United States
Environmental Protection
Agency
Environmental Sciences Research
Laboratory
Research Triangle Park NC 27711
EPA-600/2-78-126
July 1978
Research and Development
Analytical  System
for Measuring
Malodorous
Compounds  from
Kraft Mills

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                RESEARCH REPORTING SERIES

Research reports of the Office of Research and Development, U.S. Environmental
Protection Agency, have been grouped into nine series. These nine broad cate-
gories were established to facilitate further development and application of en-
vironmental technology. Elimination of  traditional grouping was consciously
planned to foster technology transfer and a maximum interface in related fields.
The nine series are.

      1.  Environmental Health Effects Research
      2.  Environmental Protection Technology
      3.  Ecological Research
      4  Environmental Monitoring
      5.  Socioeconomic Environmental Studies
      6.  Scientific and Technical Assessment Reports (STAR)
      7.  Interagency  Energy-Environment Research and Development
      8  "Special" Reports
      9.  Miscellaneous Reports

 This report has been  assigned to the ENVIRONMENTAL  PROTECTION  TECH-
 NOLOGY series. This series describes research performed to develop and dem-
 onstrate instrumentation,  equipment, and methodology to repair or prevent en-
 vironmental degradation from point and non-point sources of pollution. This work
 provides the new or improved technology required for the control and treatment
 of pollution sources to meet environmental quality standards.
  This document is available to the public through the National Technical Informa-
  tion .ServJce,'. Springfield, Virginia 22161.

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                                                    EPA-600/2-78-126
                                                    July 1978
        ANALYTICAL SYSTEM FOR MEASURING MALODOROUS
                COMPOUNDS FROM KRAFT MILLS
                            by

James D. Mulik, Robert K. Stevens, and Ralph E. Baumgardner
        Atmospheric Chemistry and Physics Division
        Environmental Sciences Research Laboratory
       Research Triangle Park, North Carolina   27711
        ENVIRONMENTAL SCIENCES  RESEARCH  LABORATORY
            OFFICE OF RESEARCH  AND  DEVELOPMENT
           U.S. ENVIRONMENTAL PROTECTION AGENCY
       RESEARCH TRIANGLE  PARK,  NORTH CAROLINA  27711

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                                  DISCLAIMER

     This report has been reviewed by the Environmental Sciences Research
Laboratory, U.S. Environmental Protection Agency,  and approved for publica-
tion.  Mention of trade names or commercial products does not constitute
endorsement or recommendation for use.
                                        ii

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                                   ABSTRACT

     Automated chromatographs equipped with flame photometric detectors were
developed for the qualitative and quantitative analysis of low- and high-
molecular-weight sulfur compounds in kraft mill effluents.  One chromatograph
equipped with a Teflon column packed with Teflon and coated with polyphenyl
ether measured the following low-molecular-weight sulfur compounds:  hydrogen
sulfide (H S), sulfur dioxide (SO ), methyl mercaptan  (CH SH), ethyl mercaptan
(C2H5SH),  dimethyl sulfide  ((CH ) S) , and propyl mercaptan (C H SH).  A second
chromatograph equipped with a Teflon column packed with Teflon and coated with
Triton X-305 measured the higher-molecular-weight sulfur compounds:  butyl
mercaptan (C^H^SU), dimethyl disulfide ((CH ) S ), and dibutyl sulfide ( (C H ) S)

     Kraft mill effluents containing sulfur species ranging in concentrations
from 5 ppb to percent levels were analyzed using a 6-stage dynamic dilution
system.

     Sulfur emission data were collected from two kraft mills, one employing
strong black liquor oxidation and the other weak black liquor oxidation.   Part
of the study was dedicated to determining the relationship between the total
gaseous sulfur and the individual sulfur compounds observed chromatographi-
cally.  In most cases, more than 90 percent of the sulfur emitted from the
kraft mills studied was accounted for by chromatographically identified
compounds.

