
  r^eatad hera.  in open c«.c - J^^id surfaca due  so  che  higher
  vith  a  very  low w-nd speed     £ -jj^^ of wks .   Please rarer
                                 s for a =ore  detailed  description.
        H«d roof tank emission  losses are due to:
             (breathing losses),  and
                                   17-2

-------
     o    vapor  displacement due  to  filling  and  emptying  (working
          losses).

     Floating roof  tank emission losses are due to:

     o    losses due to  imperfect  fit of the  seal  and  losses through
          the  gap   between  the flexible   seal  and  the  inner  wall
          (standing losses),  and

     o    losses due to  the  vaporization of the wet  tank  as  the roof
          decends when the tank is  being emptied (withdrawal losses).
     2.   Emission Models

     The relationships  describing  emissions from tanks  are described
in  GCA  (1983).   For   comparison,  the  base uncontrolled  case  will
consist  of  two  different  uses  of  open  tanks;   storage and  aerated
treatment.  Each of the different roofs (fixed roof and floating roof)
will be  considered  as  a  control alternative.  The  relationships  for
the  latter  type  are empirical.  The  models for emission losses  from
open  tanks  are  the same  as  those  describing  surface  impoundments.
Table IV-1 summarizes these relationships.

     The definition of  each of the parameters  in  these  relationships
is shown in Table IV-2.

     3.   Parameters That Control Emissions

     The rate  of emissions  from an  open tank depends on the  overall
mass transfer  coefficient,  the exposed  area,  and  the concentration or
mole fraction  in the waste.  These are the same  factors that determine
the rate from  surface impoundments and are not repeated here.

C.   Potential Controls

     1.   Summary of Applicable Controls

     The categories of  potential controls are similar to those used in
surface  impoundments:   pretreatment,  design and  operating  practices,
in-situ  controls  and  post-treatment.   Each control  will  be described
under  these approaches  in terms of  their  mode  of  action,  expected
effectiveness  and  related  costs.  Only those approaches not  already
covered in surface impoundments will be discussed in detail.

     2.   Pretreatment

     Pretreatment basically removes the volatile components  of a waste
before it  is  put into a tank.  A detailed  discussion is  given in the
Surface Impoundments chanter.
                                17-3

-------
                                    TA3LZ IV-L
                 RELATIONSHIPS DESCRIBING EMISSION  LOSSES  IN TANKS
OPEN STORAGE;       Please see Surface Impoundments, Non-Aerated





AERATED;            Please see Surface Impoundments, Aerated





FIXED ROOF TANK:





            Losses  »  Q. »  L, +  L
                       xi     a     w
Breathing;  L  -  2.26 x 10~2 K  .   P   °-68 D  L-73 H °'51 AT  °'5°  ?  CK  lb/vr

                                                                              '
Working:    L   -   7.56 x 10"4 M P K»  K  Q  Ib/y
             W                       *i   C
FLOATING ROOF TANK:
            Losses   =  Q.  =   L  •*••  L
                        i      s      v






Standing:    L   =     K V^  ?*  D '1 K   E   Ib/rr
              S3             c   r
Withdrawal:  L   -   (0.943) Q CT WT  Ib/yr
              w                 i.  u

                           D



 Source:   American Petroleum Institute
                                                                               1

-------
  PARAMETER
                               TABLE IV-2
               PARAMETERS FOR TANK EMISSION RELATIONSHIP?

                         DEFINITION
Waste;
M            Molecular weight
P            True vapor  pressure at bulk  liquid
Kc           Product factor
P  (also     Vapor pressure function
environment)
CL (also     Shell clingage factor
    tank)
 WL

 Tank;
 D
 H
 N
             Average organic liquid density
             Tank  diameter
             Average vapor  space height
             Point factor
             Adjustment for small diameter tanks
             Turnover factor
             Seal factor
             Seal related wind speed component
            Secondary seal factor
            Average  throughput
            Effective  depth
            Exposed  surface area
Site (Environmental);
v            Average wind speed
AT
8
           Average ambient diurnal temperature change
           Average ambient temperature
         (P/PA)
                                                               UNITS
                                                           Ib/lb-mol
                                                             psia
bbl/1000 ft2

lb/gallon
   feet
   feet
                                                            bbl/vr
                                                            rear"
                                                          mph
      [1  + (I-?/?.)0'5]2
                 A

   where  ?A  =.   average atmospheric pressure  =   14.7 Psi
                                                     psia
                                IV-5

-------
                •VL."--^ if - ~^aJf 7^_t:- J. - ^_£~-?v jLj*. ' ^- r%*j-~ •-- ^A-T^
                ^•fc"** -.-.•-•.»— , ^r-,-^ci^','"_^ST*_T-»^K--A.—-ariari V
     3.   Design and Operating Practices

     For   a  tank   with  fixed   capacity   and   throughput,   design
considerations   to   control   air  emissions   include  surface   area
minimization and inflow/outflow pipe  locations.  The  choice of a fixed
roof tank,  external or internal  roof  tanks,  and other types  of tanks
are also viable design alternatives.   An  operational  change that could
decrease   emissions   is   the  temperature  of  the   influent.    These
practices are discussed in Surface Impoundments.

     4.   In-Situ Controls

     Technologies applied at  a  tank  can be used to change  one  or more
of  the parameters that  affect  emission  rates  from  the surface  of  an
open  tank.  The  in-situ controls  described  below  are:  fixed  roof,
floating roof, rafts, and floating spheres.

     4.1  Fixed Roofs

     It  is  commonly accepted that fixed  roofs over open  tanks reduce
emissions.   Fixed  roofs with  a pressure/vacuum  vent  only  release
vapors  when  the  internal   pressure  is  exceeded.   Fixed  roofs  are
generally  dome-shaped,  and  they  are  either  welded or bolted  onto the
top of  the  tank wall.

     Considerations  in  designing  a  fixed  roof  for  an  open  tank
include:

     o    The pressure vacuum settings of the breather valve in a tank
           is  determined by  the  structural  strength  of  the  tank for
           safety,  and the maintenance of a vapor concentration below
           the lower  explosive limit.

     o     As  shown in the equations  above,  the choice  of  paint  on a
           tank  is an effective means of reducing emissions,  although
           the  factor is more important  for  the  fixed-roof  tank than
           the  floating roof  tank.   A highly reflective paint  reduces
           the  temperature of the tank  and  the liquid  stcred  in the
           tank.

     o    Xoof material  must  be compatible with waste components.

     Another  kind  of  roof   which  may  or may  not  be fixed  is  the
aluminum dome.   Information for this  technology was  obtained  from
Temcor  in  Torrance,  California  (1983^.   The  material  used  in  the
construction  of  aluminum domes  ara  aluminum  alloys.   The   dome  is
formed using  aluminum struts to  form a  triangular space  truss.   Tnis
is  then covered  with triangular panels.   The dome  does not require any
columns for vertical support.   Individual  domes  can be  constructed
alongside  tanks  and lifted  into place.  Hundreds  of aluminum domes
.have  been  installed  all over the country.   Aluminum domes  have been
used  to cover petroleum storage  tanks, bulk  storage  areas, wastewatar

-------
                            lffri"nir  -r^r.t.,...  ,,r-i-  , ^m*g^aLttiieL^-:.v^vs*ErSS^
               treatment  tanks,  wacar and ocher liquid  storage  tanks.   In wastewate-
               treatment,  for  example,  hydrogen sulfide  or other gases from treatment
               can  be collected  and  treated.   The  dome also provides  insulation to
               increase process  efficiency.

                   Each  aluminum  done is  designed  for the  purpose  at  hand.   An
               important  consideration  in its use  as  a  storage/treatment  tank cover
               is  the structural  strength  of  the  tank  wall because  it is the  main
               support for the dome.  The waste  in  the tank  has  to  be  compatible  with
               aluminum.

                   Vapor  losses  due  to wind  venturi action  are eliminated because
               there are no seals  used  as  in the case of a floating roof.  There  ar=
              no floating roof  weather problems.   The  aluminum dome  is maintenance
              free   (according   to  Temcor)   and   aluminum  is  very  resistant   to
              corrosion.   Since  there  are  no  columns necessary  in  the  design of  an
              aluminum dome,  there are  few  appurtenances.   According  to Temcor,  the
              cost of an  aluminum dome  is competitive with a stsel cover.  Expensive
              downtime is  eliminated because  individual domes can  be  constructed
              separately  and  then lifted into  place.

                   4.2 Floating Roofs

                   An excellent  description  of  floating  roofs and the  cvpes of seals
              available with  floating roofs is given in  U.S.  EPA (1930).   There  are
              basically two kinds of  floating  roofs, external and  internal floating
              roors.   Internal  floating roofs  are again  divided  into  two  tvpes-
              contact  where  the  roof floats on the  liquid  surface and  non-contact
              wnen  the roor is supported on  pontoons several  inches  above  the  licuid
              5TT1"*" 3 f+ a                                                            T-
                race.
                _  rloating  roofs  are  by  far  the most  commonly  used  method  of
             hyarocaraon  loss   control   in   the  petroleum  industry.   Thev   a—
             generally considered inherently effective in reducing emission losses!"
                  ^
                                           	 —	__..^ wu*^Ml *JJ«W4_t * W 3 3C ^3 •
                     raauctions of  around  95 percent  over  fixed roofs
 (U.S.^PA,  L976).   In the  internal  floating roof, the  fixed roof -s
 ventaa  to _allow  surficient air  into  the  tank to  maintain  a  vancr
 concentration below the lower explosive limit.   All internal floating
 roors are designed  to  be  retrofitted into  existing fixed  roof tanks!
 Seals for floating  roots  are normally sold separately  from  the  roof
 ana  are not  necessarily dependent on  the roof design (U.S.  EPA, 1976).

      According  to  Jonker  et  al  (1977),  the tyoe of  seals  used  is
 important  in determining emission  losses  from tanks.   Maintenance  of
 seals was  also  found to be important  in reducing  emissions.   Secondarv
 seals were determined  to  be effective in reducing emissions  in  this
 study.   Gaps  between tank walls  and  seals  of greater than  1/3  inches
were  also  found  to  be unavoidable for the  vast majority  of  tanks.   As
expected,  these authors concluded that the amount of liquid  exposed  to
a gap,  the access  of wind through  the gap and  to the  vaoor above  the
liquid,  and the  length  of  path for the vapors to reach the  ataosche-o
were  important parameters in controlling air emissions.
at

-------
     Runchal (L978)  used a cyclone fanes on the tank top to modify the
aerodynamics above  the  roof of an  external floating roof.   He found
significant reductions in the pressure diffarancas on the two sides of
the roof.   Substantial  impact on windflow was therafora  achieved by
the  fence  and  wind-induced  emissions  were  also  probably  reduced
significantly  as  a  result although  emissions  were  not  measured.^
Significant  reductions  were also  obtained  when  the  floating  roof
operated  at  a  greater  depth  from  the  top  of   the  tank  (greater
freeboard).  These  tests show  the  importance of  the wind  speed and
flow  in  determining  emissions  from external  floating  roofs  and are
considerations in the design of a floating roof tank.

     Other considerations include:

     o    Stability  of  the  floating roof  under stresses  of  water and
          snow.  A pan floater is lass stable than a pontoon roof  (Air
          Pollution' Control Association,  1971).   A  covered floating
          roof does not have this problem.

     o    Insulation  of  the roof  can reduce temperatures in the  tank.
          In a floating roof tank, a double-deck roof is not only mora
          stable but has insulating qualities as  well  (Air Pollution
          Control Association, 1971).

      o    Roof  material  and  seals  oust  be compatible  with waste
          components.

      o    Modifications  to  the  tank  may be  necessary.    Tank  wall
          deformations  and  obstructions may  have  to be  corrected so
           that seals  will conform to the wall.

      4.3   Rafts

      Please see  discussion  in  Surfaca  Impoundments.

      4.4   Floating  Spheres

      Please see  discussion  in  Surfaca  Impoundments.

      5.    Post-Treatment

      As  discussed  in  post-treatment   in   surface    impoundments,
 collection  and  post-treatment  requires  collection of  emissions by
 means of a  cover and a  vent,  and traatment units(s) at the vent.   In
 the case of tanks,  the  collection  system  may consist of a  fixed roor
 or an aluminum dome  with a vent, and  post-treatment with  a  variety  of
 treatment  tachnologias.   Descriptions   of  two   approaches,   carbon
 adsorption  and  afterburners  ara  given  in  the   chapter  or.  Surface
 Impoundments.

