GASOLINES — FEEDSTOCK FOR PYROLYSIS are produced in accordance with TU 38.402–62–120–90 “Gasolines — pyrolysis feedstock. Specifications”:

No.	Property	Unit of measurement	TU 38.402–62–120–90 Straight-run gasoline
			A	B
1	Density at 20 ˚С, max	g/cm3	0.725	Not rated
2	Distillation:
	a) initial boiling point, min	˚С	35	35
	b) 10 % of the product distilled at, max	˚С	75	Not rated
	c) 50 % of the product distilled at, max	˚С	105	115
	d) 90 % of the product distilled at, max	˚С	150	Not rated
	e) Final boiling point, max	v	170	180
3	Hydrocarbon composition:	%
	а) Aromatics mass fraction, max		7	10
	б) Naphtenic hydrocarbons mass fraction, max		35	Not rated
	в) Paraffinic hydrocarbons mass fraction, min		55	Not rated
4	Iodine number, max	g of I / 100 g of product	1.0	2.0
5	Sulfur mass fraction, max	%	0.05	0.1
6	Copper corrosion test	passes
7	Sediments and water content	none
8	Water‑soluble alkalis content	none
9	Existent Gum, max	mg / 100 cm3 of the product	2	Not rated

VACUUM GASOIL is produced in accordance with TU BY 300042199.008–2008 “Mixed vacuum gasoil. Specifications” and in accordance with contract requirements. Vacuum gasoil is designed for usage as a raw materials component for secondary oil refining processes.

No.	Property	Mixed vacuum gasoil	Vacuum gasoil
		TU  BY300042199.008–2008	As per contract
1	Kinematic viscosity at 50 ˚С, mm2/s	25.1–90.0	‑
2	Density at 20 ˚С, kg/m3, within range	860–950	860–950
3	Sulfur,% wt., max	2.0	2.0
4	Flow point, ˚С, min	19	19
5	Closed cup flash point, ˚С, min	61	61
6	Coking capacity,%, max	0.7	0.7
7	Density at 15 ˚С, kg/m3, within range	‑	873.4–953.3
8	Vanadium,% wt., max	‑	00 005

GRADE KO-20 LAMP KEROSENE is produced in accordance with TU 38.401–58–10–01 “Lamp kerosenes. Specifications” and is designed for usage in lamps, kerosene heaters, kerosene stoves and other analogous appliances.

No.	Property	КО‑20
1	Distillation:
	% recovered before 270 °C,%, min	80
	98 % recovery at, °C, max	310
2	Smoke point, mm, min	20
3	Closed cup flash point, °C, min	40
4	Cloud point, °C, max	Minus 12
5	Sulfur,% wt., max	0.1
6	Copper strip corrosion test	Passes
7	Acidity, mg КОН / 100 cm3 of kerosene, max	1.3
8	Ash content,%, max	0 005
9	Color, KNS reference units, max	15
10	Water soluble acids and alkalis content	None
11	Sediments and water content	None
12	Density at 15 °C, kg/m3, max	834

INDUSTRIAL ECO-FRIENDLY KEROSENE is produced in accordance with TU BY 300042199.025–2011 “Industrial eco- friendly kerosene. Specifications” and is used for technical purposes.

No.	Property	Commercial eco‑friendly kerosene
1	Appearance	Clear, transparent liquid without water, sediments and particulate matter at ambient temperature.
2	Total acid number, mg КОН/g, max	1.3
3	Sulfur,% wt., max	0.001
4	Smoke point, mm, min	20.0
5	Copper corrosion test (3 h ± 5 min at 50 °C), scale units, max	Class 1
6	Kinematic viscosity at 20 °C, mm2/s, min	1.25
7	Distillation:
	‑ initial boiling point, °C, max	140
	‑ 50 %(V/V), recovered at, °C, max	210
	‑ 98 %(V/V), recovered at, °C, max — distillation residue,%(V/V), max — distillation loss,%(V/V), max	310 1.5 1.5
8	Closed cup flash point, °C, min	40
9	Water soluble acids and alkalis content	None
10	Density at 15 °C, kg/m3, max	835

HYDROCRACKING RESIDUAL PRODUCT is produced in accordance with TU BY 300220696.034–2005 “Hydrocracking residual product. Specifications” and is designed for usage as raw material for thermocatalytic processes, petroleum oil production processes or as boiler fuel component.