     This report covers a period from 1969 to 1971 and work was completed as of
December 1972.  For further information contact Robert K. Stevens, Environmental
Sciences Research Laboratory, U.S. Environmental Protection Agency, Research
Triangle Park, North Carolina  27711.
                                      iii

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                                   SECTION 1

                                 INTRODUCTION

     The growth of the kraft pulping industry has created a definite need for
more quantitative data on gaseous emissions from kraft paper mills.  Previous
studies by Brink, Thomas, and Feuerstein  (1) and Adams and Koppe (2) indicate
the complexity of identifying and measuring the pollutants generated by kraft
mill activities.  Highly sophisticated and complicated analytical techniques
are necessary to quantitatively characterize these emissions. Vital to the
analytical systems used, is a detector that specifically senses sulfur, as the
characteristic, unpleasant, decayed-vegetable odor related to kraft mill
activities is produced by sulfur compounds.  Adams and Koppe  (2) and Brink
et al. (1) used the microcoulometric detector designed to measure sulfur
constituents specifically as they are eluted from a gas chromatographic col-
umn.  Most gas chromatographic systems, however, have proven unreliable be-
cause many sulfur compounds (H_S, SO , and CH SH) are so reactive that they
fail to pass quantitatively through conventional gas chromatographic columns.
Koppe and Adams  (3) reported gross losses of these compounds at concentrations
below 10 ppm.   Walther and Amberg (4) described a process-chromatograph using
thermal conductivity and flame ionization detectors consecutively for sulfur
analysis.  A thermal conductivity detector was required for fixed gases such
as H S and SO  which have no flame ionization response.  By amplifying the
thermal conductivity detector signal, Walther and Amberg were able to detect
concentrations of H S as low as 2 ppm.  The flame ionization detector is
approximately a thousand times as sensitive as the thermal conductivity de-
tector and responds to all organic compounds.

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     Stevens, Mulik,  Krost,  and O'Keeffe (5)  reported on the first automated
gas chromatographic flame photometric analysis of sub-ppm levels of sulfur
compounds in the ambient air.  This technology led to the development of
methodology for analyzing sulfur compounds in kraft mill effluents.

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                                  SECTION  2

                                 EXPERIMENTAL

     The flame photometric detector  for the analysis of  sulfur compounds, as
described by the Draegers  (6) in 1962, was used by Crider  (7) in  1967  for
monitoring SO  in animal exposure chambers.  The  flame photometric detector of
Brody and Chaney (8), shown in Figure  1, was used by Stevens et al.  (5) for
the sub-ppm analysis of sulfur compounds in the ambient  air.  The flame
photometric detector measures sulfur compounds by detecting the chemilumines-
cent emission from the excited S  molecules formed whenever sulfur compounds
are burned in a hydrogen-rich air flame.  A narrow-band-pass interference
filter between the flame and the photomultiplier tube isolates a particular
band of the S  emission at 394 mp.  The interference filter virtually  elimin-
ates interferences from sulfur-deficient constituents.   Because only the
chemiluminescent emission above the flame is viewed, the background flame
noise is reduced.

     The gas chromatographic flame photometric system shown in Figure  2 was
developed to measure low-molecular-weight sulfur compounds in kraft mill ef-
fluents.  The analyzer consists of a Varian 122 gas chromatographic oven
(Varian Associates, Walnut Creek, California), a flame photometric detector
(Meloy Laboratories, Alexandria, Virginia), a power supply and electrometer
(Tracor, Austin, Texas), and a modified 10-part sliding  plate valve  (Beckman
Instrument Company, Fullerton, California) equipped with a 10-cc Teflon sample
loop, stripper column, and analytical column.  The function of the stripper
column is to vent heavier sulfur compounds by backflushing, thereby prevent-
ing them from reaching the analytical column.  The analytical column is 36-
foot by 0.085-inch I.D. Teflon tubing packed with 30/60 mesh Teflon and coated
with 10 grams of polyphenyl ether and 500 mg of orthophosphoric acid.  The 2-
foot by 0.085-inch I.D. stripper column is packed with the same material as
                                       3

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                      HEATED EXHAUST
 H2
INLET
                   COLUMN
                EFFLUENT INLET
                                      INTERFERENCE
                                         FILTER
                                               PHOTOMULTIPLIER
                                                   TUBE
|Z HEATER
                                          AIR INLET
        Figure 1.  Cross-sectional view of flame photometric detector.

