United States
                   Environmental Protection
                   Agency
Air and Energy Engineering
Research Laboratory
Research Triangle Park, NC 27711
                   Research and Development
 EPA/600/S2-90/016 June 1990
©EPA         Project Summary

                   Test and  Evaluation of  a
                   Polymer  Membrane
                   Preconcentrator
                   Kirk E. Hummel and Thomas P. Nelson
                    The report gives results of art
                  evaluation  of  the  applicability of
                  membrane   systems   as   a
                  preconcentrator  and  defines
                  operating parameters of a membrane
                  system. Advantages of such a system
                  is a  potential reduction in cost for
                  subsequent control systems. The
                  evaluation is part  of a  joint
                  EPA/California Air  Resources Board
                  investigation of the potential of
                  membrane  technology on  volatile
                  organic compound  (VOC) emissions
                  Tests of various membrane materials
                  and  configurations  have  been
                  conducted.  A potentially  innovative
                  application  of membrane technology
                  may  be to  concentrate VOCs from
                  exhaust gases such as solvent oven-
                  drying exhaust. A  preconcentrator
                  membrane could be used to reduce
                  the size and, in turn, the capital and
                  operating costs of a conventional
                  VOC control device such as a carbon
                  adsorber or incinerator. Study results
                  do not, however,  verify  that a
                  membrane  preconcentrator is a
                  viable option  to  reduce  overall
                  pollution control costs.
                    This  Project  Summary was
                  developed by EPA's Air and Energy
                  Engineering Research Laboratory,
                  Research  Triangle Park,  NC, to
                  announce key findings of the research
                  project that is fully documented in a
separate report of the same title (see
Project Report ordering information at
back).

Introduction
  The polymeric  membrane has been
used for  a  number of  years  as a
concentrating step for various liquid and
gaseous streams,  including removal of
large molecule organics from waste water
streams, hydrogen separation, and CO2
recovery. A polymer membrane  is  an
ultrathin layer of a selective polymer,
supported  on  a porous sublayer. The
membrane (active layer) selectively filters
the  pollutant  molecules. Figure  1 is a
diagram of a  bench scale membrane
system.  A  potentially  innovative
application of membrane technology may
be the concentrating of volatile organic
compounds (VOCs) from exhaust gases
such as solvent oven-drying exhaust. A
preconcentrator membrane could  be
used to reduce the size and, in turn,  the
capital and  operating  costs  of a
conventional VOC control device such as
a carbon adsorber or incinerator. The
overall result' would be  capital  and,
operating cost  savings, possible;
performance improvements,' and reduced;
energy requirements.
  The U.S. EPA  and the  California  Air
Resources Board initiated a joint program
to investigate the  potential  of membrane
technology on  VOC emissions. Tests of

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various  membrane  materials  and    of  the  membrane  and  associated
configurations  have been conducted.    equipment.
Objectives  of  those  studies  were  to
evaluate the applicability of membrane
systems as  a  preconcentrator and  to
define  operating parameters  of a
membrane system.  The advantage  of
such a system  is a potential reduction in
cost for subsequent control systems.

Program Approach
  Tasks completed for the study include:                             •
   (a)  A detailed literature review  of
       available  data  on membrane
       recovery of hydrocarbon vapors
       and  gases. Relevant  data and
       articles  on  the   subject  of
       membrane technologies are
       discussed in the report.
   (b)  Bench scale membrane modules
       were  tested using  six  common   "     ~ ~                    """•""
       solvents to define  capability  of
       membrane to  retain  solvents and
       to develop system operating
       parameters.
   (c)  Preliminary conceptual  designs
       were  developed  from laboratory
       studies.
   (d)  Preliminary capital and  operating
       cost  projections for membrane
       augmented control  options were
       developed.
  To support these tasks a bench-scale
polymeric system was designed and
constructed. The spiral-wound membrane
was  supplied   by   a commercial
membrane  manufacturer.  The bench-
scale test processed dilute gas streams
containing 20 to 2000 ppmv solvent.

Results and Conclusions
  The membrane was shown capable of
removing about  60%  of the  incoming
solvent,  and  generated  a permeate
stream about 3 times as concentrated  as
the original feed.  It was equally effective
on all six solvents tested. No noticeable
degradation in  performance of the
module was apparent  after the  tests,
although an extended performance
evaluation was not conducted.
  Based on  the test data  and  available
cost data for two simple configurations,
membrane technology  does not appear
to be  a good  alternative to carbon
adsorption  or  other  classical control
options for low concentration  (e.g., 100
ppmv) solvent-laden  air streams at this
time. The capital and annualized costs of
the membrane-augmented system were
consistently  higher than for the carbon
adsorber alone. Cost  reductions for the
membrane-augmented  carbon  adsorber
(due to the  reduced  volume flow) were
not sufficient to cover the added expense

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                                                                     i (To Vent)
                                                           (Recycle)
                               j  ! Clean Air
                                  (To Vent)
                                     VOC
                                   Emissions
                                                                       Stripped
                                                                       Off-gas
               VOC Source
                                                      Membrane
                                                   Preconcentrator
Concentrated
  - VOC
                                                                                            Final VOC
                                                                                          Control Device
                                                                                                          Recovered VOC
                                                                                                            (Solvent)
Figure 1.  Membrane preconcentrator system..

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  K. Hummel and T. Nelson are with Radian Corp., Austin, TX 78720-1088.
  Charles H. Darvin is the EPA Project Officer (see below).
  The complete report, entitled "Test and  Evaluation  of a  Polymer Membrane
        Preconcentrator," (Order No. PS 90-188 905/AS; Cost: $23.00, 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:
            Air and Energy Engineering Research Laboratory
            U.S. Environmental Protection Agency
            Research Triangle Park, NC 27711
United States                   Center for Environmental Research
Environmental Protection         Information
Agency                         Cincinnati OH 45268
Official Business
Penalty for Private Use $300

EPA/600/S2-90/016

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