ABCDEFGHIJKLMNOPQRSTUVWXYZAAABACADAEAFAGAHAIAJAKALAMANAOAPAQARASATAUAVAWAXAYAZBABBBCBDBEBFBGBHBIBJBKBLBMBNBOBPBQBRBSBTBUBVBWBXBY
1
2
GANTT CHART: Receiving the best deals from partners!Expert advice ➜Projects for Partners for easy contract selection.
Partners see all phases of dials and always have the option to click BUY NOW or SELL.
3
4
PROJECT TITLE MORE DIALS IN PROCESS (LGC) (JET) (OIL)COMPANY NAMETrefina Verwaltungs AG
5
PROJECT HEAD of COMPLIANCE Vadim PavlovDATE15.02.22
6
Quantity: 3 000 000 bbl +/- 5%. per month.
Platts NWE ULSD Diesel Oil EN590.
2*Quantity: 150 000 metric t. +/- 5%.
Platts NWE Basis ARA Jet cod PJAAVOO
Quantity: up 5 000 000 bbl +/- 5%. per m.
S&P Platts' Crude Oil Marketwire Brent (Dated) Code PCAAS00
Quantity: 2 000 000 bbl +/- 5%. per month.
7
1. Platts Dubai Price LGC: BID $ -7 per b/ASK $ -6 per b/Agency Fee $ 1.75 per b.
2. BID US $ -25 per mt / ASK US $ -25 per mt Agency Fee US $ 6 per mt
3. BID $ -4 per b/ASK $ -4 per b/Agency Fee $ 1.00 per bbl.
4. BID $ -6.5 per b/ASK $ -6.5 per b/Agency Fee $ 1.00 per bbl.
8
No.TITLE TASKSCURATORSTART DATECLOSING DATEDURATIONPERCENT COMPLETESTEP 1STEP 2STEP 3STEP 4
9
WEEK 1WEEK 2WEEK 3WEEK 4WEEK 5WEEK 6WEEK 7WEEK 8WEEK 9WEEK 10WEEK 11WEEK 12
10
MOTUWETHFRMOTUWETHFRMOTUWETHFRMOTUWETHFRMOTUWETHFRMOTUWETHFRMOTUWETHFRMOTUWETHFRMOTUWETHFRMOTUWETHFRMOTUWETHFRMOTUWETHFR
11
1Light Gas Condensate (LGC)
12
1.1Project presented Dmitrii K.16.02.2209.03.23383100%
13
1.1.1Project accepted from SellerDmitrii K.20.02.2222.03.2339230%
14
1.2Project accepted for reviewZhanna K.17.02.2222.03.2339590%
15
1.3Project researchZhanna K.18.02.2215.03.2338740%
16
1.4Project accepted from BuyerZhanna K.22.02.2222.03.2339030%
17
1.5Acceptad all procedures & Sign. Vadim P.01.03.2222.03.2338120%
18
1.6Getting StartedAlexey S.23.03.2231.12.236380%
19
2Diesel Oil EN590
20
2.1Project presented Dmitrii K.11.02.2209.03.23388100%
21
2.2Project accepted from SellerDmitrii K.18.02.2222.03.2339430%
22
2.3Project accepted for reviewDmitrii K.11.02.2222.03.23401100%
23
2.4Project researchDmitrii K.20.02.2215.03.23385100%
24
2.5Project accepted from BuyerDmitrii K.21.02.2222.03.23391100%
25
2.6Acceptad all procedures & Sign. Vadim P.22.02.2222.03.2339030%
26
2.7Getting StartedAlexey S.23.03.2231.12.236380%
27
3JET A1 Aviation kerosene
28
3.1Project presented Dmitrii K.23.11.2118.12.22385100%
29
3.2Project accepted from SellerDmitrii K.26.11.2126.12.22390100%
30
3.3Project accepted for reviewDmitrii K.23.11.2118.12.22385100%
31
3.4Project researchDmitrii K.28.11.2113.12.22375100%
32
3.5Project accepted from BuyerDmitrii K.26.11.2126.12.22390100%
33
3.6Acceptad all procedures & Sign. Vadim P.23.12.2110.01.2217100%
34
3.7Getting StartedAlexey S.11.01.2231.12.237100%
35
4HBCO Heavy bituminous crude oil
36
4.1Project presented Dmitrii K.25.01.2209.03.2340470%
37
4.2Project accepted from SellerDmitrii K.28.01.2222.03.2341470%
38
4.3Project accepted for reviewZhanna K.24.01.2222.03.2341870%
39
4.4Project researchZhanna K.16.02.2215.03.2338960%
40
4.5Project accepted from BuyerZhanna K.16.02.2222.03.2339630%
41