No.	Property	Hydrocracked  residue
1	Distillation: а) 10 % distilled at, ˚С, max b) 50 % distilled at, ˚С, max c) 90 % distilled at, ˚С, max d) 95 % distilled at, ˚С, max	400 440 510 530
2	Density at 15 ˚С, kg/m3 max	915
3	Sulfur content,%, max	0.1
4	Open cup flash point, ˚С, min	170
5	Flow point, ˚С, min	20
6	Coking capacity,% wt., max	0.2

WIDE LIGHT HYDROCARBON FRACTION is produced in accordance with TU 38.101524–93 “Wide light hydrocarbon fraction. Specifications” and is used as feedstock for gas fractionating units (fractionator and central fractionator) for individual hydrocarbons production.

No.	Property	TU38.101524–93
		A grade	B grade
1	Components,%  wt. — sum of С1‑С2 hydrocarbons, max — propane, min — sum of С4‑С5 hydrocarbons, min — sum of С6 hydrocarbons and above, max	3 15 45 15	5 ‑ 40 30
2	Methanol,% wt.	not rated
3	Hydrogen sulfide and mercaptan sulfur,% wt., max including: hydrogen sulfide, max	0.025 0.003	0.05 0.003
4	Free water and alkali content	None
5	Appearance	Colorless transparent liquid

COMMERCIAL SULFURIC ACID, grade 1 is produced in accordance with GOST 2184–77 “Sulfuric acid for industrial use. Specifications” and is designed for production of fertilizers, artificial fiber, caprolactam, titanium dioxide, ethyl alcohol, aniline colorants and a range of other production units.

No.	Property	Commercial sulfuric acid, 1st grade
1	Monohydrate (Н2SO4),% wt.	min 92.5*
2	Iron (Fe),% wt., max	0.02
3	Ignition residue,% wt., max	0.05
4	Nitrogen oxides (N2O3),% wt., max	Not rated
5	Nitro compounds,% wt., max	Not rated
6	Transparency	Not rated
7	Color, cm3 of reference solution, max	6

*From November 1st till April 15th manufacturing plants should supply commercial contact sulfuric acid with monohydrate mass fraction 94.0 %.

COMMERCIAL CONTACT SULFURIC ACID, grade K, is produced in accordance with TU BY 300220696.043–2007 “Commercial contact sulfuric acid, grade K” and is designed for production of mineral fertilizers, artificial fiber, caprolactam, various salts, aniline colorants and a range of other production units.

No.	Property	Comercial contact sulfuric acid, grade K
1	Monohydrate (Н2SO4),% wt.	92.5–98.0*
2	Iron (Fe),% wt., max	0.006
3	Chrome content (Cr), mg/kg, max	0.7
4	Molybdenum content (Mo), mg/kg, max	0.1
5	Sulfur dioxide content (SO2), mg/kg, max	20
6	Elemental sulfur content (S), mg/kg, max	0.15
7	Organic substances content, reference units of optical density, max	0.08
8	Ignited residue,% wt., max	0.02
9	Nitrogen oxides (N2O3),% wt., max	0.02
10	Transparency	Transparent without dilution
11	Color, cm3 of reference solution, max	1

*Seasonal restriction: from November 1st till April 15th acid is supplied with monohydrate (Н SO ) mass fraction max 94.0 %.

PETROLEUM EXTRACT is produced in accordance with TU RB 05778477–25–93 and is designed for usage in melting roofing felt production, as carbon-contained additive to molding compounds in foundry production, and as dipping compound for impregnated gland packings.