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   FLAME
PHOTOMETRIC
 DETECTOR
       CARRIER IN N2
                                                            HEATED
                                                           EXHAUST
                                    NEEDLE
                                    VALVES
                     SOLENOID
                      VALVES
      15 MINUTE
     INDUSTRIAL
      CAM TIMER
                                             SAMPLE IN
                                         iiiiiiiiiiiiiiiiiiiiriiiiiiiiiin
                                           STRIPPER
                                            COLUMN
                 *  10 PORT
                  ESAMPLING
                  =  VALVE
                                                          SAMPLE
                                                          VACUUM
DEENERGISED
  POSITION
                                       ANALYTICAL COLUMN
Figure 2.   Automated gas chromatographic-FPD sulfur gas analyzer  equipped with a pre-colnmn,
           backflusing modifications, and a 36-foot by 0.085-inch Teflon column packed with
           Teflon  and coated with no.1 yphenyl ether.

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the analytical column.  Two solenoids and an industrial cam timer automati-
cally actuate the valve at 10-minute intervals.  The timing sequence to ac-
tuate the valve for sample injection, foreflushing, and backflushing is as
follows:

     1.  Valve is energized for 1 minute.
         a.  Sample is injected into stripper column and analytical column.
     2.  Valve is de-energized for 9 minutes.
         a.  Stripper column backflushes heavy sulfur compounds to vent
             while the analytical column continues to be foreflushed.
         b.  Sample loop is refilled.

     Th'j 10-part valve was modified to minimize the sample-to-metal contact
that can cause severe losses at levels below 10 ppm.  The fittings on the
valve connecting the 1/16-inch pipe to the 1/8-inch tube were drilled out so
that the Teflon lines would go through the fitting and into the body of the
valve up to the Teflon slider, thus making the valve essentially all Teflon.
The column exit was also fitted into the base of the detector to further
minimize sample-to-metal interaction.

     A chromatogram of a sub-ppm mixture of sulfur compounds which was ob-
tained using permeation tubes as a source of sulfur compounds is shown in
Figure 3.  Hydrogen sulfide, sulfur dioxide, methyl mercaptan, ethyl mercap-
tan, dimethyl sulfide, and propyl mercaptan were resolved in 10 minutes on the
36-foot by 0.085-inch I.D. polyphenyl ether Teflon column.  Chromatographic
conditions were as follows:

     •   Nitrogen carrier gas flow of 100 cc/minute.
     •   Detector temperature of 105°C.
     •   Exhaust temperature of 110°C.
     •   Column temperature of 50°C.
     •   Flame conditions:  hydrogen flow of 80 cc/minute; oxygen flow of 20
         cc/minute.

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     4 KlO'9a
     •»	•   —
      0.24 ppm
       S02
                                     2x109,

                                 0.17 ppm  0 18 pprr
                                 CH3SCH3  C2H5SH
                                                                                      2x10 -9 a
                                                                                      0 ?4 ppni
                                                                                      C3H7SH
                                                                                               10
                                          MINUTES
Figure  3.   Chromatogram of a mixture  of hydrogen  sulfide, sulfur  dioxide, methyl
            mercaptan,  dimethyl sulfide, ethyl mercaptan, and propyl mercaptan.

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     The analytical system developed for the  heavier  sulfur  compou >cls  is shown
in Figure 4.  A Teflon 6-port gas sampling valve  (Chromatronix,  Inc.,  2743
Eighth Street, Berkeley, California),  equipped with a 10-cc  Teflon  sample
loop, was used since backflushing was not necessary.   The analytical column is
10-foot by 0.085-inch I.D. Teflon tubing packed with  30/60 mesh Teflon coated
with 10 percent Triton X-305.  The lighter sulfur compounds  emerge  rapidly
from this column as one peak, followed by heavy sulfur compounds that elute
separately.