-------
       A post-traatment systam has been installed at a facility owned by
  Waste  Conversion  in  Hatfield,  Pennsylvania.   This  facility  treats
  wastes  including   acids,   caustics,   sewer  sludges,   coolants,   food
  processing wastes  in  about  25  tanks.  All of  these are hooked up  to
  scrubbers.   The first  scrubber was installed  4  years  ago,  and  there
  have  been  numerous  additions  since.   The  post-treatment   system
  includes carbon adsorption (sent to another company  for  regeneration),
  wet   scrubbers  with   sodium   hypochlorita   and  "caustic  soda,   and
  precipitators.   In  this  facility,  there  is  some  in-situ  control  as
  well,   in  the  addition of  activated carbon  to  treatment  solutions
  themselves  to adsorb volatiles  before  emission.   The  whole  system  is
  large,  e.g.,  the carbon adsorption  consists of 5 carbon drums 12 faet
  in  diameter  and 9 feet high  each.  The  primary purpose  of all the
  controls  is  the reduction  of odors.  Otherwise, 'the operators of this
  facility  believe that  they  do   meet  point source air  standards with
  controls.  So far, the  system costs around $500,000  (Waste Conversion,
  Personal Communication, July, 1984).
 D.   Effectiveness of Tank Controls

      1.   Methodology

      1.1  Selection of Parameter Values

      To evaluate the  eff activeness  of controls in  reducing  emissions
 from tanks, waste,  tank and site  (environmental)  parameters  necessary
 for quantifying emissions were  defined.   These parameters were  shown
 in Table IV-2.  Parameters  required  to calculate emissions  from  open
 tanks were the sane  as  those  used in  surface impoundments exc=p«-  for
 wind speed  at the surface  of  the  liquid.   This was  varied because
 etriciancies from the baseline of  using controls are very  sensitive  to
 the surfaca wind speed.

      From  various  sources of data, GCA (1983) compiled typical ranges
 or^values  for input parameters  used  in relationships  for" calculating
 emission losses from  tanks.

      One tank size was chosen  from  these  data  as a  representative
 tank.   Other  average  or  representative  values were  chosen  for  a7!
 parameters   within   reasonable  expectations   of    tank   design   and
 operation.   Some  economies  of scale  are  expected  for  larger' sizas.
 The  general cost-effectiveness relationships developed below for the
 single representative case are axpected to hold for larger sizes.

     1.2  Calculation of Mass Transfer Coefficients and  Emissions

     The storage  tank was  selected  to represent  the  tanks   in  use
Treatment tanks were not considered as  different because  technologies
 to  control  emissions  would  be similarly  effective  in  treatment  and
storage  tanks, unless the treatment  tank was aerated  in which  case
Boating roots,  rafts and  floating  spheras  would not be viable  as

-------
 control technologies.   However, for each technology that is applicable
 to  both  types   of   tanks,  the  relative  efficiencies   and  cost-
 effectiveness would be equivalent.   It was also assumed that emissions
 were liquid-phase controlled.

      The relationships for calculating mass  transfer  coefficients  and
 emissions losses were shown in Table  IV- I.   Total  emissions from open
 tanks were calculated as  in surface  impoundments.   The floating  roof
 tank  chosen   for  comparison   is  the  external  floating  roof  tank.
 Emissions using  rafts  and  spheres were  calculated as  10   percent  of
 baseline plus losses  due  to clingage  during withdrawal using L   for
 floating roof tanks.                                             w

      1.3  Emission Reduction and  Efficiencies of  Controls

      The open tank was  used as  the  basis of  comparison  for all  the
 control   technologies,   i.e.,   it  was considered   the  tank without
 controls.

      The reduction in  emission  rates  is defined by:

           a   -  qt  - Q2

 where the subscripts  I and 2 refer to tanks without controls and with
 controls respectively.

      The efficiency (E)  is defined by:

           E   -  100 (Q  - Q
     The  reduction  in  emission  ratas  depends  on the baseline select ad
in  terms  of  surfaca wind  speed  in  the open tank.   The efficiencies cf
controls  ara extremely sensitive  to   surfaca  wind speed.   Curves cf
efficiencies of  the controls with  varying  surfaca  wind speeds will be
shown.

     L.£  Cost-Ef f activanass of Controls

     The in-situ controls for emissions raductions  wera compared using
the  cost  of  each percant of Deduction efficiency  per square  faet of
surfaca   area   ($/percant-ft~) .   Carves   were  developed   to   shew
cost-affactiveness  with  varying   surfaca  wind  speed  based  on  the
relationships  in Table  IV- 1.   Pratraatment,   in-situ  controls,  and
post-treatment wera  compared by considering  the  curves  of  cost  per
pound  removed  (reduced)  versus pounds  per year  removed  (reduced) .
Similar curves were ganeratad  for cost per  pound removed  (raducac"5
versus throughput in pounds per year.   As in the discussion an surface
impoundments the  curves ara:

-------
,*»,,,*-

                                7  =  £       (?/lb-reducad)

                                y  -  A/ET     ($/lb-reduced)

                Post-Treatment     y  =  1  + p  ($/ib-reduced)

                                      F
                                7  =  2T~" "*" p  C?/lb-ramoved )

                whera:   A  - annual  cost of in-situ control ($/year)
                       R  » reductions (removal) (Ib/year)
                       E  » efficiency of control
                       T  » throughput (Ib/year)
                       F  - cost  of collection  per year ($/vear)
                       p  - cost  per pound of post-traatment ($/lb)

           dlffAWe f.comPared  in-situ,  post-treatment  and   pretreatment  using
           situ costsPwea-ereoaC3er C°-S ^ Caken.from Spiv«y at al (1984).   In!
           Post-treatment costs were obtained  from  EPA  (1982).

               2.   Parameters


           .^ ^ ^\*"r^^2£^^ r?r

           ™;3f iaf £'£%rzxz- wrs-s^._
                      o be usea in the floating roof and that thev we^e i-
           aooa  condition.    The  waste   parameter   (?)  was  choser   as  1
           representative value for wastes  storad in tanks.

              3.  Emissions

              Emissions were  calculated  using a  mole fraction of 1 ^r  the
          volatile components  in the impoundment.  Emissions from one^  tanks
                                         che U^i
              4.   Emissions Reduction and Efficiencies

              In-Situ


              Emissions  reductions  and  efficiencies  of  each of the  *n-s'tu

             '-±J:!^^Tabfar7-4-  Curves of efficiencies of     ^
                                                   —,_ ^T^ ^  anr? -^"* ^ *• *• v

                                    fixed roofs.  External floating roofs^

                                , are much more efficient than fixed roofs
                                                    s
                  ts and spheres become less efficient than fixed r


-------
 Tank:
                                TASLZ IV- 3
                       PARAMETER VALUES  FOR TANKS**
       PARAMETER                VALUE
                                                      UNITS
                              100.08               Ib/lb-aol
                                2.5                   psia
          Kc                    1.0
          ?                     0.0466
          CL                    °-3               bbl/1000  ft2
          WL                    9                 lb /gallon
          D                    45.75
          H                    10                    faac
                                1.3
          c                     i.o
          Kj                    0.6
          5S                    °'7
          H                     0.4
          E?                    0.75
          Q                     8.2 x  10           bbi/year
          Ho                    30
          A                  1643.9
Site (Environmental) :
         7                    10
         iT                   15                     «7
         9                    25                     «C
**
   Assume tank is 40 feet call capacity s 11,700 bbl, and turnovers
   per year - 70.  Primary and secondary seals, both the good condition
Source:  Arthur  D.  Little,  Inc.
                                rv-12
                                                                             .1
                                                                             ---a
                                                                             -

-------
                                                  TABLE IV-4
                                         I2**§J»!LJ^ICIKIICTESOF CONTROLS
Surface Wind
   Speed
(l'0/ft/aec)
2 x 10~5
10-*
2 x I0~/l
  10
    "2
                      Fit
                        **
                             j£l!ii£lioiisOl)/y r ) *
                                     El'R
                                        ***
                                                    Rafts/
                                                   Spheres
                                                                         FR
 Rafts/
Spheres
16,107
86,431
779,609
2,490,508
12,025.586
72,603
142,656
508,440
8 36. 105
2,547.004
12.082,082
61,032
124,080
453.286
748,184
2,287,993
10,869,563
13.6
45.8
81.5
.88.4
96.1
99.2
61.3
75.6
91.7
94.8
98.2
99.6
51.5
65.8
81.8
84.8
88.2
89.6
                                                                                                                           I
                                                                                                                           K
                                                                                                                           >
*
**
***
         unit  ,nole fraction of volatile covenant
   FR - Fixed  Roof
   EFR - External  Floating Roof
 Source:  Arthur D.  Little.  jm:.


-------
    100
    90
    30
    70
    SO
5   50
'3
    40
    30
    20
      10"
10"
10'°
                           Surface Wind Speed, UQ ft /sec
       FR  »  Fixed Roof

       EFR a  Extsrnal Floating Roof



       Source:  Arthur D.  Litels,  Inc.,  1934
10'
            FIGURE IV-1   EFFICIENCIES OF IN-SJTU CONTROLS FOR TANKS

-------
                       •»&tk:£l^'f,S-^^r^^T'' ^ ,-" - '-  fi'"
            t.
    through the po«-tr.«ment unit
    »*          fician=7 of
   ««  <«  ^arisen:
                   Iha
              and  the
                                                                  carbon
         an
     5.   Costs

     j?r e treatment
    In-Situ  Controls

                 b?
  the  differance in a  new tank wlch a
 According  to the vendor,  Se S«a
  ithin  the  saae  magnitude  of a" or
         by  taking the  difference!

      Installation costs wer<=>
 -he cost  for aluminum domes
 spneras have verv low Insta
-re not included" in chrj
 -or rarts  and spheres  vere not included.

ra,..R°70f3  hfve  a  lccS lifetime Cover 25
ra.ts  last  1  year and that
                                                                  « «
  n
     Per
                                                  "cfs, Che loca£ion
                                                    derived ^ Caki"S
                                                     W±thouc  a roof'
                                                         Iv vould  be
                                                     as the  figures
years)
u

                          ««•
                                                        *S  ^  «of3.
                                                        and float^^
                                                      ,   TheSe ««'
                                                      Disposal costs

                                                        as3UEe^ =^at
                                                                  »




-------
                                  TABLE  IV-5
                 Tanks
                      1
   Open top with vind girder
   With column supported cone roof
   With double deck external floating
     roof  incl.  primary and secondary
     seals
                   Total

                    95,000
                   115,000
                   215,000
  la-Situ

    Column supported cone roof
    Aluoinua dome^
    Double deck external floating
      roof incl.  priaary and
      secondary  seals
   Rafts
   Bloating spheras
  Collection
  C«xcl. treataent)

1.  For t.
    and
     20,000
 16,000 - 25,000
    120,000
    130  -  210
 10,300  -  14,300
                    Annualizad
     3,200
 2,600  - 3,900
    19,000
  13C - 210
1,700 - 2,300
16,000-25,000     2,600 - 3,900
                              17-16

-------
          c aftarb»~
       6.
                                        P°ur.d, rasoec-
                      of

      r -
   °P*ratad in
          appea"
                                     'affec«ve, bai
                                              ng
          of
     Figuras IV-
                                          catlk
   'Pectivelv. r


 constant *•*-,
           costs.
                   -3icu  c
                         ontrols and for ^
                                     es  are  ac a

                                     ae  levels of
          T7-3



                                 n
•j-c c-t"ia boct
        om la;-
            -
                              .
                    ""«=«=»« cost

   -srractiva,
and fi:c
                 hyperbolic
S^ i.72^. "^"iS1^ SS?
S %^^S?5^ ^ȣ^ rs?
wt^-^-^^«2-t5£^:
                                                      , ,:

                                                       Sfl
                                                      I III I

-------
                                                          TABLK TV-6
                                                COST-KFPKCTIVENKSS FOR TANK IN-SITU CONTROLS
3
          Surface Wind Speed
              (ft/uec)	
                  10
              2 x 10
—5
-5
                  Hf<
              2 x
                  10
                  10
r3
-2
                                                         Cout-Kffectlvenean
Column Supported Aluminum
Cone Uoof
I'.. 2
4.2
2. 4
2.2
2.0
2.0
Double Deck Ext.
Dome
II.
3.
2.
1.
1.
1.
7 -
5 -
0 -
8 -
7 -
6 -
17.
5.
2.
2.
2.
2.
5
2
9
7
5
A
Floating Uoof
18.
15.
12.
12.
11.
11.
9
3
6
2
8
6
Rafts S
0.2 - 0.3 2.
0.1 - 0.2 1.
0.1 - 0.2 1.
0.1-0.2 • 1.
0.1 1.
0.1 l.
Iphei
0 -
6 -
2 _
2 -
2 -
2 -
refi
2.
2.
1.
1.
1.
1.
1
7
1
7
6
6
5
                                                                                                       Multiply
           Source:  Arthur I). Little, Inc.

