MIL-DTL-16884N
APPENDIX A
TABLE A-I. Detailed batch requirements; hydroprocessed SPD.
Requirement
Characteristic
ASTM Method
Minimum
Maximum
Acid Number, mg KOH/g
0.08
D974 (R), D664
D524 (R) 1/
Carbon Residue on 10% bottoms, mass %
0.20
D189 1/, D4530 1/
0.14
Cloud Point, °C
-1
D2500 (R), D5771,
D5772, D5773
Corrosion, 3 hours at 100 °C
No. 1
D130
Density, at 15 °C, kg/m3
770
805
D1298 (R), D4052, D287
Derived Cetane Number
42
80
D6890, D7170
D86
Distillation:
Report
Initial Boiling Point, °C
290
191
10% Recovered, °C
Report
50% Recovered, °C
357
290
90% Recovered, °C
385
300
Final Boiling Point, °C
Report
T50-T10, °C
20
T90-T10, °C
3.0
Residue + Loss, volume %
D93 (R) 2/, D3828
Flash Point, °C
60.0
Heating Value, MJ/kg
43.5
D4809
Hydrogen Content, mass %
14.5
D7171 (R), D4808, D5291
Kinematic Viscosity, at 40 °C, mm2/s
1.7
4.3
D445
DSEP
85
D7261
Particulate Contamination, mg/L
1.0
D6217 (R), D5452
D3241 3/
Thermal Stability:
25
Change in Pressure Drop, mm of Hg
3 4/
Tube Deposit Code, less than
Total Water, mg/kg
100
D6304
NOTES:
1/
Fuel must meet the requirements for one of the three test methods. If ASTM D189 or ASTM
D4530 is performed in lieu of the referee test method, ASTM D524, the maximum allowable
carbon residue shall be 0.14 mass percent.
2/
ASTM D3828 may give results up to 1.7 °C below the ASTM D93 results.
3/
4/
If the visual rating of the heater tube shows Peacock (P) or Abnormal (A) type deposits, the
fuel sample is not acceptable.
15
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