gyf-208
New
Automatic
Engineers Available to Service Machinery Overseas
Gasoline/Diesel
1000, 000tons/Year
Available
12 Months -15 Months
GYF
Standard Packing
Subject to product specification
China
Product Description
Table 1-1 Raw material specifications
| Name of raw material | Item | Unit | Index |
| Raw oil | Water bearing | % | ≯2.0 |
| Stripped crude | saltiness | Mg/g | ≯3 |
| Water bearing | % | ≯0.3 |
| Gasoline quality index: | |||
| Steam top gasoline dry point | ≯170ºC | ||
| Always top gasoline dry point | ≯170ºC | ||
| Regular first-line quality indicators: | |||
| 98% point | ≯260ºC | ||
| Flash point | >38 | ||
| Diesel quality index: | |||
| 95% point | ≯365ºC | ||
| 0# Diesel oil | Freezing point | 0±4ºC | |
| -10# Diesel oil | Freezing point | -10±4ºC | |
| -20# Diesel oil | Freezing point | -20±4ºC | |
| Note: Freezing point and 95% point control one of them | |||
| Mixed wax oil index: | |||
| Carbon residue | ≯0.3 | ||
| Name | Requirement index | |
| Circulating water temperature | ≤30ºC | |
| Circulating water pressure | ≥0.4MPa | |
| System steam pressure | 0.8~1.0 MPa | |
| Instrument air pressure | ≥0.3MPa | |
| Fuel oil pressure | ≥1.0MPa | |
| High gas pressure | 0.2~0.5 MPa | |
| Sealing pressure | ≥2.0MPa | |
| Circulating cooling water: | ||
| Water supply temperature | ≤30ºC | |
| Return water temperature | ≤40ºC | |
| Water supply pressure | 0.35MPa | |
| Backwater pressure | 0.20Mpa | |
| PH value | 6~9 | |
| turbidity | ≤2000mg/l | |
| Fouling coefficient | ≤0.0004m2·h·ºC/kcal | |
| Power: | ||
| High voltage | 6000V±10% | |
| frequency | 50±1Hz | |
| Low voltage | 380V/220V±5% | |
| frequency | 50±1Hz | |
| Instrument compressed air: | ||
| 0.4MPaG dew point | -20ºC | |
| temperature | Normal temperature | |
| stress | 0.4MPa | |
| NO. | Raw material name | Unit | QTY | Remark |
| 1 | Fuel oil + fuel gas | kg/h | 4605.75 | |
| 2 | Electricity | KWh/h | 3673.8 | |
| 3 | Circulating water | t/h | 1737 | |
| 4 | Fresh water | t/h | 7.163 | |
| 5 | Softened water | t/h | 19.902 | |
| 6 | Sewage | t/h | 10.38 | |
| 7 | 0.9Mpa steam | t/h | 7.609 | |
| 8 | 0.3Mpa steam | t/h | 5.89 |
| NO. | Process NO. | Device name | Specification and model | Structural form | Volume m3 | Operating pressure Mpa | Operating temperature ºC |
| 1 | T-701 | Primary still | ф3000*54154 | Strip float valve | 375 | 0.08 | 300 |
| 2 | T-702 | Atmospheric tower | ф3800*47758*16/18 | Strip float valve | 530 | 0.08 | 350 |
| 3 | T-203 | Decompression tower | ф6400/4200*35145 | filler | 908.2 | -0.093 | 440 |
| 4 | T-703 | Regular line stripper tower | ф1200*7502*10 | Float valve | 8 | 0.08 | 350 |
| 5 | T-704 | Normal two wire stripper tower | ф1200*6550*10 | Float valve | 8 | 0.08 | 250 |
| 6 | T-705 | Normal three wire stripper | ф1200*6000*12 | Float valve | 8 | 0.08 | 350 |
| 7 | T-101A | Dehydration tower | ф1200*6800*16 | Filler | 8.3 | 1.7 | Normal temperature |
| NO. | Process number | Device name Crude oil/regular line | Specification and model | Shell pass medium | medium Crude oil | stress Mpa | Stress Mpa |
| 1 | H-701A | Crude oil/normal top cycle | BES1000-4.0-265-6/25-4 | 16MnR | Crude oil | 2.3 | 1.5 |
| 2 | H-702A | Crude oil/normal third line | FB900-220-25-2 | 16MnR | Heavy firewood | 2.5 | 1.5 |
| 3 | H-703A | Crude oil/residual oil | FB700-125-25-2 | 16MnR | residuum | 1.8 | 2.3 |
| 4 | H-704A | Crude oil/Chang Yizhong | FB700-125-25-2 | 16MnR | Crude oil | 1.8 | 2.3 |