     A chromatogram of a sub-ppm mixture of high-molecular-weight sulfur
compounds is  shown in Figure 5.  Butyl mercaptan, dimethyl disulfide, dipropyl
sulfide, and  dibutyl sulfide were resolved in 10 minutes on the 10-foot by
0.085-inch  I.D. Triton  X-305 column.  Chromatographic conditions were as
follows:

     •   Nitrogen  carrier  gas  flow  of 100  cc/minute.
     •   Detector  temperature  of 105°C.
     •   Exhaust temperature of 110°C.
     •   Column temperature of 70°C.
     •   Flame conditions:  hydrogen flow of 80  cc/minute;  oxygen  flow of 20
         cc/minute.

      Teflon permeation tubes gravimetrically calibrated according  to the
 procedure  of O'Keeffe and Ortman (9) were used as primary standards.   The
 permeation tube assembly is shown in the upper right of Figure 4.   The instru-
 ments were calibrated by injecting aliquots of an air stream flowing over the
 tubes into the chromatographic column.   The concentration of the sulfur com-
 pound is inversely proportional to the air flow over the permeation tube.

      When kraft mill stack effluents are sampled directly, special sampling
 techniques are required to reduce losses due to the high moisture content and
 the wide concentration range of the sulfur compounds present  (ppb to percent
 levels).  Grimly,  Smith, and Martin (10) designed and constructed a dynamic
                                        8

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             GAS
       II  SAMPLING
       U)   VALVE
                                                                    PERMEATION TUBE
                                                                        ASSEMBLY
                                HEATED  EXHAUST


                                 FILTER
D.C. POWER
 SUPPLY
CHARCOAL
 FILTER
                                    PHOTOMULTIPLIER
                                       TUBE
                                                ELECTROMETER
                                                                                     AIR
                                                                                   SOURCE
Figure 4.  Automated gas chromatographic-FPD  sulfur  gas  analyzer equipped with a 6-port gas
           sampling and a 10-foot by 0.085-inch  Teflon column packed with Teflon coated with
           Triton X-305.  Also shown is the permeation tube sample dilution system.

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      4x10-* a
      0.22 ppm
      CH3SSCH3
             2x10-8 a
             0.21 ppm
             (C3H7)2S
                                                                      2 x 10'8 a
                                                                       0.18 ppm
Figure  5.   Chromatogram of a mixture  of propyl mercaptan butyl mercaptan,
            dimethyl disulfide, dipropyl disulfide,  and dibutyl sulfide.

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dilution system to bring the effluent samples into the inherently limited
dynamic range of the flame photometric detectors.  The dynamic dilution system
is capable of diluting effluent samples from a 10-to-l dilution to a 10 -to-1
dilution.
     To determine if the chromatographic peaks represent the total volatile
sulfur introduced into the chromatographs,  a Meloy total sulfur analyzer
continuously monitored the diluted sample.
                                       11

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                                  SECTION 3

                            RESULTS AND DISCUSSION

SAMPLING

     The chromatographs, sample dilution system and total sulfur flame
photometric detector were installed in a mobile laboratory, which was moved
first to a kraft mill employing the strong black liquor oxidation process and
then to a plant using the weak black liquor oxidation process.

     Figure 6 is a diagram of a typical chemical pulping operation.  The weak
black liquor oxidation plant investigated for this study differed slightly
from the typical plant in that the lime kiln had a separate stack vent.  In
the strong black liquor oxidation pulping operation, the emission from the
lime kiln was vented through a scrubber and into the recovery stack.  The
letters in Figure 6 designate the points where samples were extracted for
analysis.  Samples from each emission point were pulled to the dilution ap-
paratus through a 250- by 1/4-inch heated Teflon line.  The sampling line was
maintained at about 180°C to prevent sample condensation.  The probe was fixed
into position in the emission-source gas stream and sampled at a flow rate of
50 liters per minute.  Multiple measurements were made over a 3- to 4-hour
period at each sampling point to determine the extent of the variation in
concentration of the individual sulfur compounds with time.  Wide variations
in concentrations of the major constituents were not observed in this study;
the data contained in Tables 1 through 4 can be considered typical.
                                       12