-------
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              it
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                    . $ per P
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       x1 -

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-------
o
I
i
                                                                                          Puil Trudlmenl. (> » j46/lt»

                                                                                                  iUui|iii
-------
        A).	._
        (iO
/   E
                                                             F - 3000. p = $4S/U,


                                                                   Adsorption
                                                           F - 3000.,, - $5/11,


                                                                     R«uwwrailon
                                                                                                                                                              K

                                                                                                                                                                "
  I
 $
 r-
                                                                                                                                                             f.vv:
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                                                                                                                                                            •S.'s

-------
                                                    •' i n'M «fri frf^'Hi'if''~^^i~'-'^'^sgj3SSzi^.
If the price of post-treatment can be reduced,  it may become more
iii^n^r*1 f"°acins  r°°fs  « *ro«gh£cV",7
around  10   Ib/yr  (e.g.,  if post-treatment costs  $5/lb  ($11,000/MO
vxth  . caroou   regeneration).    Under   low   ost-trea*
                                                    -treatmet   costs
                                                    than fi.el
  r0nf,In  ChS a.na^sis'  the "fluencies and the  cost-effectiveness  of
  roofs  are  prooafaly underestimated  with respect to spheres and  rafts
  Fixed  roots  are  likely  to  be very  comparable  to  using   spheres'
                   of the iow  cosc  °£                      '        "
      Figure  IV-4  shows  the cost-effectiveness versus  the  pounds oe-
 year  recuced or  removed  per  year.   Each  of the  hyperbolic  cu4es
 represents   au   annual   cost.    la-aim  controls   «»   favored  co
 precreatnent  as  the  pounds  per  year  is  increased.   If "« TTn-si"

 orn!lnLflaS  f TUal CrC  °f  S3'000/^ (corresponding to  fixed roo7
 or alumiaua  dome), a  reduction  rate  of  3,000  Ibs/yr is the trade-o°-
 point at which  the in-situ control becomes more  «s".£f.ct" ?
 pr.treaea.nt at the cost  of  $l/lb  ($2,200/Hg).   If  pr.tr.IU.lt
 vas  increased  to  $2.00 per  pound (S4>400/Xg)f  a  rate  of
 E.    Summarv
      Roofs  are well-used, proven  emission  control technologies  -om

 deJ-'i^ra^Sv^teen1"' • F£°aCia* s?heras> »d to a much  leaser

 industry  for  emissions  control.   Pretreatment ^and^oo^t-^"3
      ao                                  «. easily a
 t~e  case  or  tanks.   :,asCe  Conversion  in  Hatfield,  ?\," is  a ,«od
 esanpie  wnere post-treatment  has  been  used  effec-'^e'V  "
   ssicns  from  treatment  tanks.   As  an example  o'?  a"
     ao.e  procuct   Calgon Corporation  offers  7..Morb,  a    t
        Ventsorb  is  a  55-gallon  dn
specifically developed Co be  used  at
process  applications.   Each  unit   co_  «w.«u  ^jj-ao^   a

and^h"7    P°Sed °f aftar asa§a-  Tha ^ics can  also  be  taken
a"-. C e  "rbon re?lacsd-   Replacement carbon  costs  around  $300 " o
am..  (Calgon Corporation, Personal Communication, September 1984)'.
     Certain technologies may be applicable in storage tanks  but  -
in treatment tanks.  Floating  roofs  are general!, not aon
                                     Post-treatment are  applicable  to

-------
                                   *Ssiisj£iuii_
         r°  a similar wav  -fn   •











             8"   M Ser                              °U"
                                     or  in      s
                                                               vaste before
without  a large V«
-------
 F.    References

 Air  Pollution  Control  Association,  1971.    Control  of  Atmospheric
 Emissions  from Petroleum Storage Tanks.   Journal of the Air Pollution
 Control Association,  21:260-268.

 American Petroleum Institute,  1952.   Evaporation Loss  from Fixed Roof
 Tanks.   Bulletin  2518.  American Petroleum Institute, Evaporation Loss
 Committee, Washington, DC.

 American Petroleum  Institute,  1964.   Use  of  Variable-Vapor-Space
 Systems  to   Reduce  Evaporation  Loss.   Bulletin  2520.    American
 Petroleum Institnta,  Evaporation Loss Committee, Washington, DC.

 American Petroleum Institute,   1980.   Evaporation Loss  from  External
 Floating Roof Tanks.   Bulletin 25L7  (Revised).   American  Petroleum
 Institute, Evaporation Loss Committee, Washington, DC.

 Calgon   Corporation,   Pittsburgh,   PA.   September   1984.    Personal
 Communications.

 Chicago Bridge  and Iron  Company,  Boston, MA.   July  1984.   Personal
 Communications.

 Corripio, A.3., K.S.  Chrien, and L.3.  Evans,  1982.   Estimate  Costs  of
 Heat  Exchangers   and  Storage  Tanks  via   Correlations.    Chemical
 Engineering, 89(2): 125-127.

 Federal  Register, May 19, 1980.  Vol. 45,  MO.  98, p. 33075.

 GCA,  1983.   Evaluation  and Selection  of  Models  for  Estimating Air
 Emissions  from  Hazardous  Waste  Treatment,   Storaze   and   Disposal
 Facilities.   GCA-T3.-32-33-G.   Revised Draft  Final Report.   Prepared
 for the U.S.  Environmental  Protection  Agency, Office of Solid  Vases,
 Washington, DC.
Jonker,  ?.£.,   C.3,   Scott,   and  W.J.   Porter,   1977.    Pollution
Regulations from Floating-Roof Tank-Seal Study.  Oil and Gas  Journal,
75 (24):72-75.

Runchal, A.K.,  1978.   Hydrocarbon.  Vapor Emissions  from Floating  Roof
Tanks and  the Role  of  Aerodynamic  Modifications.   Journal of the Air
Pollution Control Association,  28(5):  498-501.

Spivey, J.J., C.C.  Allen, D.A. Gcasn,  J.P.  Wood,  and R.L. Stailings.
1984.   Preliminary  Assessment  of Hazardous Waste  Pratreatment  as an
Air  Pollution  Control  Technique.    Draft  Final  Report.    Research
Triangle  Institute,  Research  Triangle  Park,  NC. "  For  the   U.S.
Environmental Protection Agency,  IZRL,  Cincinnati, OH.
                               IV-2 4

-------
  Temcor, Torranoe.  CA. , October !983.  Personal  Co,«uni=ations .
                  rlr            '.     "«« " *'•«-. ^
 Tanks.   E?A-i50/3-76-036 Hydr°';a'bo.n Missions from Petroleum Storage


 KesearchTriangUPark.se.         E^iron«eatal   Protection  Agency,
                         r            Ed

 Protection Agency,  ^search Triange Park  uc      B'S-
                                                            "
•-USr^-S; 198C°-  .B""» B^»i»»  '».
EPA-450/3-30-034a.   n.S   Enliror J / i ^,     " PraP°sal Standards.
Triangle Park, 8tc.        E^"on«ental  Protection  Agency,  Research
Emergency and Remedial  .2-^-    <****•




     Conversion,  HatfieZd, PA, July 1984.

-------
                             I.  LANDFILL.'?
A*   Landfill
  techniques  is  required  by
  practices  to  isolate  che
  UndfiU facility  contains  "r.e
          -
                                              T  -«•• •»
                                               ,,A varia".
                                        .             '         cre
                                     m"=a  as  several acras at a fav
                  t      ent
  Che land surface  foiloving c7osu°8
                                  ~
                                         S°me M"s to
                                                              use
                   in
                                                     the

-------
B*   Session Sources and Models

     I «    General
                                  n
                          .r
     ily  (or  te^orarv)   cove-
   permeate  che  final" (per^anVut)
   landfill.  The  rata of  emi7/£m
   the  for*  in which  the  ^^T
   operating practices at the facility.
                                           ; fr°°  ac
                                               T the  arsa wich  «*
                                        aT*  ? ^/^  COnP°u^s  «c
                                             Cl°Sed  Secci°°s  of  the
                                       be
      tight  so  that  no  essins
integrity  at  soce  lats-  dat-   then
utltiaately   penneate  through' the
through the  cover  into the  ?r   Vo^
diffuse  to  the surface  and  into  t
generally quite low  as aar'
solid surface and exhibit
                                          -
                                               aaoiene  conditions  and
                                                         bui:< solids,

                                                        MW"d  C° bi
                                                       onca^e"s lose
                                                    C3nsc^^==s  can
                                                   ""*  and  ^SSra.
                                                    "  ** *«& 3olids
                                              v       ^  racas
                                              b'C°M abs°rfaed On
  carried out by  adding  liquids dife"c*' TV
  operating  face  and  then olac'n* ^ the
  possible to have pools  of  l^id nr-J
  good practice  *ould avoid  th"s  '
  vould  be siailar  to those  «  »
  organic  layer or a  land  Cr«".*
  applicacion of  vastas.
  be   avoided for nmar
      tica, etc.,  ic wifl not
                                          -    h °?fraCl0ns
                                          ^   bul.
-------
          '&iig&ti£^^&&&t3tt:
          KH^jav«iw«'«^mX¥TH*VfiSfXK
                                                     •;: ^\T£^t^itsfeslSs


            the
                                                                 „
   atmosphere  in  su,  Or in                    may         a





        2«    Hoission Models


                                               onlv
                                                  -
            Covers
                                                —usion  through covers
where:
               Q
               A
               D ..
volatilization raca nb/h
area of cover (V)     a
effactive diffusivitv (f 2;
                                                                                    I!

-------
     Tor  the  top  cover,  the  concentration  in  the  atmosphere  can
generally be neglected  relative  to  the  concentration below the cover.
Effective diffusivity  expresses  the  diffusive  behavior  of  a single
compound  through the  pores  of  the cover  for  soils  or  through  the
fabric  of a  synthetic  cover.   Of  several  equations  available  for
soil-type covers, Parser's (1978) equation appears most appropriate in
terns of the objectives of this analysis.  It is relatively simple but
indicates how diffusion relates to soil properties.  Parser's equation
is:

                                                           7
     where:    D .   *    diffusivity of compound in air (ft~/hr)
               £    »    porosity of air-filled pores
               t    *    total porosity


     Further, porosity can be related to the density to which the soil
has been compacted as:





     where:    3    »    soil bulk, density (lb/ft3
               9    =  .  particle density (Ib/ft )
     If the soil is completely dry, then total porosity and air-filled
porosity are  the  same  and the effective diffusity becomes  -he norsal
diffusivity  in  air.   If  the soil  is wet,  part of  the pore  volume
becomes  filled by vatar.   In  this  case,   the  air-filled  porosity
becomes:
     where:    
-------
           ADC
             m

            m
  where:    A    -    area of cover (ft2)

            Dm   "    Permeation rate of a given diff using. compound
                      through synthetic cover material (ft /hrj
            C    -    concentration of diffusing vapor at the top
                      or the landfill (Ib/ft )
            Cm   *    thickness of synthetic cover (ft)
                              j-.

 where:    c    =    vapor concentration (Ib/ft3)
           <    **    empirical constant
           x    -    mass of volatile  compound  absorbed oer  unit
                     mass of soil
           a    »    empirical  constant
where:
                    vapor pressure of pure component  (atm)
                    molecular  weight   of  diffusing'   component
                    (Ib/lo-mol)

                    gas law constant  (0.73 ata-ft3/lb-mol-°F)
                    temperature  (aR)
T    =    temperature
Y    -    activity coefficient
x    -    mole fraction

-------
i _
II

                            For  dilute  solutions, Henry's  Law can  be  used  as  an alternate
                       iorm.   In all of  these  relationships, vapor concentration increases
                       with increasing temperature, all other factors being equal.

