United States
                    Environmental Protection
                    Agency
 Industrial Environmental Research
 Laboratory
 Research Triangle Park NC 27711
                    Research and Development
EPA-600/S7-84-007  Mar. 1984
vvEPA          Project Summary
                    Process Gas  Chromatography
                    Study of a  Selexol  Acid Gas
                    Removal  System
                    W. A. Williams
                      This report gives results of continuous
                    compositional monitoring by process
                    gas chromatography (GC) for three gas
                    streams  associated with  the Selexol
                    acid gas  removal system at the Bi-Gas
                    pilot plant in Homer City, PA. Data were
                    obtained from  the inlet and outlet
                    streams of the Selexol system during
                    tests in April and May 1982. During the
                    two tests, product gas composition data
                    were logged  for 55  hours of plant
                    operation.
                      The Bi-Gas pilot plant, utilizing a two-
                    stage, entrained-bed,  high-pressure
                    slagging  gasifier, produces a product
                    gas that  is  low in tars and heavy oils.
                    This gas stream required very little
                    cleanup prior to instrumental analysis.
                    However, some problems were encoun-
                    tered in the analysis of the Selexol acid
                    gas stream  due to the presence of high
                    levels of naphthalene. The process gas
                    chromatographs (GCs) performed well
                    and remained very  stable during the
                    tests. Material balances based on GC
                    analyses  and  process flow rate data
                    show a high degree of material account-
                    ability. The H2S removal efficiency of
                    the Selexol absorber  was about  99
                    percent during the tests.
                      This Project Summary was developed
                    by EPA's Industrial Environmental Re-
                    search Laboratory, Research  Triangle
                    Park. NC. 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 infor-
                    mation at back).

                    Introduction
                      As part of Radian Corporation's con-
                    tract,  "Environmental  Assessment of
Low- and Medium-Btu Gasification Pro-
cesses," with the U.S. Environmental
Protection Agency (EPA),  two sets of
process gas chromatographs were oper-
ated at the Bi-Gas coal gasification pilot
plant in Homer City, PA, during April 21 -
22 (Run 19A) and May 18-19 (Run 19B),
1982. The process GCs provided semi-
continuous monitoring (continuous data
logging) of two streams simultaneously.
The GCs were used to:

• acquire gas compositional data for the
   Selexol acid gas removal process,

• evaluate the potential for the use of
  this technique for monitoring gas
  streams in coal gasification facilities,
  and

• provide a means of "tracking" process
   operation in order to assess the condi-
   tions at which samples were collected.


  Concurrent with the data acquisition
aspect of EPA's  low-Btu program,  an
Electric Power Research Institute (EPRI)
program and a  Department of Energy
(DOE) program were  implemented. The
EPRI test program focused on emissions
measurement from  a coal  gasification
facility. The DOE program addressed the
environmental, health, and safety aspects
of coal gasification. This report focuses
on EPA's data acquisition results and
summarizes the plant operation and the
instrument operation for the process gas
chromatographs over the two test periods.
Reports being prepared by EPRI and DOE
will present detailed data and results for
the overall program.

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Process Description and
Test Schedule
  Radian conducted sampling and analy-
sis of process streams at the Bi-Gas pilot
plant in Homer City, PA, during three run
episodes (Plant Runs 19, 19A, and 19B)
during a 2-month period, April and May
1982. The Br-Gas pilot plant was funded
by the  DOE and operated by Steams-
Roger Engineering Corporation. The coal
used in the tests was  Pittsburgh No. 8.
During the tests, the nominal coal feed
and product gas generation rates were
—2000 and —6000 kg/hr, respectively.
  The first test of this series. Run 19, was
conducted in early April and  lasted  12
hours. No process GC data were obtained
during  this time. During  the next test
(19A)from 0800 hours on April 21 until
1600 hours on April 22,1982, the process
GCs were used to collect  compositional
data from the Selexol absorber inlet and
outlet gas streams.  The next test, 19B,
was conducted May 18-19, 1982. During
this test  period,  the process GCs were
used to monitor the Selexol inlet and
Selexol  acid gas streams. Two  sets of
instruments, each containing three gas
chromatographs, were used to monitor
hydrocarbons  (Ci-C4+), sulfur species
(H2S, COS,  S02, CS2), and major gases
(CO2, N2, 02, H2, CO, CH<).  In addition to
the EPA-funded process GC monitoring,
liquid- and gas-phase samples and oper-
ating data were collected from the Selexol
unit. Samples for analysis were collected
from all influent and effluent gas streams
including the  high- and  low-pressure
flash vents. Figure 1  is a schematic of the
Selexol  module, including the  sample
collection points.

Instrumentation

Instrument  Description
  Two  sets of process GCs were used
during'-the  test program: an Applied
Automation  (AA) Model  7170, and a
Bendix Model 7000.
  Both GC systems are housed in a 2.4 by
3.6 m trailer-mounted portable building.
The insulated enclosure is heated and air
conditioned  to provide a  stable atmos-
phere for the instruments and the data
acquisition system. All necessary electri-
cal wiring, instrument air filtration, and
drying  systems  are contained in the
enclosure.
  Each process GC system provides the
following detectors: flame ionization (FID)
for Ci-C4+ hydrocarbons;  flame photo-
metric for H2S, COS, SO2,  and CS2; and
thermal conductivity for CO2, CO, H2,  N2,
                  Selexol
              Absorber Outlet
            (To Thermal Oxidizer)
Absorber  —
                                 Legend