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    BLACK LIQUOR
     OXIDATION
  Cr. ' IQUOR
OXIDATluN
                                 ELECTROSTATIC
                                 PRECIPITATOR  F2
                                                 DIRECT CONTACT
                                                  EVAPORATOR
                                       MULTIPLE EFFECT
                                        EVAPORATOR
\
Fl-


RECOVERY FURNACE


i
h
                                                                                    SCRUBBER
                                                                                          Jl
                                                                                            LIME KILN
                                                                                   DEMISTER
                                                                                           CAUSTICIZER
                                                                                  SMELT
                                                                                  TANK
   riqure  6.   Diagram of  a typical  chemical pulping operation.   Letters
                designate points  where  samples were extracted  for analysis.

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                                             TABLE 1.   STRONG BLACK LIQUOR OXIDATION

Sample point
Black liquor
oxidation vent
Knotter vent
Brown- stock
washer vent
Brown-stock
seal— frank v^nt-
Figure _
^ . „, Concentration, ppm
tion scfm H S SO CH3SH CH3SCH3 CH3CH2CH2CH2SH CH3SSCH3 Compound X
A 6,000 9.0 1.27 18.75 7.35 - 0.35 0.22a
B n.d.b tr° tr tr 3.22 - 3.30 tr
C 37,800 tr .29 tr 2.34 - .75 tr
D 1,970 268 tr 18.30 305 - 48 1.87
Inlet to direct-
contact evaporator  1
n.d.
             tr
                      244.0
                                                                              .21
*-*uu-t.cu L.VJ ti.i-i.ei-i.
contact evaporator 2
Precipitator inlet G
Precipitator outlet
Smelt-tank vent H
Non-condensables
to lime kiln
Lime kiln
scrubber inlet 1
Lime kiln
scrubber outlet 2
n.d. tr 164.70 - - -22
72,000 - 164.70 - - -
G2 31,000 - 146.40 - - - .12
20,000 2.08 tr -
10 291.2 - 5,720.0 6,240.0 - 572.0 tr
14,000 30.0 tr - - -
17,000 103.7 32.94 - - -
 Calculated as dibutyl disulfide

 Not determined
 Trace

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                                                    TABLE 2.  WEAK BLACK LIQUOR OXIDATION
        Sample point
                   Figure
                   designa-     Flow
                   tion         scfm
                                                    H2S
                                                         SO,,
                                                                             Concentration, ppm
                                                                         CH SH
                                            CH 3CH     CH CH CH CH2SH
                                                                                                                   CH SSCH     Compound X
tn
Black liquor
oxidation vent

Washer head vent

Multiple effect
evaporator inlet

Multiple effect
evaporator outlet

Direct contact
evaporator inlet

Direct contact
evaporator outlet

Precipitator
inlet

Precipitaor
outlet

Smelt tank
after demister

Non-condensables
to lime kiln

Lime kiln
scrubber inlet

Lime kiln
scrubber outlet
                           A


                           C
n.d.


n.d.


n.d.


n.d.


n.d.


n.d.
                                        15,000
                                        n.d.
                                        n.d.
                                        18,000
tr


2.27


14,400


tr


0.28


1.20
                                        100,000      1.28
                                        143,000      1.52
                                                     4.0
                                                     16.25
                                                     70.50
                                                                1.20
                                                                tr
                                                                tr
                                                                tr
                                                                tr
1.20


3.38


13,500


9,500






1.20


0.448


0.96


1.20


19,800


tr
0.80


3.90





4,500
                                                                                         0. 384
                                                                                         tr
                                                                                         0. 384
                                                                                         14,400
                                                                                         tr
                                                                                                         .28
                                                                                                         tr
                                                                                                         tr
                                                                                                         tr
                                                                                                         tr
                                                                                                         tr
10.40


 2.4


1,980


950


tr
                                                                                                                       tr
                                                                                                                       0.136
                                                                                                                       7,200
         Not determined
        o
         Trace

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              TABLE 3.  WEAK BLACK LIQUOR OXIDATION KRAFT MILL
Sample point
Figure
designation
                                            Total sulfur concentration,  ppm
     Gas
chromatography
Flame
photometric
detector
Black liquor
oxidation vent

