United States
 Environmental Protection
 Agency
 Industrial Environmental
 Research Laboratory
 Cincinnati OH 45268
Research and Development
 EPA-600/S6-84-008  Sept. 1984
Project  Summary
Testing and Evaluation  of  On-
Farm  Alcohol  Production
Facilities

William Kuby, Robert Markoja, and Steve Nackord
  This report gives  the results of a
sampling and analysis program managed
by the Industrial Environmental Research
Laboratory in  Cincinnati, Ohio (IERL-
Ci), to characterize the air emissions,
water  effluents, and solid residuals
from two on-farm ethanol production
processes sampled in June 1980.
  Gaseous emissions, both vented and
ambient, were analyzed in the field for
CO2, Oi, and hydrocarbons, including
some 21 alcohols and aldehydes. CO2
was the only compound identified in the
vents.  No significant increase in con-
centration  of  CQz was  found  in the
ambient air.  No other significant air
emission problems were identified.
  Liquid and  solid  samples  of the
feedstock,  make-up water, distillation
feed, byproduct, beer bottoms, product,
and washout water were analyzed in the
laboratory for priority pollutants, metals,
herbicides and pesticides, and other
standard chemical parameters (e.g..
Biological Oxygen  Demand, Chemical
Oxygen Demand). The most significant
result was the identification of very high
Biological Oxygen  Demand, Chemical
Oxygen Demand, Total Organic Carbon,
and Total Suspended Solids levels in
both process and waste  streams. The
streams were also  acidic (i.e.,  pH less
than 4). The levels of priority pollutants
were below current promulgated Re-
source Conservation and  Recovery Act
standards,  but some  metals exceeded
selected state standards.
  This Project Summary was developed
by EPA's Industrial Environmental
Research Laboratory, Cincinnati, OH,
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 objective of this program was to
test and characterize the effluents and
emissions from two farm-scale (approxi-
mately 6,000 gallons/year) ethanol
production facilities. The two sites were
in Kansas (Site A) and Nebraska (Site B).
In both cases, the feedstock was corn and
the enzymes used were a carbohydrate
enzyme (brand name Taka-therm) and a
glucohydrolase enzyme (brand name
Diazyme L-100). Surfuric acid was added
as a pH control.
  During the batch sampled at Site A, the
process produced  126 gallons of 88.6
percent (177 proof) ethanol from the 75
bushels of ground grain  (56 pounds
per bushel) or  a yield of 1  5 gallons of
anhydrous ethanol per bushel of ground
grain.  Ten  thousand and four hundred
pounds of byproduct for animal feed and
950 gallons of beer bottoms as waste
were computed from a mass balance
based on measured quantities and com-
position analysis. Section 5 of the full
report  contains a  detailed  analysis of
these effluents.
  During the batch sampled at Site B, the
process produced  about 13 gallons of
approximately 73.6 percent  (147 proof)
ethanol from the 15 bushels of  ground
grain (56 pounds per bushel) or a yield of
0.6  gallon of  anhydrous ethanol per
bushel of grain  A total of 3,350 pounds of
byproduct  for  animal feed and 145
gallons of beer bottons as  waste were
computed from  a mass balance based on
measured quantities and composition

