15.
ASTM D4806 for ethanol used for fuel Property
Limits
Units
Ethanol 92.1 min. % v/v
Methanol 0.5 max. (5,000 ppm) % v/v
Water
1.0 max. (10,000 ppm)
% v/v
Solvent-washed gum 5 max. (50 ppm) mg/100 mL
Chloride ion
40 max. (40 ppm) mg/L
Copper content 0.1 max. (0.1 ppm) mg/kg
Acidity as acetic acid 0.007 max. (70 ppm) % w/w
Appearance
Visibly free of suspended or
precipitated contaminants
Denaturant
Minimum 1.96% v/v and maximum
4.76% v/v natural gasoline, gasoline components or
unleaded gasoline.
16.
*Quarterly Denatured Ethanol Testing Requirements:
Proof
Apparent Proof
ASTM E1064
Water by Coulometric Karl Fischer
ASTM D5501
Ethanol Purity
ASTM D6423
Determination of pHe
ASTM D381
Existent Gum
ASTM D512
Chloride ion
ASTM D1613
Acidity of Ethanol
ASTM D1688
Copper
ASTM D5453
Sulfur
**Monthly Denatured Ethanol Testing Requirements:
Proof
Apparent Proof
ASTM E1064
Water by Coulometric Karl Fischer
ASTM D5501
Ethanol Purity
ASTM D6423
Determination of pHe
ASTM D1613
Acidity of Ethanol
Optional testing for an additional:
ASTM D5827
Sulfate by Ion Chromatography
***Denaturant Testing Requirements:
ASTM D5580
Benzene, Total Aromatics
ASTM D6550
Olefins
Optional testing for an additional::
ASTM D5453
Magellan E85 and Ethanol Testing
17.
ASTM D 4806
Standard Specification
for Denatured Fuel
Ethanol for Blending with
Gasolines for use as
Automotive SparkIgnition Engine Fuel
ASTM D 5798
Standard Specification
for Fuel Ethanol (Ed75Ed85) for Automotive
Spark-Ignition Engines
ASTM Standards for Fuel Ethanol
Performance Specifications
18.
19.
20.
21. ASTM D4806 (California)
Parameter Limits Test Method Frequency
Each batch
“calculated”
Olefins, 0.5 D6550-00
vol%, max
Each batch
“calculated”
Aromatics, 1.7 D5580-00
vol%, max
Each batch
“calculated”
Benzene, 0.06 D5580-00
vol%, max
Quarterly
Third party
Sulfur, ppm 10 D5453-93
California Requirements Differ
22.
California Denaturant Standards
Parameter Limits Test Method
Frequency
Olefins, 10 D6550-00 Each batch
vol%, max
Aromatics, 35 D5580-00 Each batch
vol%, max
Benzene, 1.1 D5580-00 Each batch
vol%, max
23. Producer name and
location
Traceable lot number
Load date
Quality results, limits
and test method
used
Quarterly third party
lab results statement
Certificate of Analysis
28. DP = Degree of
Polymerization
number of dextrose
molecules linked together
examples:
DP1, DP2, DP3, DP4…DP10…
29. The extent of starch hydrolysis is expressed as Dextrose Equivalent
(DE). DE is the percentage of glucosyl bonds that have been
broken.
Dextrose is another word for D-glucose.
So, DE will be low (4 - 6) at the beginning of the process such as
the Slurry tank outlet.
Meaning: Mostly large molecules exist and not many molecules of
glucose.
30. DEXTROSE
EQUIVALENT (DE)
When the DE is 100, all of the bonds between glucose units in
the starch have been hydrolyzed. About 10% of the starch
bonds are broken by the end of Conversion and up to half of
the bonds are broken coming out of Saccharification.
If half of the starch bonds are hydrolyzed the average DP is 2
and the
DE = 50
example: 25% DP1 + 25% DP3 + 50% DP2 = 50 DE
If a fourth of the starch bonds are broken the average DP is 4
and the
DE = 25.
DE determines the average DP length of the liquefied mash.
31. Estimation of DE from
HPLC results
%DP1 * 100 + %DP2 * 50 + %DP3*33+
%DP4*10
_____________________________________
___
% Solids
= est. DE
33. Milling: Grind size effects
–
A large particle size can be more difficult to gelatinize
since enzyme cannot react with the substrate efficiently.
This can result in yield loss (up to 10%).
–
A small particle size (< 200 mesh) can also cause
problems:
Mixing of floured grain in water may be more
difficult.
Small particles will also cause problems in
centrifugation, evaporation, and drying.
May have some positive effect on theoretical yield
due to enzymes’ ability to react with starch.
Typical Size : Mill grain to 100% thru 16 mesh
34. Slurry: Gelatinization
The mash is cooked at 170 – 185 degrees to
gelatinize most of the starch and break the viscosity
enough to be pumpable.
Alpha-amylase and water molecules together are
randomly breaking down (or hydrolyzing) the
amylopectin (branches) part of the starch structure.
The alpha amylase produces a mixture of short
sugar molecules (e.g. maltose, maltotriose), and
some dextrin molecules (longer molecules of sugar).
4 - 6 DE mash
35. Liquefaction
Alpha amylase is denatured in
Liquefaction primarily because of
heat.
The heat further breaks down
starch molecules for the second
addition of alpha amylase.
DE of 12 – 14
36. Purpose of Fermentation:
To produce ethanol through the anaerobic
conversion of glucose by yeast.
51% of the glucose is converted to
ethanol and 49% is converted to carbon
dioxide
Ethanol Level at end of
Fermentation is typically 12 15% v/v.