Washer head vent

Multiple-effects
evaporator inlet

Multiple-effects
evaporator outlet

Direct-contact
evaporator inlet

Direct-contact
evaporator outlet

Precipitator
inlet

Precipitator
outlet

Smelt tank
after demister

Non-condensables
to lime kiln

Lime kiln
scrubber inlet

Lime kiln
scrubber outlet
                       12.4


                       12.3


                       29,880


                       14,950


                       1.50


                       2.80


                       1.7


                       2.5


                       7.7


                       41,400


                       16.3


                       70.5
                           17.0
                           12.4
                           17,100
                           15,250
                           1.80
                           1.80
                           1.1
                           1.3
                           7.2
                           39,600
                           16.3
                           70.5
                                      16

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               TABLE 4.   STRONG BLACK LIQUOR OXIDATION KRAFT MILL
Sample point
Figure
designation
                                            Total sulfur concentration,  ppm
     Gas
chromatography
Flame
photometric
detector
Black liquor
oxidation vent

Knotter vent           B

Brown-stock
washer vent

Brown-stock
seal-tank vent

Inlet to direct-
contact evaporator      1

Outlet to direct-
contact evaporator      2

Precipitator
inlet                   1

Precipitator
outlet                  :

Smelt-tank vent        H

Non-condensables
to lime kiln

Lime kiln
scrubber inlet          ]

Lime kiln
scrubber outlet         '<.
                       37.0


                       11.0


                       3.40


                       643.0


                       244.0


                       165.0


                       165.0


                       146.0


                       2.10
                           73.0


                           11.0


                           4.20


                           624.0


                           195.0


                           153.0


                           134.0


                           171.0


                           2.60
                       30.0
                       137.0
                           23.0
                           110.0
                                      17

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ANALYTICAL RESULTS

     The principal emissions from the kraft mills employing the weak black
liquor oxidation process were hydrogen sulfide and methyl mercaptan.  Trace
amounts, (that is, concentrations less than 5 ppb), of the following compounds
were also present:  sulfur dioxide, dimethyl sulfide, butyl mercaptan, dimethyl
sulfide and an unknown sulfur compound.  This unknown compound, (for this
text termed compound X), was the last to elute from the Triton X-305 column
and had a retention time of 17 minutes.  Dibutyl disulfide (boiling point
226°C) had a retention time of 16 minutes on this column; therefore, the un-
known compound probably has a boiling point greater than 226°C, or it is an
extremely polar compound.

     As noted in Tables 1 and 2, there was no chromatographic evidence of the
presence of a wide variety of sulfur compounds.  In fact, the chromatograms
were so uncomplicated that, at least for these plants, hydrogen sulfide and
methyl mercaptan can be considered the only significant emissions.  The un-
complicated nature of these emissions is important, as the correlation of
malodor with sulfur in the ambient air of this kraft mill cannot be totally
determined by a simple sulfide test, especially since the ratio of sulfide to
methyl mercaptan from the main recovery stack is roughly 1 to 1.  Tables 2 and
3 list:  (a) the sum of the sulfur emissions obtained by gas chromatography
from each sampling point; and, (b) the values obtained with the total-sulfur
flame photometric detector analyzer.  With the exception of the measurements
made at the inlet to the multiple-effect evaporator, the gas chromatographic
and total-sulfur measurements were in close agreement.  This indicates that
sulfur compounds identified chromatographically represent the majority of the
emissions.   The discrepancy in the values obtained from the multiple-effects
evaporator may have been the result of sampling problems caused by the high
concentration of particles, water vapor, and organics.

     The identified emissions from the strong black liquor oxidation process
are shown in Table 4.   Sulfur dioxide and hydrogen sulfide represent the major
                                       18

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pollutants emitted from this plant.  Again, the chromatographic data were
relatively uncomplicated although measurable quantities of dimethyl sulfide
and dimethyl disulfide were emitted to the atmosphere from several vents.

