Fuel Oil (FO) Non-Bunker

Fuel Oil (FO) Non-Bunker.

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Sl. No.	Characteristics	Unit	Method No.	Requirement
Sl. No.	Characteristics	Unit	Method No.	Grade LV	Grade MV1	Grade MV2	Grade HV
1	Acidity, inorganic	mg KOH/g	ASTM D974/ IP 139	Nil	Nil	Nil	Nil
2	Ash, Max	% by mass	IS 1448 [P: 4]	0.1	0.1	0.1	0.1
3	Carbon residue, mAX	% by mass	IS 1448 [P:122]/ISO 10370	14	16	18	20
4	Gross Calorific value	cal/g	IS 1448 [P:7]/[P:6]	Not limited but to be reported
5	Density at 15°C kg/m3 or Relative density at 15.6/15.6°C		IS 1448 [P: 16] or IS 1448 [P: 32]	Not limited but to be reported
6	Flash point, Pensky-Martens (Closed), Min	°C	IS 1448 [P:21]	66	66	66	66
7	Kinematic viscosity at 50°C Above	cSt	IS 1448 [P:25]/ ISO 3104	80 Max	80	125	180
7	Up to		IS 1448 [P:25]/ ISO 3104	80 Max	125	180	380
8	Sediment, Max	% by mass	IS 1448 [P:30]	0.25	0.25	0.25	0.25
9	Sulphur, total, Max	% by mass	IS 1448 [P:33]/ ISO 8754	3.5	4.0	4.0	4.5
10	Water content, Max	% by volume	IS 1448 [P:40]/ ISO 3733	1.0	1.0	1.0	1.0

S.N0.	Characteristics	Method No.		Requirement for Commercial
				Butane	Butane-Propane mixture	Propane
1	Density at 15°C,Kg/m³		[P:76]/ISO3993 D 1657	Report	Report	Report
2	Vapour pressure at 40°C, kPa, gauge, Max.		[P:71]/ASTM D 1267/D6897	520	1050	1550
3	Composition, Liquid volume percent a) C2 Hydrocarbons b) C3 Hydrocarbons c) C4 Hydrocarbons d) C5 Hydrocarbons and heavier OR		ASTM D 2163/ [P:151]	— Report Report 2.5 Max	Report Report Report 2.5 Max	Report 95.0 Min 4.0 Max 0.2 Max
3	Volatility: Evaporation temperature in °C for 95 percent by volume at 760 mm Hg pressure, Max.		ASTM D 1837-2011/[P:72]	2.2	2.2	-38.0
4	Total Volatile Sulphur ppm, Max.		ASTM D 3246/D6667	140	140	150
5	Copper strip corrosion at 38°C for 1 h		ASTM D 1838 / [P:152]/ISO6251	Not worse than No. 1
6	Hydrogen Sulphide		ASTM D 2420/[P:73]	Pass the test
7	Moisture Content		–	—	—	Pass
8	Free Water Content.		–	None	None	—
9	Caustic test			Pass	Pass	Pass