                                 Bulk liquids

                            The mix of free liquids and solidifying  or  bulking agents can be
                       represented  by the  models developed for  land  treatment.    In  land
                       treatment, also called land-farming, oily wastes  are  deposited en and
                       tilled into  soil  surraces.   The rate  of  emission displays  a  complex
                       time-varying  relationship  reflecting   depletion  of" the   volatile
                       materials near the  surface (Thibodeaux as  reported in Hwan»   1982)
                       The  characteristic  time  for  land   treatment" cycles  is  qu'it-  Ion-
                       relative to the period during  which mixed liquids are  exposed at the
                       working face of a  landfill.  At landfills, bulk  liquids are mixed  v* eh
                       solidirying materials such  as  kiln  dust, prior  to  deposition  in the
                       landfill.   Pooled  tree  liquids may be present,  but  onlv for short
                       periods.   The bulked  liquids, in the  solidified matrix,  mav be  exoosed
                       to  the  atmosphere  for periods ranging  from hours  to several days."

                            In this situation,  it is  reasonable  to  assume  that losses occur
                       at  the  exposed  surface through  diffusion from  free lisu'd in  the po-as
                       or  the  bulking  agent.  In  this  case, the mass flow equations s-
                       to:
                                      Ak   C*
                                        oa
                           where:    A    »    area of exposed face (fc2)
                                    • T:Cjja  *    overall mass transfer coefficient (ft/hr)
                                     C    -    equilibrium concentrations above  free i-'
                                               (To/ft )

                           For purs or mixed  organic compounds,  the overall  coe---'"-'»~-  -3
                      generally  gaa-fila  ccntrolled  and  follows  a  law siailar'To" chose
                      discussed in the surface impoundment chapter.   The coefficient deoe-ds
                      generally en wind speed, seme  characteristic dimension  of  the expose-
                      surface, and diffusiviry in  air.

                                Bulk solids
                      liquid rarfaca.

-------
                           -. '-. >' - =J»i. .'- -
      3.  Controlling parameters


         Covers

       as  the vater tableevel)
   leachate collection
                                              factors

                                         3nd  lin"
                                                 to
  ™r"s 'Is a VT stro°s *s«i«"7
  -owermg the  internal  temperature  of  ^»
  volatile emissions.  Diffusivity of
  selection of the  basic  cover
  content.  For synthetic  covers,
        and memo ranee thickness.

         Working faces
mass transfer coefficients  as -
practical.         ~" '
                                          Since

                                             means of
                                     -^ would reduce

                                          m°difi2d b^
                                         and  moiscure
                                                 of
                                         -Id  reduce
                                      - bulk liauid is
                                        cc^ld be added.

                                        -2_ac facilities


                                        s" case, is not
 c-  Controls

    1-   Introduction

    There i
 compared to  	
 the _ same for all "cr«aKaenc and
 Design  and  operating pracf'c=>s  mav ,-a^    ' .	5 -i«ariixs.
 without interfering Jith aormal 0™it "ont" ,em±SS10ns "nsiderablv
 covers  including  vents  is ^^d^thm^a8Wn 3f P««umeni:


£3;~;is:=^^in::?^ss
includes t-,0  distinc, cypas of'conJoiT' P°SC ' CraaC—- Broaches,
                                       **
                                       ^ «sts are

                                          landfill,.

-------
                                               -JM-.. r^JF^ j^r^f ^U^ -W ~*1 r-^^r^-rrT*^'^ 
-------
 froa being filled.  Table 7-1 shovs a ranking of a variety evr>es of
 soils according to several different functions («*  igygf  ri?
 c'^^^r/110;' ^^ very hish =^---/97^;rtun:teDi:;
correspona to clays and miXes of clays and other soils


          .      ^.r^r^T^r
curves shoOT ccrr.spoad to the  So-c7iled standard  enaction '
                                      -

iS.,  falaved-  " » «"-: "«a« of about 13 It./cibic ^oc  ::1 -
       "^a="°" «" «                              '"
                           .ff active diffusiv-y by f

-------
                                                                       TAHJ.IJ  V-l

                        HANK-lNf;  OP  USC.S  SOIL TYHI-S ACCOHDTNC TO  I'ERPOttMANCIi  OK  COVKR  FUNCTION
                	-	*""»  *«•-	''^'"'«-.-^"U^^^^^^
                 U»ll  KiuJtJ »mvo|M,  Kl.vtl  u.m.1         t             f        K         f        ..        „
                 • ImuivM.  litilu  o,- „.,  nuft                                                      *•        K           t         U             r
                 I'ourly  ni.i,l.,J  gr.ivuU.  _(uvvl-    '       f             r        t         „
                 • Hill!  KlUlmeu.  |||| III U|  „„                                               'BK           t         |T             j.
                 f I nil*
                 Silly .muni*, (riivul- vi,,,j .id
                 A! m in p.
i;i;

su
SI'
Sll
si:
HI.

ml H| mttH
Wu|| ui.i.l.-.l ua.iJ.,
.un.lo. lln U in nu
1'iiiiily uruilfil .1111. In
u.xiilN. 1 In In (,r ,,u
rluytiy «UM«|MV NUIIIJ
UllllllM aill^L 1 l.tla*

y i.
HI'Hvully j;
1 Inuu
, «l»vclly l
1 limn
• III •IklllM.U |i-f

i; F
F
f e
!•' G
r F
r. f
                i-l.iyfy fliiu nuiiili4t ^i  I'luyiiw
                Ulllu Ullll Hll|)j|UI I. ll^

        «.'!.      liliiiKiinli: ••!.,>• ,i| |,,u 4., Bej|u
                (.Li.,! li:lly. (ilnvtlly Ll.iy.,.
                u.iii.ly i-luya,  .Illy t|jy,j,  |,.ai,
                i:l.iyu
                i l.tyu ul |,iu |,I«.| Idly
        Ml      lil»iB.tnlc  ulllu.  nli.-ni-v»im ui
                n.il In,  i-ljj| Ic  villa

        t'll      lii.iiK.iuli:  tl.iy. ul |,|K|,                  ^
                |>l.iul Ully.  (.I cl*yu                                 r        I         K        F        r           F         F
        • ft      Hi d ,1111 c il.iy. „) i»..,||.,« !„ (,,„(,          r
                |ll.l:illl.l|y. U1|1.,.,U .Hill                                      "         -        -        F                     F

        ft      l'«.il uuJ oiliur hiulily .ii,;,i,,l,:            ,.
                ttUlIu                                                          ~"~U--
      H«yY•-r=-.,,c.:iiJ,l,-i  -irvii,.u.ii  FV7,i,;  ,.%^,r
Source:   Kl'A,  1«J'/«J.
                                                                                                                                                                                      1
                                                                                                                                                                                      $
                                                                                                                                                                                     k

-------
   """'"'''''* >'']>"^'i  f-i v'.i'.-ouj;  "

3 a
             Source:  Arthur D.  Licrle,  Inc.,  1
     .cm
    -CQQ1
                                        •3          .4




                                      rracnon Water {w/o,.j
                                                    «'
                       V.,  RELATIVE O.FFUS1VITY.NSO.L COVERS

-------
                                                                      rjK»-#)*>* *>*!••*?";
                                TABLE V-2
         RELATIVE DIFFUSIVIT?1  AS A FUNCTION OF SOU PQRQSTI
 Water


Coatant(w)
                                          Total Porosity (s )
      Relative


  Water  Fraction
                                0.3
                            0.4
0.5
                                                      0.6
                                                  0.7
                                                                       0.8
(1


6
11
13
25
31
37

43.

•b/fO

0
.24
.5
.7
.0
.6
.4

.7

(w/P )


0
0
0
0
0
o,

' 0,

w
0
.1
.2
.3
.4
.5
.6

.7


.20
.052
.005
0
-
-





.29
.11
.029
.0029
0
-





.40
.19
.072
.019
.0019
0

^



.51
.23
.14
.052
.014
.0012

0

"~

.62
.37
.20
.096
.037
.0096

.00095

0

.74
.48
.28
.16
.073
.023

.0072

.0007:
  1.
D ..
 err


D .
 air
                    (e)  10/3
                                and  £
                                              v
Source:  Arthur D.  Little,
                 Inc.

-------
      130
     SO
3       '°       '3       20       2S
  MOISTURE CONTENT, PERCENT OF DRY a
                                                    IGHT
          FIGURE V-2   EXAHPLE STANDARD COMPACTION
                      FOR VARIOUS SOIL TYPES
Source:  U.S. Envi^encal Proceed Agency, 1979

-------
decreases demonstrates  the need  to  prevent  drying  out.   Very  large
relative increases in diffusivity occur as the moisture content begins
to fall much below the optimum point.

     3.3  Final or Permanent Covers

     When a working cell at a hazardous waste landfill has been filled
up to  its capacity,  that portion of the  landfill  is  closed.  Closing
involves  the" installation  of  a  cover or  cap  over  the  top of  the
collected wastes to serve many purposes.  These include the prevention
of infiltration of surface water,  the  reduction  of gaseous emissions,
general  site  security,  and  others.   The   current  regulations  for
landfills focus on the problem of grcundwater protection and emphasize
infiltration  control  and  leachata  collection as  a  means  to achieve
this objective.   Fortunately,  from an  emissions point of  view,  this
objective  also  serves  as  an  implicit  gaseous  emissions  control.
Covers  that are  effective in  reducing water  infiltration  are  also
effective in  reducing  emissions.   Both gas  and liquid permeability of
permeat:
always  be  some  residual  level  of  emissions  even  when  a  synthetic
membrane  cover has been installed.                                 -- —

     The  installation  of  covers  does not eliminate  the  generation cf_-
gases.  Gas generation continues through the volatilization of organic"
wastes  and in some  settings  through the generation of  methane  as  a
product of  anaerobic degradation.  These gases will gradually build up
in  the  landfill  and may,  if  sufficient  pressure  is  generated, damage
the  cover.   At the  same  tine because of the  increased  pressure, the
gases  will  tend  to  diffuse  laterally  out  of  the  landfill  and
ultimately  to  the  surface.    Some  sort   of  vent  system  is  of tan
installed in  conjunction  with the  cover  in  order to  prevent either or
these two situations from arising.

     The  discussion above on  temporary covers  describes  the  basic
behavior   of   soils   relative  to  permeability.   In  designing  and
installing  a  permanent cover, thera  is  considerably more flexibility
than is  possible  in temporary covers.  The economics  permit  a much
wider  choice  of materials  and complexity  of  design.   In particular,
layered   designs  are  becoming  quite commonplace.   The  designer can
incorporate  favorable  trafficability,  water  impermeability  and gas
barrier properties are using  different materials  rather  than suffering
the trade-offs intrinsic  in the  use of  a single material.  Figure 7-3
 (EPA,  1979) illustrates  the concept  of layering.  In even  more complex
systems,  synthetic membranes may be  added  in  addition to the various
soil lavers.
                                 7-14

-------
             :::::::::::::::::::::: LOAM (FOR VEGETATION) :J:!ji|J:J::;H:jH::::
                                  CLAY (BARRIER)
             oooooooooooooooooo**--- ----^ii^ix7^;?r5"^°icaoooooaoo?c"oTo"oo"oP
             OOOOOOOOOOOOOOOOOO ^-3Aiyt?\ ,****. —     —  TOOCOOOOOOOOOOOOOO
             oooooooooooooooooo GRAVEL (GAS CHANNEL) 100000000000000000
             OOOOOOOOOOOOOOOOOOww M                   OOOOOOOOOOOOOOOOO

                                CLAY (BARRI SR)




1








j SILT (FILTER)

!
1



I!
!