No.	Property	Petroleum extract
1	Density at 20 °C, kg/m3	960–990
2	Kinematic viscosity, at 100 °C, mm2/s (cSt)	10–25
3	Refraction index at 50 °C, min	1.5300
4	Open cup flash point, °C, min	210
5	Phenol,% wt., max	0.01
6	Water,% wt.	Traces

PLASTICIZER OIL / (PN-6 OIL) is produced in accordance with TU 38.1011217–89 and is designed for usage as plasticizer and extender of synthetic divinyl (methyl)-styrene rubber and as rubber mixes softener.

No.	Property	PN‑6k	PN‑6sh
1	Kinematic viscosity at 100 °C, mm2/s	30–35	32–40
2	Refraction index at 50 °C, min	1.520	1.525
3	Aniline point, °C, min	67	65
4	Phenol,% wt., max	0.01	0.01
5	Sediments  content	None
6	Water content	Traces
7	Open cup flash point, °C, min	230	230
8	Pour point, °C, max	36	36
9	Density at 20 °C, g/cm3, min	0.950	0.960
10	Hydrocarbon type content: а) Paraffinic‑haphtenic hydrocarbons,% wt., max б) Gums,% wt., max	14 8	14 8

PETROLATUM is produced in accordance with TU 38.401166–90 and is designed for ceresin production. It is also a component of lubricants, vaselines and sealing compounds:

No.	Property	PS‑55	PS‑60	PS‑65
1	Color	Light brown
2	Drop point, °C	55–60	60–65	65–70
3	Metals corrosion test	Passes
4	Acid number, mg КОН / 1 g of petrolatum, max	0.05
5	Water soluble acids and alkalis content	None
6	Mechanical impurities,% wt., max	0.03
7	Water,% wt., max	traces
8	Sulfur content,%, max	0.6
9	Phenol and cresol content, mg/dm3, max	None
10	Open cup flash point, °C, min	240
11	Penetration, 0.1 mm, max	70

PETROLEUM SLOP WAX is produced in accordance with TU RB 300220696.009–2002 and is designed for usage as raw material for solid paraffins production and other petroleum refining and petrochemistry processes.

No.	Property	Grade 1	Grade 2	Grade 3	Grade 4
1	Appearance	Crystalline mass from white to light brown or dark grey color
2	Oil,% wt., max	50	5.1–10.0	10.1–15.0	15.1–20.0
3	Melting point, °C, min	49
4	Sulfur content,%, max	0.5
5	Closed cup flash point, °C, min	180
6	Water,% wt., max	traces
7	Mechanical impurities,% wt., max	0.1

COMMERCIAL DEASPHALTED OIL is produced in accordance with TU BY 300220696.044–2008 and is designed for usage as catalytic cracking feedstock component and as furnace fuel oil component.

No.	Property	Commercial deasphalted oil
1	Kinematic viscosity at 100 °C, mm2/s)	17–35
2	Density at 20 °C, kg/m3	Not rated, definition is mandatory
3	Sulfur content,%, max	2.2
4	Open cup flash point, °C, min	220
5	Pour point, °C, max	65
6	Coking capacity,%, max	1.5
7	Color: on colorimeter, CNT units, max as per ASTM scale, max	8.0 8.0
8	Ash content,%, max	0.01
9	Water content,%, max	Traces

PETROLEUM VACUUM DISTILLATES, grades VD-1, VD-2, VD-3 and VD-4, are produced in accordance with TU BY 300220696.037–2006 and are designed for usage as feedstock for plastic lubricants and conservation compounds production:

No.	Property	VD‑1	VD‑2	VD‑3	VD‑4
1	Kinematic viscosity at 100 °C, mm2/s, min	3.5	5.5	10.0	17.0
2	Color on colorimeter, CNT units, max	2.5	3.5	4.5	6.5
3	Open cup flash point, °C, min	185	205	230	250
4	Coking capacity,%, max	0.10	0.15	0.30	1.30
5	Water,% wt., max	0.03
6	Density at 15 °C, kg/m3, max	Not rated, definition is mandatory
7	Sulfur content,%, max	Not rated, definition is mandatory

Note: It is allowed to produce and supply distillates with quality parameters differerent from specified in the table and in supply contract by agreement with the consumer or under contract terms.