DISPERSION CALCULATIONS

     A measurement not made during these studies was the determination of the
concentrations of sulfur compounds downwind of the kraft mills.  Although
these determinations were not made, estimates of the impact of emissions from
the recovery furnace stack and lime kiln stack can be made using Turner's
dispersion estimates (11).  On the basis of Turner's calculations for a night-
time inversion,  (wind speed 3 meters per second), the concentrations of the
sulfur dioxide, hydrogen sulfide and methyl mercaptan from the weak black
liquor oxidation and strong black liquor oxidation kraft mills were determined
and are listed in Table 5.  Based on these estimates, the concentration of the
sulfur gases in the ambient air 6000 meters from the source, indicates that
the malodor impact of these gases would be negligible.

     The total malodor impact of a kraft mill on the surrounding community can
only be determined, however, by chromatographic measurements of the sulfur
gases downwind of the plant.  These determinations are necessary because a
typical kraft mill is comprised of many separate point sources, some emitting
only two or three sulfur compounds while others emit a variety of inorganic
and organic sulfur species.
                                       19

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              TABLE 5.  ESTIMATE OF ATMOSPHERIC DISPERSIONS OF
                         SULFUR GAS FROM KRAFT MILLS
                                Strong black liquor oxidation
             Source concentration, ppm   Estimate of abmient concentration, ppm
Emission
source
                               so.
                                         SO,
Recovery
furnace
stack
                               146
                                         0.004
Lime kiln
                103
33
                                           0.001
                             0.001
                                Weak black liquor oxidation

             Source concentration, ppm   Estimate of ambient concentration, ppm
Emission
source
                             CH SH
                                                                      CH SH
Recovery
furnace
stack
                1.52
0.96
0.001
0.001
Lime kiln
                70.50
            0.017
                                      20

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                                  REFERENCES

1.   Brink, D.L., J.F. Thomas, and R. Feuerstein.  Malodorous Products from
     the Combustion of Kraft Black Liquor.  Tappi, 50(6):276-285, 1967.

2.   Adams, D.F., and R.K. Koppe.  Direct GLC Coulometric Analysis of Kraft
     Mill Gases.  J. Air Pollu. Control Asso., 17 (1):161-165, 1967.

3.   Koppe, R.K., and D.F. Adams.  Evaluation of Gas  Chromatographic Columns
     for Analysis of Subparts per Million Concentrations of Gaseous Sulfur
     Compounds.  Environ. Sci. Technol., 1:479-481, 1967.

4.   Walther, J.E., and H.R. Amberg.  Mobile Laboratory for Source-Sampling
     Kraft Mill Emissions.  Tappi, 51(11):126A-129A,  1968.

5.   Stevens, R.K., J.D. Mulik and A.E. O'Keeffe.  Gas Chromatography of
     Reactive Sulfur Gases in Air at the Parts per Billion Level.  Anal.
     Chem., 43(6):827-831, 1971.

6.   Draeger, B., and H. Draeger.  West German Patent 1-33918.   Patent Date
     July  1962.
7.   Crider, W.L.  An Automatic Flame Emission  Instrument  for Selectively
     Monitoring SO  in Animal Exposure Chambers.   In:  Proceedings of the
     12th Annual Analysis Instrumentation Symposium,  1966.  pp.  67-73.
8.   Brodey, S.S., and J.E. Chaney.  Flame Photometric Detector.  The
     Application of a Specific Detector  for Phosphorus and  for  Sulfur Com-
     pounds Sensitive to Subnanogram Quantities.  J. Gas Chromatogr.,
     4(2):42-46, 1966.
                                       21

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9.   O'Keeffe, A.E., and G.C. Ortman.  Primary Standards for Trace Gas
     Analysis.  Anal. Chem. , 38 (6) -.160-763, 1966.

10.  Grimley, K.W., Jr., W.S. Smith and R.M. Martin.  The Use of a Dynamic
     Dilution System in the Conditioning of Stack Gases for Automated
     Analysis by a Mobile Sampling Van.  Presented at 63rd APCA Meeting,
     St. Louis, Missouri, June 1970.

11.  Turner, D.B.  Workbook of Atmospheric Dispersions Estimates.
     Public Health Service, Publication No. 99-AP-26, Revised 1969.