             FIGURE  V-3   TYPICAL LAY25ED  COVER SYSTEMS
Source:  U.S.  Environmental Protection Agency,  1979

-------
      The  gas  channel shown  in the  figure  ±s installed  for use with
 some  sort of  vent system  to control lateral  gas  migration.  Several
 technologies can be used:

      o    Trench vents.  Trench vents are  narrow  trenches backfilled
           with sand,  gravel and/or stone.  They are often lined on one
           side and can be  open to the atmosphere  or  capped with clay
           and  fitted with  laterals  and riser  pipes  vented to  the
           atmosphere.   They   can  also  be  connected   to  a  negative
           pressure fan for forced withdrawal.

      o    Vertical barriers.   Vertical barriers  include slurry walls,
           grout curtains, and synthetic  liners.

      o    Forced wells.  Forced wells for  lateral migration  control
           are  identical  to  those  for vertical  control,  except  that
           they are placed around the perimeter of  the  sits  and spaced
           such that all gas is drawn  to  the wells  before  crossing  the
           site boundary.

      o    Injection trenches  and wells.   These are similar  to  forced
           induction trenches  and wells,  except  that  a blower  is used
           to  force  air  into  the  systen.  This  creates  a  pressure
           gradient  in the landfill, causing gas to flow away  from  the
           system,  and thereby preventing lateral migration  across  the
           boundary.

      In  installations where  the principal purpose  of the gas  control
 system is  to pravent  damage to  the  cover,  the vapors released directly
 into  the  atmosphere.   For emission  control  purposes,  some  sort  or
 treatment  would be  added.

      4.    In-3itu Controls

      Sone  of the controls considered are classed as ir.-situ controls.

      5.    Post-Treatment

      Post-crsarment involves  the  collection  of  gaseous emissions from
 the landfill and treatment of those emissions to remove or destroy the
volatile organic components.   Such systems consist of  the collection
means  and  the  treatment  means.   Combinations  of external  covers  and
treatment  techniques  such as carbon  adsorption or incineration  have
been  discussed  above  in  the  chapter  on  Surface Impoundments.   This
approach can be  used  on  landfill  operations in essentially  the  same
manner as that for  surface impoundments.   As  previously discussed,  air
inflated structures can be installed over  closad or  operating landfil"
sections covering  the typical  range  of  sizes  from a fraction of "an
acre  to  as much as  5  or  6  acres.   These  types  of  structures  can
include  complicated vehicle  air locks to  permit  access  during  the
operating phase.                                               "**"
                                 T* • £.
                                 v-J.3

-------
         The   air  introduced   Co
    conventional systems escapes bv n
    in this  application be exhausted
    to the treatment  system.
    from the surface  of the
                           e  zn
    arter passing through the treatment ^stel
                                            rh
                                                           '      <     in
                                                    Che aacari^' *°uld
                                           &  '""*  °f VentS ««i«cced
                                                         V3p°r raleasad
                                                      C°
                                                            as weu  as
               of   a  cover  at  che  fflcos  f P^ffipa  reaS°n for the
Louisiana,  is  to  keep   precipitation  out    A   7   in   LivinS^°n,
approach  with  comparable  peSoSnc-  vould  f  alteraative  control
connected  directly  to  gas ven"ts^ns^lT .   • t • *  Craat:aenc
exiting through  the covlr.  ForLd  vents  1U?/ ^
drxving mechanism  for introducing JsasJCa^   ^  C° pr°Vide
for achieving high collaccion        ™   «°    « tr.at»ent  unit  and
     Effectiveness


     !•    Introduction
  and

  Rightly  diffarent  from that  Ucd
  landfills  there  is  ™  ./1, 7
  reference  casef   E^erT Wf'n Tas
  emission  rate   through^ the  covers
  orders  of  magnitude.   Therefore
  reduction  are   arbitrary  and [  daVand
  reterence.   Cost-effectiveness ^  t
  cost  per pound  of  emissionTr4oved
                                              ace
                                                       the effectiveness
                                                          -chodology is
                                                      impoundments.

                                                        "
                                                      °    C°V"  but  Che
                                                           °V8r  Several
                                                             °U
                                                    on   the   choice
                                           "'  eMa±«d  °n Cha
      2-
        Effectiveness
   2.1  Covers
                                                                   of
                                                                   of
                                    .
 means to examine the effectiveness  of
 equation  described   above  h7v«b..,,
 relative effectiveness  of di^     "
 and  Figure  7-4  present  data
 covers  of different  total
 are  expressed in  te-ms of
 ffnlt  emissions  are th? pounds
per pound  Per cubic  foot of
Diffusivit  Wa8 assumed to be G
                                                       °n rhe  ?
                                    a
                                  tv at
                                                =°
                                                   SCa=S'  Tabla 7-
                                              C°mbinacioas  of soil
                                             WaCer co^ents.

                                                     12~*«*
                                 Cnn,  , aaisslons  P«r  square foot

                                  ?       1011 ^  Che  b°tt0n sida'
-dfill operations
                 and


-------
                                TABLE 7-3

              UNIT EMISSIONS1*2 THROUGH  12-INCH SOIL COVERS
                   FOR SOILS  OF DIFFERENT DRY POROSITY
                                           Unic Emission (ft/hr)
 7.  Water'
     0
     5
    10
    15
    20
    25
Z Moisture  at  Zero
  Porosit^
Dry Porosity (Bulk density)4
0.3(113)
.056
.016
.0020
.0000032
-
-
15.3
0.4(101)
.083
.039
.015
.0036
.00033
-
24.7
0,5(84)
.111
.069
.039
.020
.0084
.0027
37.1
0.6(57)
.142
.10
.073
.050
.032
.020
55.3
    Cnits  are
Ib   /  Ib    or ft/hr;
        a-3
               rt  -cir
                                            0
                                            AC
2.  Diffusivity  in  air   -   0.23  ftVhr;  t  =  1  ft;
3.  Percent of dry  veighc

4.  Bulk density  (lb/ft3)  in  she-parentheses,  based  on
    density * 2.7

Source:  Arthur D. Little,  Inc.
                               T7-TS

-------
a .07
 .001
.0001
                                  Source: Arthur  D.  Liet^   Tnc
                                  |  ,                        — *" J  .ki-iV. • ,
                         10
                                    '5          20

                                  i Water (% of dry weignt)
  FiGURE  V-4   UNIT
                                                             A LANDFILL

-------
  proportional to cover  thickness.   For a 5  inch  cover,  the data  shown
  in Che table and figure should be multiplied  by  2.  Conversely,  for a
  24-inch cover,  these data should be divided by 2.

  rn -LiSpir% 7~t  Sh°.7  Che  ««-««   sensitivity  of   emissions  to
  conditions  in the soil.   For a given  soil type  compacted  to  a  given
  porosity,  the emission rate can vary over  several  orders  of magnitude
  depending on the percent  of water.   In the  steeper part  of the curves,
  a  change in only a  few percentage  points in water content  can make a
  substantial  change in  emission rates.

      The reduction in  emissions along any one of the  curves  in Figure
  V-4  is due  to  the  displacement  of air  filled voids in  the  soil  bv
  water.   At  some point, the pores will  become completely Billed  v< -h
  water  and  the emissions  will become  essentially zero.  ' The moistur-
  content corresponding to pore  saturation  is  indicated  at the  bottom  of
  Table  V-3.   Under  saturated conditions, organic compounds can  diffuse
  througn the water in the pores.  The rate of this process  is  very  slow
  compared^to  the  rate  through  air  and  has  been  assumed   to  be


      The extreme sensitivity to conditions  illustrated  in the  cu—es
  indicates  the critical significance  of  choice   of   cover  mater-'al
 compaction practices, and moisture control in achieving high  levels'  of
 emissions control when  using soil covers.  In most cases, the  choice
 or  daily cover materials  is made on economic  grounds  with the  result
 that materials   excavated  from  the  site  or  available   from   nearbv
 sources are  generally used.  It may be fortuitous  that these mat — ^'s
 have properties  desirable  from an emissions  control point of view  *  T*
 not, the  properties  can  be  altered  to  provide  lower  poros—v  ar~d
 cugner  moisture  retaining properties  by arising  in relaeivelv 'soa**T
 amounts of  clay  or  clay materials.                          ~       *"

      Hoistura  control   is  perhaps  the  most  important   -'ac—   -'n
 emissions  reduction.   Hut  little  attention  is  gene-a^v  — *»--  ~-\
 moisture  control.   Cover ratarials are often piled u=  unco-e-°--' Ta T_
 inactive  portion  of  the   sita.   The  moistura  content,  unde- ".--"s
 practice,  depends  on   the   recent  weather  patterns.   To   oi-m~~a
 emissions, daily  cover materials should be as w«t  as possible  ra-Iciv^
 to  the  maintenance of mechanical properties appropriate to  workab^li-v
 and  structural integrity.                                         --L-L-<

      Soil, synthetic  membrane,  or  combinations  of  the  two can be used
 for_ permanent covers.  As  is the  case for  soil materials, there  are
  r"l      availac.a ror vapor permeation through synthetic mamfar-nes
 or  t..e  type  anc  conriguration used as  covers  or liners.   Table  7-4
 presents data  recently  reported on permeation  rates for  a  var-'^-r 0-
 ;J?ar";al? \°r  S2vVaral differeac "Sanic  chemicals.   The data shown in
 this taole have been converted  into the same units  used to dist>iav  the
 soil  cover  characteristics  above.    Permeation  ratas  f-hraizh"  aU
 polymeric materials is highly dependent on the  chemical nature"of  eh-
duzusinz compounc.   Polar compounds such  as  acetone genial'y be^ava

-------
                              TABLE V-4
                      Xylene
                      Acetone
                      Chloroform

                 TEFLON1 - 4 MTT.S
 0.011
 0.00028
 0.0071
                     Xylene
                     Acetone
                     Chloroform
0.000008
0.00063
0.0027
Units are
           rt -hr

-------
  quite dirrerently  from hydrocarbons  such  as xylene  or  chlorinated
  hydrocarbons  such as chloroform.  In the 30 mil  polyethylene membrane
  the  permeation rate of xylene is about  50  times  that of  acetone,  but
  in a 4  mil Teflon  membrane,  the ratio  is  reversed.  Acetone  passes
  througr.  the  Teflon membrane  at about  100  times  more  raoidlv  than
  rylene,  but Terlon  remains more  effective in absolute terms.'

       It   is   important   to   note   that   the  magnitude   of   these
  permeabilities  fall within  the  range  obtainable  with  soi^ covers
  Four  points have  been  indicated on the  Figure 7-4  above to  represent
  typical  temporary and permanent soil cover conditions and 2 membranes.
  Points A and  B  respectively are located at  points  corresponding to
  conditions  that might  be  expected in a  temporary soil  cover and at a
  permanent  cover.    Point  C  and  D  represent  the  permeability   of  a
  neoprene   and  a   higher   performance   material  such   as   Teflon
  respectively.   The  synthetic  materials which  are often characterized
  as impermeaole  are  in  theory  of the  same  order of  effectiveness as
 properly designed and  maintained soil covers.   And,  if  water content
 is maintained  at  the saturation point,  soil covers  can theor-tica^y
 reduce   emissions   essentially   to   zero  (neglecting   liquid  phase
 diffusion), a  level unattainable with the polymeric  materials commonlv
 used in today's practice.

      Composite membranes  including  a  layer  of  Mylar,  a  uolyester
 polymeric  material, can  achieve  vapor  permeation  rates  that  are
 efrectively  unmeasurafale.   These   materials  have   been   used   in
 developmental   applications  in   food   containers   and  in   suec-'al
 protective  fabrics.   (Personal communication,  A.  Schwope).  Laminates
 in forms  suitable for  field  application  as  permanent cover mat*-als
 are presently  unavailable.

      As   components   of  permanent  covers,  synthetic  memb-*nes   ha**e
 several  advantages  relative  to soils.   Once' insta^d,  -he"-  i-e"uJ-»
 little maintenance  to maintain  their efficacy.   Performance over 'Non-
 periods or  time is,  however, uncertain.   The materials may deface  an'
 It  Cms occurs, would have  to  be replaced.  In practice, c-ac;ci-^  and
 nonhomogeneicies  in  the  materials   could si-if icantlv   raeac-'  cb«
 er.ectiveness  relative  to  the design  values.   Small fissu—s  <*. a
 cover  would act as  conduits  for the vapors generated within  a  ~ar»-
 area   of  the   landfill in   the   vicinity  of   the   crack.   Car-ul
 maintenance  or _the  cover including vegetation to prevent erosion, and
 installation or  sprinklers  to  maintain  moisture  content  at  uniform
 Bevels wiil  reduce the  probability  of  the formation  of  cracks.   The
 roots of  plants must be  prevented from penetrating the gas barrier.