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analysis. The Analytical Results section of
the full report contains a detailed analysis
of these effluents.
  The gaseous emissions, both vented and
ambient were sampled using an extractive
system. The sample  gas was also split
into two streams: one going to  a total
hydrocarbon monitor and the other to a
gas chromatograph. The total hydrocarbon
instrument monitored total  hydrocarbons
in the gas stream while the gas chroma-
tograph speciated the components of the
gas stream. Table  1 lists the compounds
screened for by the gas chromatograph.
The gas velocity in the vent was measured
by  using a hot wire anemometer flow
measuring  device. The sensing probe
was  inserted  upstream of the gas
sampling probe. Liquid and solid samples
were taken of each of the solid and liquid
effluents at the appropriate points.
  Methodologies used for organics
analysis are based on EPA Methods, the
FDA  Pesticide Analytical  Manual, and
Standard Methods lor the Examination of
Water and  Wastewater 14th  Ed. APHA,
AWWA, WPCF. Aqueous samples were
analyzed according to Table  2 and solid
samples were analyzed  according to
Table 3.
  Analytical methodologies used for the
general chemistry analyses were based
on Standard Methods for the Examination
of Water and Wastewater 14th Ed. APHA,
AWWA, WPCF, and Methods for the
Analysis of Water  and Wastes, EPA,
March  1979.  Aqueous samples were
analyzed according to Table 4. The
analytical   procedures for  high solid
samples were  basically the same as for
the liquid samples (Table 4).
  Metals were determined  by  atomic
absorption   spectrophotometry. Samples
were digested  with  nitric acid. Mercury
was  determined  by the cold  vapor
technique. Other metals were determined
by  either  flame  or graphite furnace
atomization of the acid digest.
Analytical Results
  The laboratory and field analytical
results are  presented and discussed in
this section. A  brief description of the
quality control procedures is also included.
The actual results for precision, accuracy,
and recovery experiments are given in
Appendix A of the full report.
  The laboratory analytical sample matrix
is shown in Table 5.  Table 6 gives the
ethanol content  in the various streams.
  The data are organized  as follows:
  • Conventional parameters
  • Metals, cyanide, and  phenols
Table 1.    Species Screened for by Gas Chromatograph
                                    Alcohols
Methanol
Ethanol
1 -propanol
2-propanol
1 -butanol
2-butanol
2-methyl 1-propanol


Formaldehyde
Propionaldehyde
Butyraldehyde
Isobutyraldehyde
Aldehydes
2-methyl 2 -propanol
1 -pentanol
2-pentanol
3-pentanol
2-methyl 1-butanol
3-methyl 1-butanol
2-methyl 2-butanol

Valeraldehyde
Isovaleraldehyde
Furfuraldehyde
 Table2.    Aqueous Samples

       Analysis
                            Method
Extractable organics by GCMS
Volatile organics analysis
  (purge and trap}
Herbicides
                            EPA 625
                            EPA 624

                            Standard
                              Method 509B
 Table 3.    Solid Organic A nalyses

     Analysis
    Method
                                 Note
Pesticides
Herbicides
Volatile organics analysis
  (purge and trap)
Base/neutral and acid
  fraction
 FDA 211  13e
 FDA 222.13c
 EPA 624

 EPA 625
Dilute with organic-
  free water
Soxhlet Extraction
Table 4.   Aqueous General Chemical Analyses

   Analysis
                     Method
BODs

COD

TOC
Total suspended
  solids
Total solids
Phenols
Cyanides (total)
Ammonia
Nitrate
Sulfate
Phosphorous

Specific
  conductance
Metals
pH
Total Kjeldahl
  nitrogen
     5-day incubation, sample analyzed for oxygen
      depletion
     Acid dichromate reflux, back titrate with ferrous
      ammonium sulfate
     Conversion to COz infrared quantitation
     Gravimetric,  105°C, weigh residue on filters

     Gravimetric,  105°C, weigh residue
     Distill, amino antipyrine color, CHC/3 extraction.
     Distill, barbituric acid colorimetry
     Distill, followed by nesslerization
     Brucine colorimetric
     Turbidimetric
     Nitric/sulluric acid digest, ascorbic acid
      colorimetry
     Wheatstone bridge conductivity

     Atomic absorption spectrophotometry following
      acid digestion. Analysis by cold-vapor flame-
      less AA (Hg), flame and graphite furnace analy-
      ses as appropriate for others
     Electrometnc
     Sulfuric acid mercuric oxide digestion, distillation,
      nesslerization
Metals: Al, Sb, As. Ba. Be, Bi, Cd. Ca, Cu. Cr. Fe, Pb, Mg. Mn, Hg. Ni. Se, Ag, Tl, Ti, and Zn