12.  Lindvall, T.  On Sensory Evaluation of Odorous Air Pollutant Intensities,
     Nordisk Hygienisk Tidschrift, Supplementum 2.  Karolinska Institutet,
     National Institute of Public Health, No. 5-104-01, Stockholm, Sweden,
     1970.
                                       22

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                                   TECHNICAL REPORT DATA
                            (Please read Instructions on the reverse before completing/
1. REPORT NO.
  EPA-600/2-78-126
                                                           3. RECIPIENT'S ACCESSION NO.
4. TITLE ANDSUBTITLE
  ANALYTICAL SYSTEM  FOR  MEASURING
  MALODOROUS COMPOUNDS FROM KRAFT MILLS
             5. REPORT DATE

              July  1978
             6. PERFORMING ORGANIZATION CODE
7. AUTHOR(S)
                                                           8. PERFORMING ORGANIZATION REPORT NO.
  J. D. Mulik, R. K.  Stevens  and
  R. E. Baumgardner
9. PERFORMING ORGANIZATION NAME AND ADDRESS
  Environmental Sciences  Research Laboratory
  Office of Research  and  Development
  U.S. Environmental  Protection Agency
  Research Triangle Park,  NC  27711
             10. PROGRAM ELEMENT NO.

               1AD712
             11. CONTRACT/GRANT NO.
12. SPONSORING AGENCY NAME AND ADDRESS
                                                           13. TYPE OF REPORT AND PERIOD COVERED
  Environmental Sciences  Research Laboratory - RTP, NC
  Office of Research and  Development
  U.S. Environmental Protection Agency
  Research Triangle Park,  NC  27711
               Final
             14. SPONSORING AGENCY CODE
               EPA/600/09
15. SUPPLEMENTARY NOTES
16. ABSTRACT
       Automated chromatographs equipped with flame photometric  detectors were
  developed for the  qualitative and quantitative analysis  of low- and high-
  molecular-weight sulfur compounds in kraft mill effluents.   One chromatograph
  equipped with a Teflon  column packed with Teflon and  coated with polyphenyl
  ether measured the following low-molecular-weight sulfur compounds:  hydrogen
  sulfide (H2S), sulfur dioxide (S0?), methyl mercaptan (CH^SH), ethyl  mercaptan
  (C2HrSH), aimethyl  sulfide ( (CrL)?S), and propyl mercaptan (C-H?SH).  A second
  chromatograph equipped  with a Teflon column packed with  Teflon and coated with
  Triton X-305 measured the higher-molecular-weight sulfur compounds:  butyl
  mercaptan (C.HgSH),  dimethyl disulfide ( (CH-)?S2), and  dibutyl sulfide (  (C.Hq)~S)
       Kraft mill effluents containing sulfur Species ranging in concentrations
  from 5 ppb to percent levels were analyzed using a 6-stage dynamic dilution
  system.
       Sulfur emission data were collected from two kraft  mills, one employing
  strong black liquor oxidation and the other weak black liquor  oxidation.   Part
  of the study was dedicated to determining the relationship between the total
  gaseous sulfur and the  individual sulfur compounds observed chromatographi-
  cally.  In most cases,  more than 90 percent of the sulfur emitted from the
  kraft mills studied  was accounted for by chromatograDhicallv identified compounds.
17.
                                KEY WORDS AND DOCUMENT ANALYSIS
                  DESCRIPTORS
  * Air pollution
  * Sulfur inorganic  compounds
  * Sulfur organic  compounds
  * Sulfate pulping
  * Chemical analysis
  * Chromatography
                                              b.IDENTIFIERS/OPEN ENDED TERMS
                             COSATI 1'ield/Group
                              13B
                              07B
                              07C
                              13H
                              07 D
18. DISTRIBUTION STATEMENT
  RELEASE TO  PUBLIC
                                              19 SECURITY CLASS (This Report!

                                                 UNCLASSIFIED
                           21. NO. OF PAGES

                              27
20. SECURITY CLASS iThi

  UNCLASSTFTFD
                                                                         22. PRICE
 EPA Form 2220-1 (Rev. 4-77)   PREVIOUS EDITION .s OBSOLETE
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