SEFK
                              United States
                              Environmental Protection
                              Agency
                              Industrial Environmental Researc
                              Laboratory
                              Cincinnati OH 45268
                              Research and Development
                              EPA-600/S2-81-072 Oct. 1981
Project  Summary
                              Evaluation  of  Solvent
                              Loss from  Vapor Degreaser
                              Systems Phases 2 and 3:
                              Effect of Crosscurrent Air
                              Velocity on Control  System
                              Performance
                              R. W. Gerstle and E. S. Schindler
                               The U.S. Environmental Protection
                              Agency (EPA) initiated a research
                              program to evaluate the solvent loss
                              reduction capabilities of various de-
                              greaser modifications, controls, and
                              operating practices of open-top vapor
                              degreasers. PEDCo Environmental,
                              Inc.. was contracted to carry out the
                              research program. The American Soci-
                              ety for Testing and Materials (ASTM)
                              was asked to assist EPA in defining
                              and formulating the test program and
                              reviewing its progress. A special
                              ASTM subcommittee of Committee
                              O-26 on degreasers was established
                              for this purpose.
                               This Project Summary was devel-
                              oped by EPA's Industrial Environmen-
                              tal Research Laboratory, Cincinnati,
                              OH, to announce key findings of the
                              research project that is fully docu-
                              mented in a separate report of the
                              same title (see Project Report ordering
                              information at back).


                              Introduction and Summary
                               The program began with the writing
                              of a detailed test plan, which was
                              .submitted to EPA for technical review.
                              The plan provided details of tests, test
                              location, types of solvents, variables and
                              control modifications to be tested,
                              parameters to be measured, and test
                              procedures. The results of these tests
                              referred to as Phase 1 were presented in
                              the report "Evaluation of Solvent Loss
                              from Vapor Degreaser Systems," No-
                              vember 1980.
                                Phase 1 quantified the ability of a
                              control device to reduce solvent loss
                              from a job-shop-size degreaser at the
                              ideal operating conditions suggested by
                              the manufacturer and EPA. It also tested
                              the effect of non-ideal operating con-
                              ditions on solvent loss, but did not
                              quantify the effectiveness of control
                              devices operating at non-ideal condi-
                              tions. The test data showed, however,
                              that a slight draft across the lip of the
                              degreaser increased solvent loss dra-
                              matically. On the basis of this increase,
                              the EPA decided that control devices
                              should be evaluated for the ability to
                              control solvent loss at high cross-
                              current air velocities: 0.67 m/s (132
                              ft/min) and 1.12 m/s (220 ft/min).
                                Phase 2 comprised the supplemental
                              tests that were performed to supply the
                              previous evaluation. Tests were also
                              conducted to supplement the Phase 1
                              data about variations in hoist speed.
                                Some Phase 2 results were unusual.
                              Although the refrigerated freeboard

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   chiller (RFC) substantially reduced sol-
   vent loss when methylene chloride (MC)
   was  used, it substantially  increased
   solvent loss when 1,1,1 -trichloroethane
   (TE) was used. Further, Phase 2 results
   indicated that changing the freeboard
   ratio (FR) reduced solvent loss only
   slightly, regardless of solvent. Phase 3
   was,  therefore, conducted to re-verify
   the Phase 2 results, further examine the
  -interaction of air velocity, RFC, and FR,
   and to explain the anomalies experi-
   enced in the Phase 2 testing.
     A separate set of plant site evalua-
   tipns were also conducted to characterize
   the cross-current velocities that typically
   are found in industrial sites. Seven
   plants were evaluated which included a
   broad range of industrial functions from
   aircraft manufacturers  to heavy ma-
   chinery manufacturing to small and
   large appliance manufacturing. The
   typical average cross-current velocity
   was found to be approximately .445
   m/s  (87.6 ft/min). Thus, the typical
   plant's cross-current draft characteristics
   were found to be within the boundary of
   this experimental program.

   Conclusions
     The conclusions that were developed
   from  the program characterizes and
   quantifies the effectiveness of various
   control options for vapor degreasers.
   Those conclusions, when combined
   with Phase 1 test results, are summa-
   rized  below.
     • An increase in cross-current veloc-
        ity will increase  solvent emission
        rates from open top  vapor de-
        greasers. A 40 percent increase in
        emissions is predicted at .67 m/sec
            over calm  conditions. The typical
            plant draft conditions were within
            the draft conditions of this research
            program. Thus, the emission rates
            determined during the program are
            typical of those which would be
            experienced in an industrial facility.
            Increased freeboard ratios will
            reduce emission rates. Increasing
            freeboard from .50 to .75 will de-
            crease emissions by 40 percent in
            some cases. Additional incremental
            reductions are achievable as the
            freeboard is increased above .75.
            Refrigerated freeboard chillers will
            reduce emission rates when used
            either by themselves or in combi-
            nation with other control options.
     Control effects of greater than 40
     percent are possible under some
     conditions.
  •  Automatic lids can assist in the
     reduction of solvent emission rates.
     Test indicated that the  use of an
     automatic lid can reduce solvent
     loss by greater than 50 percent in
     some instances.
  The best emission reduction technique
was found to be the  minimization  of
cross-current drafts at the  lip of the
degreaser.  However, some operational
constraints may prevent the lowering of
air velocity. Other  solvent  reduction
options, as previously  indicated, were
also  found to be effective in reducing
solvent loss.
           R.  W. Gerstle and E. S. Schindler are with PEDCo Environmental, Inc., Cincin-
             nati, OH 45246.
           Charles H. Darvin is the EPA Project Officer (see below).
           The complete report, entitled "Evaluation of Solvent Loss from Vapor Degreaser
             Systems Phases 2 and 3: Effect of Crosscurrent Air Velocity on Control System
             Performance," (Order No. PB 81-246 308; Cost: $9.50, subject to change) will
             be available only from:
                   National Technical Information Service
                   5285 Port Royal Road
                   Springfield. VA 22161
                   Telephone: 703-487-4650
           The EPA Project Officer can be contacted at:
                   Industrial Environmental Research Laboratory
                   U. S. Environmental Protection Agency
                   Cincinnati, OH 45268
                                                                                US GOVERNMENT PRINTING OFFICE, 1981 — 559-017/7364
United States
Environmental Protection
Agency
Center for Environmental Research
Information
Cincinnati OH 45268
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                Protection
                Agency
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