     Maintaining appropriate moisture levels  is, however, inconsistent
with  groundwatar  protection  objectives  at   a  landfill.    Downward
infiltration of water  and  prevention  of leachata   fo-mat-'on  is  a
primary objective for covers from this  point  of  view.   Combinations of
a  soil cover and  membrane  can be designed  to  achieve  both  sets  o-
oojectives.

-------

   finite emission  rate    Tables
   7ear  through an acre  of  surface
   systems  depicted as  points A   B
   Emissions  are given  for  a      '
   landfill.  The table ind/cates
   in plica.  considerable  loss of
   occur.   Volatile  solvents  such  as
                                    as
  vapor  pressures of the order  of  100
  conditions.   Such comnounds if  nrp.l ,  P
  could be emitted  in Grange  of 'several met
  of  quite  low permeability'   X^S?-
  suitable cover material (E^A   197?^, %
  order of magnitude greater!
                                                           W±11 exhibic
                                                ^ancit7 of emissions  oer
                                                       to  the  four cover
                                                       Figura  V~L afa°ve.
                                            V*P"  concenc^tions   in   the
                                             ""* h±Sh Performance covers
                                            0?r°rb *™SS
                                                      &
                                                   per  million at ambient
                                                          «*il«t.d  form
                                                            «"idered  a
                                                    emissio*s  of  about  an
  organics at present.
  of  cover systems
      of  the
                                                             of volatile
       2.2  Post -Treatment
 leve l                       eu
 ultimately entering  the  atmosphere
 permeability, emissions  w^ll  conrn,
 all the materials  in the landfill h
 For very  effective  covers  t?ett
 hundreds  of  years.   Post-tr a Lent
                                                   "tlt*  of  missions
                                                         is SOme finica
                                                       ataosPhe^ oncll
                                                   into che atmosphere.
 atmosphere, abov^  the  landfall
 discussed above, the  syst^ e"
 systems  employing  extarra'  s
 configuration plus  adsor^t" on
 control means can be use"   The
 collection system.  The  treatment
efficient asca
                                                 -landfil-  or  from  Che
                                                             vapors  and
                                            C"CU"  =he Sasas-   2i=^«
                                                      °r °Cher =aseous
                                        o              primari^  °*  the
                                       ion  can  achieve high levels of
                                                               .
.«
        induction
sicuaclon..  I
crunches)  and Injection
   limited,  tn.  integrity
                 .ff.cei
                               "
                                                  ° e;-va    many
                                                 ars , <^l»ding lin.d
                                                  oo<1' but:

-------
                                 TABLE V-5
                             ANNUAL EMISSIONS
                                          Emissions (Ib/year-aeral
 Vapor  Concentration
        (ppnrv)	
         10
         50
        100
        500
       1000
       5000
      10000
      50000
     100000

Daily Cover
A
42
210
420
2100
4200
21000
42000
210000
420000
Final
Cover
B
1.0
5.3
10.5
53
105
530
1050
5300
10500
Neoprene
Caa
C
10.5
53
105
530
1050
5300
10500
53000
105000
Laminate
Can
D
0.1
.53
1.05
5.3
10.5
53
105
530
1050
Notas:
I.  A, 3, C, D refer t
o points on Figure 7-i
Source:  Arthur D. Little, Inc.

-------
    the        tlo^^ Sh-ld -tend  Co  bedrock
                        s^^^^^t
                 control strategy         ° * lad««i«» wells may be the
       3.  Costs

       3.1  Pretreataient
  were used.  Pretreat^ent CO8Cs  take^ f       ^ *"**«      n^ents
  the  range  of $1.00  per po^d  ^QQQ^J9^7 ee al"  C1984) are in
  incomxng waste  stream.  Cost  of other con?  ?   W3Ste  rem°Ved  "°°  «n
  of  pre-trwtMnt  costs  to  reflect  va-fr    *? C°mpared Co a "nge
  P-pert.es,  treatment type, s±z^d^~           «.  strj,
      3.2  Design and Operating Practice

      Installed cover system
     •  1979).   Membrane  cover  ^ayer^1™3^/  ara  shown  in Table V-6.
     s.  Costs depend on aiany site suacf^!.  *    timeS  as  exP«nsive
 De  Onnei J«—_j  •,          -^ -s-^'-c SpSCinp  rar-f-/^-^^   m»_ .    . _
                                                ticular sica
                                                           '

             ra                         ma_



passes  were  performed    v^ -  acaxeve  higher  comnaction -- exr-I
    3.3   In-Situ Controls



    3-4  Post-Traataent

-------
                               TA3L2 V-5


                ESTIMATED UNIT COSTS FOR SOi-E COVER LAYERS
           Layer Trae  and  ^^v—ss                              -nstallad Cosl
                   •        —~"	^s                                dollars/'.-c2
 Loose soil  (2 ft)

 Compacted soil (2 ft)
                                                                       0. /O
 Cement concrete (li -'r.)
                                                                       9.00
 Asphalt ccr.cra-a (I in.)                                          _ .. _ _
                                                                   2.jO-3.pO
 Soil-csnant (T in.)                                                   ,  _^
                                                                       i.jO
 Soil-asrhalt
                                                                       1. 50
 Polyethylene nenbrane (10 ail)r                                   l Q0_,  ..


 Polyviayl chlorida ae-brane (20 ail)                              1.^0-2.00

 Cilcrinatad ?ol"a-ir/lana =anbrana (20-20 ail)     .                , KO_-  ^

 Hi'palon aecbrane (20  ail)                                             _  _p

 ZTecprane aeabraae                                                      ^

 Zthylene prop'/lsr.a rubber aeabrana                                -_-.-,
                                                                   2.TG-J.>u
 3u-yl rubber asabraa-                                              ^  »     -
                                                                   2.iQ-3.30

 Paring asphal-  (2  in.)                                             1.20-1.-?

 Sprayed  asphal- nanbrana (lA  in.) and soil ccvar

 P.einfcrcad asphal- aeabraae  (ICO  ail)  and scil cover              1.50-2.00

 2e=tcni-3 layer (2 i«.)                                               . ,
                                                                      -.-"••j
~ Hot rasczsiandad becaus
     Sourca: U.S. Eavironmaatal Protacriou Agancy, 1979
                                    V-2S

-------

                                  TABLE  V-7
                                 0.4 Acre
  Air-Supported System
  Pipe  Vents
  Compacted  Soil Cover
  20-JtLl Hypalou Cover
                                                         6  Acre
c»tta
$150,000
80,000
2,000
6,500
AnnualizecP
$24,000
12,000
500
1,500
Cauital
$1,600,000 .
403,000
28,000
96,000
Annualiz
$250,000
60,000
5,000
15,000
 Nota:   1.
        2.
        3.
Treatment costs must be added to the f±surM 3hown. •
Cost in 1982 dollars.
                                                and  typical O&M costs
Source:  Arthur D. Little, Inc.

-------
     Costs for a post-treatment system based on collection by Beans of
vents  coupled  to  carbon adsorption or incineration  are  also shown in
Table 7-7.   The costs  ara  based on  a  pipe vent  system.   Pipe vents
include  the blowers  required  to drive  a  control  system.   Passive
trench vent systems might be used in situations where cover protection
is  the only function of  the gas  control.   Pipe vents  appear  better
suited  for  post-treatment applications.   The  costs presented  do  not
include the cover.

     4.   Cost-Effectiveness

     As  noted  in  the  introductory  paragraph  to this  section,  de-
finitions of an  uncontrolled,  reference landfill  is  rather arbitrary
since  covers  are  required  by  regulations,  but vary  widely in  per-
formance.  Thus, it is  not meaningful to  compare cover performance Co
other operating controls on the basis of pounds of volatiles removed.

     Notwithstanding  that   analytic  problem,  operating   practices
involving covers may  be extremely cost-affective, that  is,  providing
significant  emissions  reduction  for little  incremental  cost.   The
earlier discussion describing  emission  rata as a function of  cover
properties  indicates   that  several  orders  of  magnitude   or  more
improvement in performance  may be attainable  with  careful  practice.
The  costs  to achieve  this performance  can be  quite low.   Moisture
control of  daily   cover and  grain size  modifications  by adding  soil
conditioners,  clays,  etc.,  ara  not  expensive  relative  to  the  basic
operating  costs  at  a  landfill.   Under  these  circumstances,   the
cost-effectiveness  would   be  high,   compared   to   pratreatment,   for
example, expressed as pounds of volatile reduction per  dollar.   Even
the  added  cost of  heavier  earth-moving  equipment  to achieve  dansar
compaction should not change the cost-effectiveness very  much.

     The use of permeability reducing techniques  for permanent  covers
should  be  similarly  ccst-effactiva  comparad  to  conventional  design
approaches.   Lew vapor permeability soil and synthetic membrane  covers
do not  raprasant  significant  incremental costs.  Design  requirements
for covers ara  established currantly  by  regulations designed  to  raduca
or prevent surfaca watar infiltration.  Incremental  costs to maximize
gas control performance ara  small.

     Combination covers appear most effective.   Although  permeability
in  soil covers  can,   in  theory,  be reduced  to  zero,  it  would be
extremely  difficult  to  achieve  perfect   performanca   in   practice.
Imperfections  in soil covers, particularly in large cells, ara mora or
less inevitable.   Maintaining  high moistura content  runs  counter to
control  of  watar  infiltration.   Adding  a  synthetic  membrane  could
offset  these practical  difficulties without significant incremental
costs.  The cover  would prevent  watar  infiltration  from penetrating
into the closed call,  and would act as  a  seal to inhibit permeation
through cracks  in  the  soil layer.
                                7-23

-------
                     Even  as  performance approaches the  theoretical Unit, the-e  are
                two  Actors  which suggest  the  potential applications  of" alternative
                controls.   rirst,  as  noted,  practical performance  mav  not   reach
                theoretical levels.  There are no data currently available  to estate
                the  departure  from  theoretical performance.   Second,   covers  only
                retard the loss  or materials from the landfill.   Little  decav occurl
                in hazaraous  vaste landfills so  that,  with any  finite permeabilitv
                wastes wzll  continue to  enter  the  atmosphere.   The applications"of
                pre- or post-treatment can remove volatiles  permanently. "
                ehev !r f     K  costs are less than post-treatment  for  landfills as
                they are for other  kinds  of disposal facilities.  Thus,  unless  there
                is  some  technical  reason  that  pretreatment would  not be  practical
                post-treatment  would not  be the cost-effective  choice.   Pretreatment
                    s are expected  to  be less  than  five dollars per oound of  waste
                removed  (1-2 dollars/per  pound  have  been used in comparison,  above)?
                Post-treatment  costs are  expected to  exceed  about  five  dollars  per
                pound removed plus  the  costs of the collector (cover  or vent system"
                Thus,  pretreatment would  always be preferred.   Covers serve more  than
                one purpose; keeping out rain as well as keeping  in volatiles.  If  the
                covf,"11 ?,e  all°Catad  to SOTeral  Proses,  post-treatment,  using
                covers, would appear mora  cost-effective.                   -   -     °


               E.   Summary

                    Cover design and maintenance  present  the  most  cost-effac^ve and
               InS?!!*      ^  °r  emissi°n  "Auction Potential  of  all the  controls.
               In theory, emissions can be reduced to essentially zero bv  maintain*
               the  nores  ot a «urf 1 rmra-,- f,,tT  ~*  	    „   ..   . •  UittiUl-<:1-u-n-s
4,
|
j               organic vapors.
                    Combination cover  systems  with both  soil  layers  and
                      lnf^-4^'^ Va^ 'f*h ?«fo»«« 1—13 'for both vapor'  a
              water  inf.ltratxon  control.   Combinations   can  offse-  ,-ac-'-l
              limitations  in  soil  covers due  to  cracks and inhomcgeneities. " "   ~~^~

                    Very  little data are available that characterize currant  sracfce
              at  operating landfills  or at closed, previouslv  active  sites   The""
              is,  even  in this  situation,  a  reasonable ejection  chat oast  and
              current practices are poor with respect to vaoor control, and 'so eh"-
              scale    nC1S"  °P?°rtrait^  Co  "du« '»Por 'emissions  on  a  Stional
              11fflir                        the potential for emissions,  but nay have
              f^^1^1011-  C1 ChS  hiShl? v«i*bl. wastes that are  nlaced i"
              landfills.  Much  or  the wastes may  come  from widely disused  sma^
              generators.  These conditions limit the practicality 'of  Dret~4acmSt~~

-------
      Post-treatment  systems  have not been used  at landfills, but  the
 recent  installation of  an  air  inflated structure  at  a  landfill  in
 Louisiana  indicates  that this approach  can  be applied.  The  critical
 element  in a post-treatment  system is the collectors means.   Treatment
 technology is  proven but expensive.  The  covering structure  includes
 air  locks  to permit  vehicle  access  and prevents rainfall from falling
 on the site.
F.   References

EPA, 1979, Design and Construction of Covers for Solid Waste Landfills
(Prepared by R.J. Lutton, et al.).  S. Report No. EPA-600/2-79-165.