                                 Gas Sample
                                 Liquid Sample
                             I # |  Sample Point
                                                               Acid Gas
                                                               To Sulfur
                                                               Recovery
   Selexol
Absorber /n/ei,   ,  __,
  (From HP  (——*"
 Gas Washer)
                                                                Recycle
                                                              Condensate

                                                              Solvent
                                                              Stripper
 Figure 1.    Selexol acid gas removal system.
 02, CH«, and H2S. The FID of the Bendix
 Model 7000 was not operational during
 the tests due to an undelivered factory
 back order for parts.
   Three process streams were monitored
 during the tests. The sample acquisition
 system for the Selexol inlet and outlet gas
 streams was the same. The gas sample
 was taken from a valve tao, filtered, and
 the pressure reduced from 5250 to 440
 kPa using a stainless steel two-stage gas
 regulator. The sample was then trans-
 ported to the analytical instruments via
 heat-traced 0.64 cm Teflon tubing that
 was maintained at 394 K.
   The acquisition system for the Selexol
 acid gas sampler was similar except this
 gas stream was  not under pressure.
 Therefore, after filtration, a Teflon-lined
 pump was used to move the  sample
 through the heat-traced transport line.
   A separate gas conditioning system for
 each GC system was used to further filter,
 dry,  and deliver sample gas  to  each
 analyzer.  Each analyzer was equipped
 with a sample loop/valve injection system
 through which the sample was continu-
 ously purged. All the instruments utilize
 multiple columns and  automatic  valve
 sequencing for component speciation. A
 Spectra-Physics Model  4000 Integrator
 was  used  to record  and integrate the
 chromatographic output. The Integrator
 also  controlled the recycle time for the
 five operating GCs.
                               Instrument Operation
                                 The process GCs performed well and
                               remained very stable during the tests.
                               Limitations in the data obtained with the
                               GCs were caused either by (1) mechanical
                               problems with  plant operation,  or  (2)
                               stream compositions beyond the analyt-
                               ical capability of the instrumentation as it
                               was  configured during  the tests.  The
                               impact of mechanical problems with plant
                               operation on data collection is a reality
                               during any source test. The impact on the
                               process GCs can be minimized or elim-
                               inated by early reports of these problems
                               to the process GC operator. For item (2),
                               above, the sample preparation techniques
                               can easily be modified for subsequent
                               tests with the process GCs.

                               Results
                                 During the two  tests, the  analyses
                               conducted (with the process GCs) on the
                               individual gas streams were:
Run 19A,
April 21-22,
1982
 Selexol
 Absorber Inlet
 Selexol
  Absorber
  Outlet
                                                      Volatile
                                               Major  sulfur
                                               species species
                                                  V
                                                  V     V
 Light
hydro-
carbons
    v/

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Run19B,
May 18- 19, 1982
Selexol
Absorber Inlet
Selexol
Acid Gas



V

N/



V

N/
                                                                                  70
  Samples of the gas streams were col-
lected and analyzed approximately every
10  minutes  using the process GCs. In
addition, grab samples (gas bombs) were
collected three to five  times at each
location. Graphs depicting hourly aver-
ages  of the analyses  for major  gas
components are shown in Figures 2 and
3. Corresponding grab sample data are
also plotted  for comparative  purposes.
The discontinuity for the  Selexol inlet
data in Figure 2 is due to a temporary loss
of instrument carrier gas flow. The large
excursion around midnight during Test
19A reflects the shutdown of the coal
feed which occurred following the slag
burner  shutdown at 2310  hours.  As
shown in the figures, the process GC data
are generally in good agreement with the
grab sample  data.
  Average gas  compositions  for Tests
19A and 19B are shown  in Table 1. The
sulfur  species data  indicate  about  99
percent removal of HaS from the inlet gas
stream  during  Test  19A.  There also
appears to be some removal of COS;
however, the inlet analysis for COS for
both test periods was near the detection

  50

  45

  40
        1^   ^"S^^  >	>»
                         H2=38.0%
  30
Q.

§25
§70

  5
\   ,-.'-.*• CO = 31.5%
 \  /      *
 \ / NOTE: Data points
 \>  are grab samples.
                          CO2 = 15.1%
                                                     NOTE: Data points
                                                     are grab samples.
                                           50
                                           40
                                        
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  Table 1.    Average Gas Composition for the Bi-Gas Pilot Plant, Runs 19A and 19B
                              Run 19A
                         Run 19B
Species
H2
C02
N2
CHt
CO
HtS
COS
C*He
Ct+
Selexol
Absorber
Inlet
38.0%
15.1%
6.9%
8.6%
31.5%
0.41%
200 ppm"
36 ppm
1100 ppm
Selexol
Absorber
Outlet
41.4%
14.1%
6.6%
7.9%
29.9%
<4 ppm
76 ppm
NA"
NA
Selexol
Absorber
Inlet
37.2%
20.1%
4.9%
9.2%
30.0%
0.38%
WOppm"
NA
NA
Selexol
Acid Gas
ND"
51.5%
23.1%
ND
ND
12.9%
c
c
c
  "Not detected.
  ^Estimated value.
  "Unable to quantify; detector overloaded.
  aNot analyzed.
     W. A. Williams is with Radian Corporation, Austin,  TX 78766.
     William J. Rhodes is the EPA Project Officer (see below).
     The complete report, entitled "Process Gas Chromatography Study of a Selexol
       Acid Gas Removal System," (Order No. PB 84-158 336; Cost: $11.50, subjectto
       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
             Research Triangle Park, NC 27711
     U S. GOVERNMENT PRINTING OFFICE. 1984 — 759-015/7635
United States
Environmental Protection
Agency
Center for Environmental Research
Information
Cincinnati OH 45268
Official Business
Penalty for Private Use $300

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