4.6Acceptad all procedures & Sign. Vadim P.24.02.2222.03.2338810%
42
4.7Getting StartedAlexey S.23.03.2231.12.236380%
43
44
45
 GENERAL TECHNICAL SPECIFICATION
LIGHT GAS CONDENSATE
ORIGIN RUSSIA - JET A1
HEAVY BITOMINOUS CRUDE OIL mixture
46
47
ParametersUnitsResultTest Method
COMPOSITION
Parameter Min: Max:
48
Specific Gravity at 15.56 /15.56 °C---0.7327ASTM D4052
Appearance C&B (1)
API Gravity: 15.5oAPI 16.5oAPI
49
API GravityoAPI61ASTM D4052
Acidity, Total (mg KOH/100 cm3) Max. 0.10 D3242
Sulfur Content (Total) NA 2.65%
50
Sulfur Content (Total) maxwt.%0.25ASTM D4294
0.015 (2) IP354
Water and Sediment NA 1.0%
51
H2S Contentppm<1UOP 163
Aromatics Mt %) Max. 25 D1319
Asphaltene Content 7,0% NA
52
Mercaptan Contentwt.%0.17UOP 163
Sulphur Total wt Max 0.25 D1266-D1552-D2622-D4294-G-R5194
Wax as per PetroChina condition NA ≯3.0
53
Nitrogen Content (Total)ppm<10ASTM D4629
Sulphur, Mercaptan (wt %) Max. 0.003 D3227
Hydrogen Sulfide (Liquid Phase) as per PetroChina condition NA ≯20 ppm
54
Water Contentwt.%<0.025ASTM D4006
or Doctor Test Negative D4952
Organic Chloride NA ≯3.0 ppm
55
Salt ContentP.T.B.<1ASTM D3230
VALATILITY
56
PONA test:ASTM D1319
Distillation Temperature: D86
* Shall the water and sediment content be reported in excess of the maximum
57
Saturate contentvol.%89.5
10% Recovery (°C) Max. 205
allowance the final invoice price will be subject to the ratable reduction.
58
Olefin contentvol.%2
50% Recovery (°C) Report
Other parameters may deviate +/- 10% from the properties given in the general technical specification with respect.
59
Aromatic contentvol.%8.5
90% Recovery (°C) Report
60
Kinematic Viscosity at 0 °Cmm2/s1.061ASTM D445
Final BP (°C) Max. 300
61
Kinematic Viscosity at 10 °Cmm2/s0.862ASTM D445
Distillation Residue (vol %) Max. 1.5
62
Kinematic Viscosity at 20 °Cmm2/s0.777ASTM D445
Distillation Loss (vol %) Max. 1.5
63
Cloud Point°C-44ASTM D2500
Flash Point (°C) Min. 38 D56-D3828
64
Pour Point (Upper)°C-57ASTM D97
Density @ 20°C (kg/m3) 775-840 D1298-D4052-GOST R 51069
65
Reid Vapor PressurePSI11ASTM D5191
FLUIDITY
66
Wax Contentwt.%0.4BP 237
Freezing Point (°C) Max. -47 (3) D2386-D5972
67
Copper Corrosion, 3 hrs at 50 °C1aASTM D130
Viscosity @ -20°C (cSt) Max. 8 D445
68
Acidity Totalmg KOH/g<0.05ASTM D664
COMBUSTION
69
Aniline Point°C60IP 2
Net Heat of Comb. (MJ/kg) Min. 42.8 (4) D3338-D4529-D4809
70
Molecular Weightg/mol112.6Osmomat
Smoke Point (mm) Min. 25 D1322
71
Bromine Indexmg Br2/100 g807IP 130
or Smoke Point (mm) Min. 19 D1322
72
Lead Contentmg/kg< 1ASTM D5863
and Naphthalene’s (wt%) Max. 3 D1840
73
CORROSION
74
Copper Strip (2h @ 100°C) Max. No.1 D130
75
THERMAL STABILITY
76
JFTOT AP @ 260 °C (mm Hg) Max. 25 D3241
77
Tube Rating (Visual) Max. <3(5)
78
CONTAMINANTS
79
Existent Gum (mg/100 cm3) Max. 7 D381
80
Water Reaction Interface Max. 1b D1094
81
MSEP Rating D3948
82
Fuel without SDA Min. 85
83
Fuel with SDA Min. 70
84
OTHERS
85
Conductivity (pS/m) 50-450 D2624-GOST 25950
86
Without SDA Max. 10
87
Lubricity (wear scar) (mm) Max. 0.85 (6) D5001
88
ADDITIVES
89
Antioxidant (ppm) Max. 24
90
Static Dissipator (ppm) Max. 3(7)
91