Farmer,  W.J.  at  al.,  1978,  Land  Disposal  of  Hazardous  Pastes:
Controlling Vapor Movement  in  Soils,  in  Proceedings of 4ch Annual EPA
Research Symposium.  EPA Report No. EPA-60019-78-015.

Haxo,  H.   et  al.,  1984,  Permeability  of  Polymeric Membrane  Lining
Materials,  Proceedings,  International  Conference  on  Gecmembranes,
Denver, CO.

Hwang,  S.T.,  1982,  Toxic   Emissions  from  Land Disposal  Facilities.
Envir. Progr., Vol. 1, No.  1 (Feb. 1982).

Schwope,  A.,   July  1984,   Arthur D.  Little,  Inc.,  Cambridge,  MA.
Personal Communications.

Spivey, J.J., C.C. Allen, D.A. Green, J.P. Wood, and  R.L.  Stailings,
1984.   Preliminary Assessment  of  Eazardous .Waste Pretraatment  as  an
Air  Pollution  Control  Technique.   Draft  Final  Report.    Research
Triangle  Institute,   Research  Triangle   Park,  NC.  "  For   the   U.S.
Environmental Protaction Agency,  IF.RL, Cincinnati,  OH.

Weiser, H.3.,  1949, Colloid  Chamistr-r, John Wiley and Sons,  New York.
                                V-30

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                     VI.   LAND TREATMENT FACILITIES
A.   Description
(Spivey ec al



                                                      .
                                               approximately 12  acres

                                                   ™
                                                               «  each
                                                      =    "
   The wastes  aay be anoiiad  to the  soil *m--a,-a  -•
   -'aues    -^a  ^t,^,-,-    '" -   i.         soix aur^ace  xr.


       'ch.^^^
           aost  Import

    rT.   The  four «jor

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       o    Overland  Flow - wastewatar  is  caused  to  flow over relatively
           Impermeable  soil with  a slope  from  about  2  to 82.   This
           technique is  used  for  treating  contaminated  run-off  or
           wastewatar errluents from industrial  processes.


       Following  the  application  of wastes to  the soil, the wastes inav
 be  incorporated into the  top layer  of  soil by standard  cultivation
 techniques.  The  soil may  be tilled  several  times following a single
 application  of wasta  before the next  application.   Typically,  the
 wastes are tilled into the top 4 to 8 inches (10   to 20 cm) of soil.

     _ In  some  settings the  sita  is  revegetatad.   In  this  case,  the
 surraca  is  not  tilled after each  application.   This  technique  is
 commonly used  to  treat  dilute wastes which can be anolied  bv  soray
 application.                                            ""
 3.    Emission Sources and Models

      1.    General

      Emissions  to the atmosphere  at a  land  treatment facility  ar^se
 from two primary sources.  The  first  is pools of liquid wastes  which
 form a,ter application on the surface.   These pools remain until  the
 liquids  see?  into  the underlying soils or are  incorporated  bv  t«U'-*
 Volatilization  directly  into the atmosphere can  occur as long 7s "the
 liquid wastes are exposed  at  the surface.

      The second source is  wastes which have been  incorporated  into  the
 soil.  Volatile  constituents in the wastes can ent=-"tbe  int—st-'c««
 ana  eventually  diffuse   to  the  soil  surface.   At  the  sur^ce "the
 emissions ais into the atmosphere and are swept away from the  site.

      2.   Emission Models

      2.1  Surfaca Emissions

     Emissions  from  a surfaca  layer of liquids behave  in the  sa-e
general manner as emissions from a floating layer of organic compounds
on a sur.ace  impoundment.   For  pure or highly  concentrated  organic
mixes, the tollowing equation describes  the emission rate:
                Ak  C
                  S
     where     Q    -    emission rata (Ib/hr)

               A    »    surfaca- area  (ft*")

               kg   *    aass  c=snsfar coefficient  (ft/hr)
                                71-2

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                      vapor concancracions of diffusing., component
                      in equilibrium with liquid, ib/ft
  and   k
        g
                      k  RT
 where
                     mass transfer coefficient  (lb-mol/ft2 hr)
                     gas constant (ata-ftJ/lb-mol - °R)
                     temperature (°R)
                     total pressure (atm)
      approprUt
                                             •"« Wllcitlon  of

                                                       "'   Xt  "
                                                        ™ 5
2.2  Emissions from Incorporated Wastes
species, is:
                                              he  ith  contaminant
     Q  -  AD ..
             err
    where:    0
                                             C )  X
                        flux race (Ib/ft2-hr)
         Deff

                                         of air filled pore space
                         air
         air      *    aolfcular   diffusivity  of   i   in  air
                       (tt /hr)

-------

               t

               A
        total porosity

        tortuosity factor  (T s 4)

        depth of surface injection  (ft)

        time after application Chr)

        surface area of application  (ft )

        depth of penetration of plow slice  (ft)

        initial mass of component i  (Ib)

        concentration  cz   i   on  gas  side  o
        interface (lb/ftJ)
     This model  is appropriate once  the waste has  been incorporated
into the soil.  It assumes:

     o    The soil column is isothermal
     o    No capilliary action
     o    No adsorption on soil particles
     o    No biochemical degradation

     This  rather  complex  equation  becomes  much simpler  under  two
separate  assumptions.   The  first  assumption is  that  the  waste  is
placed on the surface and immediately tilled.  In this case,  h  equals
zero.  This  equation,  rearranged  in terms of emissions  per  unit area
is:
     wnere:
               f
G  D .. (H ,„'
 2  err   o/A
                                          Deff/
                          2 h  t
                             P
2t D .. h
    err  o
             J
                       YMO/A'
     As long  as  the assumption of  no  biodegradation is valid,  i.e.,
for a  short time  following  applications,  the  Thibodeau-Hwang equation
indicates  that  emissions would  decrease  proportional  to  the  square
root of  time  expired after application.  Once biodegradation becomes
important, so that  vapor concentration, Cg,  decreases wiih  time,  the
relationship becomes sore complex.  Emission  rate would  decrease more
rapidly than  the  inverse square  root  form indicates.  The esact form
deuends on the aature of the behavior  of concentration with time.
                                                         •

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   SSSSakfca^^^^tg^^^'SJ^ngSS^ i-
  ,r  *           si?Plif?i:iS ^sumption is that  the wastes are  injected
  at  a  depth  equal  to  the  depth  of  penetration  of  the  ?low  or
  C                                     ho  «" Che equation  'becomes
          JL
           A

      Similarly  in  this  case, the emission  rate would remain constant
  the rariCtr  HChea, W°Uld ^"^ ^"^ C°  £he functional "orm of
  the relationship between concentrations and time.

      3.   Controlling Parameters

      3.1   Liquid Pools
 a liaidnnnl            pa"meter thac "n *• controlled  as long as
 Jj,qrt V °VS Present'   To m^i°i"  volatile emission, the time
 that the  liquid are  exposed should be kept as short as possible.

      3.2  Incorporated Wastes
 m™h^miS/i0nS'  °nCa ChS WaStaS  have  been  incorporated,  depend  on a
 number  of  parameters.   In  all cases, emissions  depend  in different
 For  th0^   °raS °U the  C0nceac^tion of  the  component in th.  ££?
 For  the  case vnera wastes are injected at  the same deoth as  the  olow
 cut   the initial emissions depends additionally only on the ef-ec-ive
 diffusivity and depth of injection.   The  deener  the  injection   ch^
 lower  vouxa  be the  emission  rate.   The  rate  defends  direct on
 errective  diriusivity.   Diffusivity  in   the   form  devoid  bv
 Thioodeaux  and  reported by Hwang  (1982) is  related to the oorositv of
 or fandf--  ^ C°r"°si="k fac="'  ^rosity as in the  case of  covers
 on eif        ?endS °n  Cha dSgras  =°  Which ch« sci- is compacted and

controllaole parameter for land treatment.
rfM^F°r-  Surfa? in^ecc:Lons' tlie initial emission rate defends on the
depth  or  the  plow cut, waste application rate,  and  time  (.nt'StW)
        S arfaCriVe <                concentration (implicit' function
                                   ly  with the square  root  of  time
                        In  this   configuration the  rate  depends
                                       rather chan che          *
inve^selv    r
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      The total emissions for a fixed area over a period of cine,  say a
 year, depend on the number of applications.   A given quantity of  waste
 can  be  applied  as fewer  and  larger  portions  or more  and  smaller
 portions.   The  total  emissions  over the period will  depend on  Che
 number of  applications.   The  forn  of  the  exact dependence  requires
 that the rate  equations  above be integrated.  The  integration cannot
 be  carried  out  analytically,  without  an  explicit  form  of   the
 relationship between  concentrations and  time,  which  depends on  the
 nature of  the  biodegradacion  process  and  on  its  coupling  to  the
 diffusive   mechanism.    This   relationship   is  complex  and  poorly
 understood  at present.

      The  equations were integrated  for  several possible forms for  Cg
 as a function of time  to  determine the general shape of  the  dependency
 on  application   rate.   The  results  indicate  chat  cotal  emissions
 increase  with increasing frequency  of applications;  thus, to control
 emissions  for  a fixed  quantity of   wastes  applied over  an  intended
 period,  the  maximum  quantity  consistent  vith  the  bicdegradative
 behavior should  be  applied  each time.
 C.    Controls

      1.    Introduction

      Emissions  from  land  treatment  can  be  reduced by  removal  of
 volatile  components of wastes prior to application.  Pretreatment will
 have  the  same  effectiveness   for  this  type  of  facility  as  those
 discussed  previously.   Post-treatment  techniques involving collection
 systems  in conjunction  with a  treatment process  can  also  be applied.
 The equations indicate chat the rate of emission is quits sensitive to
 a number  of  che  operating design  parameters.   There ara,  as  a resulc,
 several  control  methods  chat involve design  and operating practises.
 There  ara  no  available  control approaches  considered  as  in-situ
 methods for  this type of  facility.

      2.   Pretreatment

     Pratraat^aent  may  not  be  appropriate  or  effective  for  land
 treatment.   If  the biodegradation  processes  chat  occur  in  the  soil
 produce volatile  compounds from  the  breakdown of  heavier  molecules,
 then  pretreatment will not be  so  effective.   Pretreatment  may be  more
 an  alternative   to  land  treatment  not  an  adjunct,  since  both  are
 designed to handle the same kind of  organics.

     3.   Operating Practices

     Volatile emission  rate can  be  controlled  through  the  means  by
which the wastes are injected and by adjusting  the  amount  applied per
unit  area  per  pass.    Subsurface   injection  is  considerably  more
effective   in   controlling  emissions   than   is   surfaca   injection
 immediately  followed by   tilling.   Wastes  should be  injected at  che

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  maximum  depth  consistent  with  the  parameters  determine  the waste
  degradation  rates    Typical common depths of application range from 4
  to  8 incnes  (10-20  cm)  below the soil  surface hooding  and Shipp,
  19/9).   A variety  of  types  of  equipment  have  been  developed  for
  subsurface injection (EPA,  1983,  Overcash and Pal,  1979).  In some of
  these Devices,  the waste  is simultaneously injected below the surface
  and  mixed  into the  top 6 to  10  inches  (15  to  25  cm)  of  soil.   The
  initial  injection  may be followed closely  by a  second pass  with 'a.
  cultivator to distribute  the  waste  uniformly  across  the  treatment
  area.   Monographs  discussing  land  treatment  recommend  subsurface
  injection  for  wastes   with  volatile   components   and   odorous
  constituents.   Subsurface   injection  minimizes   exposure  of   the
  operators during application.