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    Priority pollutants
      — Acid compounds
      — Base/neutral compounds
      — Volatile organics
      — Pesticides and herbicides
  The process  waste  streams (beer
bottoms  and washout water) exhibited
certain common characteristics of  high
BOD5, COD, TSS and TOC, and low pH
(acidic).
  Solids  and oxygen  demand were
extremely high but decreased over  time
through the system. The analytical values
for Site B are probably on the low side
because of the warming of the samples in
transit. Laboratory analyses indicated that
most of the substances contributing  to
oxygen demand were biodegradable.
  The discharge  of the materials high in
free and bound  nutrients (i.e., nitrogen
and phosporous) stimulate biological
activity. All process  streams exhibit this
characterization.  Nutrients are an impor-
tant limiting factor  in the growth of all
plants. With all other factors being equal,
the rate and profuseness of plant growth
is proportional to the amount of nutrient
available. A high concentration of nutrients
will produce  rapid plant growth  first
becoming apparent as algae bloom. The
term "bloom"  is  used when the concen-
tration of individual species exceeds 500
individuals per milliliter of water.
  The  results from the metals analyses
indicate  that the corrosivity  (low pH)
problem might be significant. Metals (Ca,
Cu,  Fe, Mg,  Mn, and Zn)  detected  at
significant levels tended to increase  in
concentration through the system; how-
ever, the metals did tend to concentrate in
the byproduct even though the pH of the
byproduct and  liquid streams were
similar. The sources of metals throughout
the  process  included the  valves  and
general piping, squeezer trough, distilla-
tion  columns, and  holding and settling
tanks. The low pH of the process streams
may be leaching metals from equipment,
the majority of which were not stainless
steel. The increasing levels of copper,
iron, manganese, and zinc through the
process are indicative of this problem.
  Only traces of  a few priority pollutant
organics, herbicides or chlorinated
pesticides, were  detected in any of the
samples.  Except  for  the pesticides and
herbicides, these traces of  compounds
seemed to be contamination problems in
the laboratory rather than actual residues
of the  compounds. In the winter when
doors  would be closed, it  would  be
advisable to vent fermentation tank and
product tank emission to the outdoors to
prevent dangerous accumulations of COj
and ethanol in the work place.
Conclusions and
Recommendations
  The overall results indicate several
areas of concern regarding the environ-
mental  impacts from on-farm alcohol
production. Although primary concern
should be with those normal discharges
from the process, one must additionally
be concerned with the "dumping" of poor
batches and disposal of the solid materials
other than by byproduct  use, i.e., as a
feedstock.
  For the process liquid  and solid
streams, these concerns include high
oxygen demand, high nutrient content,
metals  in the process  streams  and
wastes, low pH (acidity), herbicide and/or
pesticide residues from feed grain  (but
this would be highly dependent upon the
feed grain supplier and the area of use).
Regarding air emissions,  particularly
during the  winter months, the only
apparent concerns are venting of C02for
safety reasons from the fermenter off-gas
and ethanol vapor from the product tank
to the outdoors.
  Finally,  a treatabihty study should be
performed on  all effluents and  off-
specification process waste to determine
appropriate waste treatment methods
and obtain treatment design criteria.
TableS.    Analytical Matrix
Site
A











B











Sample type
Make-up
water
Feed grain
Distillation
feed
Beer bottoms
Washout
water
Byproduct
Product
Cooker
runoff
Make-up
water
Feed Grain
Distillation
feed
Beer bottoms
Washout
water
Byproduct
Product
Soil
Soil control
I
X


X

X
X





X


X

X
X





§

* 1 6
«> -S> +
QL 3C Uj


X X
X

X
X

X
X
X



X X
X

X
X

X
X


*AI. Sb. As, Ba. Be, Bi. Cd. Ca. Cu, Cn, Fe. Pb. Mg. Mn. Hg. Ni. Se. Ag. Ti. H Zn

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  Table 6.   Analysis Results — Percent Ethanol by Gas Chromatography3
Sample type
Distillation feed
Beer bottoms
Washout water
Byproduct
Cooker mash runoff
Product
Site A
6.9
0.9
1.2
0.08"
Less than 0.5
87.0 (88.6 f
Site B
3.9
2.4
1.1
0.08"
71 0(73.6 f
  "Accuracy estimated at +10 percent.
  "Percent by weight.
  cNumbers in parentheses are results from hydrometer tests.
     William Kuby, Robert Markoja. and Steve Nackord are with Acurex Corporation,
       Mountain View. CA 94042.
     R. £. Mournighan is the EPA Project Officer (see below).
     The complete  report, entitled  "Testing and Evaluation of On-Farm Alcohol
       Production Facilities," (Order No. PB 84-215  789; Cost: $11.50, 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
      S GOVERNMENT PRINTING OFFICE, 1984—759-015/7819
United States
Environmental Protection
Agency
Center for Environmental Research
Information
Cincinnati OH 45268
Official Business
Penalty for Private Use $300
                               PS

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