       Emission rate  is a weak function  of  the  application rate  per unit
  area.  For economic  reasons,  land treatment facility  operators apply
  ^J^^  WSfCe  Per  Un±t  area "Distent  "it*  the degradation
  capabilities  and carrying or  assimilative  capacity  of the soils   In
  practice,   application  rates  often  exceed' values   recommended  in
  conventional Design and guidance sources.   Emissions increase when the
  design  capacity is  overloaded because  degradation will be impeded and
  the volatile  materials  remain in the soil for longer periods* of time.
  Typical application rates  range  from about  one-half a pound per square
  foot  to aoout  three times  that  rate.   (EPA, 1983)
      th "JTi?  ^l11^ S0il P°rosi^ is Probably  not controllable but
  on       ri    --    t0 PreV6nt excassive drying.   If the soil becomes
 too dry   the  errective diffusivity can increase by  several  orders of
 Sf1^';- C K"  ^^ discussio* of  l««ills  for 'the  particulars of
 the  relationship  between  diffusivity  and   soil   porosity)     So'l
 moisture content should be maintained at the maximum level  consistent
 w..h  the  parameters   controlling  degradation  in  order  to   keen
 atmospneric emissions to a minimum.                                  ?

      -unu.0i  Ove.
                                T7T-7

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     D.   Effectiveness

     1.   Introduction

     The  effectiveness  of  controls  at  land  treatment  focusses  on
tilling  practices.   Prettraatment  and  post-traatment perform essen-
tially the sane as described in the preceding sections.  Emissions are
referred to surface applications as the uncontrolled case.

     2.   Emissions Reduction and Effectiveness

     Figure VI-1  indicates  the percent  of volatiles  applied  in land
treatment thac would be lost to the atmosphere through volatilization.
These curves are based on the equations developed above.   The emission
loss  relationships  and  the   data  generated  using  them  assume  no
biological  degradation.  This  assumption  is obviously unrealistic.
The  main function  of  land  treatment  for  organic  compounds is  to
provide degradation.  The actual emissions  and  percentage lost to the
atmosphere will  be less  than that depicted  herein for  this  reason.
Nevertheless, the equations and the data  are  useful in describing the
relative  effectiveness  of  a variety  of  alternate  controls.   The
results  shown  in Figure VI-1 are  consistent vith  data   taken  in the
fiald.  (Hinear  et  al.,  1981).  As  reported in  this reference,  oil
wastas spread and  tilled into soil resulted in losses of 0.62 and 27,
in  tvo  separate  field  tests  (Francke  and. Clarke,  197£,  and Suntech,
undated).  In another'tast reported in this sane reference, 11* of the
wastas from  an API  separator were lost  to the  atmosphere  (Suntech,
undated).  In this last test the wastes were spread on the surface but
not  tilled  into  the  soil.   Vapor concentration over  the  types  of
wastes treatad wera not  raported.  Based  on the  types of hydrocarbons
generally prasent in  the wastes  treatad,  the vapor  concentration can
be estimated.  A value of around 1,000 pom appears reasonable.

     The same kind of data ara shown in a somewhat different  format in
Table VI-1.   la  this table the  quantity  of volatile  lasses per  acra
per  year  is  shown  for  compounds  of  incraasir.g  vapor  pressure.
Comparison  of the  columns  for  surfaca  injection  versus  chose  for
subsurface injection  illustrate  the  reduction  that  is  theoretically
possible.  Figure VI-2  illustrates  the  raduction  efficiency  diractly.
The potential reductions shown in  Tabla VI-1 and Figure  VI-2  may noc
be  achieved  in  practice,  if  the  rate of  biodegradation is  reduced
sufficiently by  subsurface  injection.  Stated  alternatively,   if  the
rate of  degradation is  slowed down,  then there is more  time and  more
unreactad  materials  available for  volatilization.   The  efficiency
depends on the relative volatility  of  the  constituent.  Efficiency for
low volatility compounds is quite high  exceeding  902 for constituents
with vapor concentrations below about  1,000 ppo.   The efficiency falls
off  for  the  more  volatile   compounds.   For  reference,  the  vapor
concentration  in  equilibrium with benzene  at normal  temperatures  is
about  100,000  ppm.   The  corresponding  equilibrium  concentration  for
sylane is about  10,000  ppm.   The overall  effectiveness will  depend on
the particular -?!•? of comnounds in  the waste..
                                 VI-3

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          r      »
   too
1
                                                      100
                                             Vapor Concimlrutlon Ippmv)
                                                                               1.000
Source:  Arthur 1). Uttle,  Inc.,  J9»/,
                         FIGURE  VI-1  ARGENT OF VOLATILES LOST TO ATMOSPHERE
                                                                                                       10.000

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                              TABLE  VI-l





              ANNUAL LQSSZS FROM I ACRE OF LAND TREATMENT1
                               Injection  (h*)  and  Plow Depth (h )
                                            s                    p
Equilibrium
Vapor Concentration
(PPMV)3
10
50
100
500
1000
5000
10000
50000
100000
h
h - 4"
P
4.8
10.7
15.2
34
43
107
152
2872
2872
- 0
3"
3.4
7.6
10.7
24
34
76'
107
246
2S72
h
4"
.1
.2
.4
2
4
20
40
200
TO-?2
- h
P
8"
.05
.1
.2
1
2
10
20
100
200
Notes:






       Units ara aetric tons per year;  2S7  aetric  tons  applied per year




     2
       Complete (LOOS)  loss




     ^ Parts per ailiion by voiuae







 Source:  Arthur D. Little,  Inc.
                               VI-10

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             MOID;
               12Cyi.lus/Yr
                      Application lldlo
                                100
                                                       1,000
                                               Vapor Concuriiiiilion (p|>mv)
10,000
J	1  Mill.]
          100.000
Source: Arthur  1). Uttlc, Inc.,  l'J«4

       F.GURE VI-2  REOUCT.ON EFFICIENCY FOR SUBSURFACE INJECTION RELATIVE TO SURFACE INJECTION

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       3.   Costs

       3.1  Pretreatment
       PretTeatmen' c°scs «a  "snmed,  as above  to  be of  the  order of
  $1-2 per pound ($2,200-$4,400/Mg)  of wastes recovered.

       3.2  Operating  Practices

       The  more  effective  subsurface   injection   technique   is  oulv
  incrementally  more expensive than  surface  application.   The  addition
  «  nSfr CJ °? equlpme:15 Co a  tank  crx:ck spreader adds about  7%  (about
    '°  I  C?/?e CfSC  °r  Che syacaa  ^ercash and  Pal,  1979).   The labor
  cost  should be about the same for either applications  technique.
            _  application    rates    according,    to   the    Thibodeau-c
           up, woulc reduce emissions.  This control would be costly  as
 the  land  required to treat  a  given quantity  of  waste  would  inc-ase
 proportional  to  the  decrease  in  application  rate.   The  added "cost
 depends on the  cost of land.

      3.3  Post-Treatment

      Post-treatment using an air-supported cover  in  combination with
 ca.faon  adsorption or  incineration costs  the   same  as   these systems
 described in the previous chapters.

      4.   Cost  Effectiveness

      Based on the model used herein, subsurface inject"'on  is ^e m0st
 cost-errective   emission  control   for  land   treatment   facilities
 ^resucted  ernciency or reduction ranges from  about 20-40%  for h^hi-
 volatile  components  to   better  than   95%  for  low  vanor  p« ssu-'=>
 constituents.   The cost-effective curves, if plotted on  the  same t-^e
 or  rigure  usec  in the discussion  of  surface  impoundments  and  -anks
 would ^raij. below pretreatment at about  100  pounds per year,  a fj
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     _  In such a case, post-treatment using air-inflated structures plus
  incineration  or  adsorption  would  be  the choice.   If adsorption  is
  used,  the  recovered  wastes  can  be  reapplied.   In  this mode,  per-
  formance would  be  similar  to  that  of the  system described  earlier
  where recovered wastes are reinjected  in  the  aerated  imooundoent over
  which the cover is installed.



  E.    References


                                             (Prepared by K.W. Brown and
 Francke,  E.G.  and  F.E.  Clark,  Disposal  of  Oil  waste  bv Mi

    110"'     R±dSe Nati°nal Laboratory, Report No. VC-ll/Y-1934.
 Hwang,  S.T.,  1982,  Toxic  Emissions from  Land Disposal  Fac^'ties
 Envir. Progr.. Vol. 1, No. 1, (Feb. 1982).           '


 Minear, R.A. et al., 1981, Atmospheric Hydrocarbon Emissions from La-d
 Treatment  of  Refiners  on  ffaggM.  Am.^.M
 Washington, D.C.   Report No. DCN 81-219-060-06.
                                               °    an    reataent   or
                                Science  Polishers,  Inc.,  Ann Arbor,
                                                 '  aiid R'L-  ^tailings,
      P..             Assassmenc  of  Hazardous Waste  Pretraatment  as an
      PoLLucion  Control  T^±^T.   Drart  Final  Report. - Research
 .r.angle  institute, Research  Triangle  Park, NC.   For  the  U.S.  Envl
 ironmentax Protection Agency,  IERL, Cincinnati, OH.
                      iry  of  Results  from  Toledo,  Ohio.   Re^ae-r
         Tests, Suntech Environmental Group, Marcus Hookj ?A? undacad;

Vooding, H.S. and R.F.  Shipp,  1979.   Agricultural  Use and Disposal of
Septic Tank  Sludge.   In Pennsylvania  Znrormation  and recommendat-ons
tor  tarmers,  septage  haulers,  municipal  officials  and  ragulatorv
agencies.  Pennsylvania State University Coop.  Ext.  Serv.  Spec.  Circ'.

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TECHNICAL REPORT DATA
(Please read Instructions on the rtvenc before completing)
1. REPORT NO. 2.
EPA-450/3-84-017
A. TITLE AND SUBTITLE
Evaluation of Emission Controls for Hazardous Waste
Treatment, Storage, and Disposal Facilities
7. AUTHOR(S)
John R. Ehrenfeld and Joo Hooi Ong
9. PERFORMING ORGANIZATION NAME AND AOCHESS
Arthur 0. Little, Inc.
Acorn Park
Cambridge, Massachusetts 02140
12 SPONSORING AGENCY NAME AND ADDRESS
U.S. Environmental Protection Agency
Office of Air Quality Planning and Standards
Emission Standards and Engineering Division
Research Triangle Park, North Carolina 27711
3. RECIPIENT'S ACCESSION NO.
S. REPORT OATE
November 1984
6. PERFORMING ORGANIZATION CODE
3. PERFORMING ORGANIZATION 3S?ORT NO.
10. PROGRAM ELEMENT NC. ,
11. CONTRACT, GRANT NO.
68-01-6160
13. TYPE OF REPORT AND PERIOD COVE^EC
14. SPONSORING AGENCY COCE
EPA/200/004
15. SUPPLEMENTARY NOTES
IS. A3STHAC1
             The purpose of this report  is  to  evaluate controls for volatile
       emissions arising from the treatment, storage,  and  disposal  of hazardous
       wastes.  For each principal  type  of  hazardous  waste management facility,
       sources of atmospheric emissions  are  described  and  controls representing
       different approaches, are examined and  compared.   The evaluation  is based
       on actual data and on theoretical models  where  data are lacking or where
       the control technologies have  been borrowed  from  other types of applica-
       tions or are novel concepts.   The information  developed in preparing this
       report is intended to support  the analysis of  the regulation and  control
       of these volatile emissions.
                                KEY WOROS AND DOCUMENT ANALYSIS
                  DESCRIPTORS
                                              Ib.lOENTlFIERS/OPSN ENDED TERMS  C.  COSATI hlflu
  Air  Pollution
  Pollution  Control
  Hazardous  Waste TSDF
  Volatile Organic Compounds (VOC)
Air Pollution Control
18. DISTRIBUTION STATEMENT          ,.     ,,^-^c
 Release unlimited, Available  rrom  NnS
 5285 Port Royal Road. Springfield, VA
 22161
^^^••MM^H^M^MMMMMMMMMMHM^MM^^
EPA Form 2I2Q-1 (R*r. 4-77)   PREVIOUS EDITION i i O sso LSTI
                                               19. ScC'w'H
                                               UNCLASSIFIED
                                164
                                               20 SEC'JRIT^ CLASS {Tins
                                               UNCLASSIFIED
                                                                          12. PRICE

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