| 5 | H-705A | Crude oil/normal third line | FB700-125-40-4 | 16MnR | Heavy firewood | 2.3 | 2 |
| 6 | H-706A | Crude oil/Regular 2 middle | FB700-125-25-2 | 16MnR | Crude oil | 2 | 2 |
| 7 | H-709A | Head oil/Chang Erzhong | BES800-4.0-160-6/25-4 | 16MnR | Hair oil | 1.8 | 2 |
| 8 | H-712A | Crude oil/minus three lines | BES700-4.0-120-6/25-4 | 16MnR | Wax oil | 2.5 | 2 |
| 9 | H-714A | Crude oil/normal second line | BES1100-40-365-6/25-2 | 16MnR | medium | 2.3 | 2 |
| 10 | H-718A | Device name | FB700-120-25-4 | 16MnR | 2 | 1.8 | |
| 11 | H-719A | Crude oil/minus three lines | FB1100-330-25-4 | 16MnR | Crude oil | 2 | 2 |
| 12 | H-721A | Pulling oil/reducing three lines | RBEU900-4.0-205-6/25-4 | 18-8 | Wax oil | 2 | 2.5 |
| 13 | H-727A | Minus four wire evaporator | FB1000-265-40-4 | 16MnR | Softened water | 2 | 0.9 |
| 14 | H-728A | Normal three wire cooler | FB700-125-25-4 | 16MnR | Heavy firewood | 1.5 | 0.5 |
| 15 | H-730A | Primary side cooler | FB700-120-25-4 | 16MnR | gasoline | 0.4 | 0.5 |
| 16 | H-731A | Minus one cooler | FB800-160-25-4 | 16MnR | Wax oil | 1.8 | 0.5 |
| 17 | H-732A | Often a line cooler | FB600-90-40-4 | 16MnR | Aviation fuel | 1.5 | 0.5 |
| 18 | H-733A | Normally two-wire cooler | FB700-120-25-4 | 16MnR | Diesel oil | 1.5 | 0.5 |
| 19 | H-735C | Reduced line cooler | FB700-125-25-2 | 16MnR | Wax oil | 1.8 | 1 |
| 20 | H-736ABC DEFGH | Initial head air cooling | P9×3-4-3020/129-16Ra | 16MnR | Initial top oil vapor | 0.4 | |
| 21 | H-737A | Cold after the first roof | FB1100-330-16-4 | 16MnR | gasoline | 0.4 | 0.4 |
| 22 | H-739 | Often head air cold | P9×3-4-3020/129-16Ra | Constant oil vapor | 0.4 | ||
| 23 | H-739 | Often head air cold | P9×3-6-196-16S-23.4/Ra | Constant oil vapor | 0.4 | ||
| 24 | H-739 | Often head air cold | P9×3-4-3020/128-16Ra | Constant oil vapor | 0.4 | ||
| 25 | H-740A | Often cold after top | FLB1100-360-16-4 | 16MnR | gasoline | 0.4 | 0.4 |
| 26 | H-740B | Often cold after top | FLB1100-360-16-4 | 16MnR | gasoline | 0.4 | 0.4 |
| 27 | H-741 | Often three air cold | SL9×3-4-2440/129-25Rb | 1.5 | |||
| 28 | H-743 | Reduced first line/crude oil | BES900-4.0-265-6/25-4 | 16MnR | Crude oil | ||
| 29 | H-230A | Reduced top cooler | FLB1100-350-16-4 | 16MnR | Diesel oil | 0 | 0.4 |
| 30 | H-231A | Reduced top primary cooler | FLB1100-350-16-4 | 16MnR | Diesel oil | 0 | 0.4 |
| 31 | H-232A | Reduced top two stage cooler | FLB1100-350-16-4 | 16MnR | Diesel oil | 0 | 0.4 |
Table 1-7 Pumps
| Device name Crude oil pump | specification | Head m | Inlet pressure MPa | Outlet pressure MPa | medium Crude oil | TemperatureºC | Flow rate m3/h | Speed r/m | Shaft power KW |
| Priming pump | 250Y-150×2A | 262 | 0.2 | 2.1 | Hair oil | 50 | 472 | 2950 | 488 |
| Normal bottom pump | 250AYS150×2A | 260 | 0.06 | 1.8 | Normal slag | 160 | 480 | 2985 | 430 |
| Primary top pump | 250YS150×2C | 190 | 1.45 | gasoline | 350 | 400 | 2950 | 269 | |
| Slag pump | 100Y-120 | 123 | 0.08 | 1 | residuum | 30 | 100 | 2950 | 54.1 |
| Normal top pump | 65Y-100×2C | 125 | gasoline | 20 | 2950 | 20 | |||
| Normal top circulating pump | 80Y100B | 73 | 0.05 | 0.6 | gasoline | 30 | 40 | 2950 | 15.3 |
| Chang Yi Zhong pump | 150Y-150 | 150 | 0.2 | 0.64 | Light diesel oil | 90 | 180 | 2950 | 113 |
| Often two pumps | 150Y-150B | 110 | Light diesel oil | 155 | 2950 | 76 | |||
| Normal line pump | 150Y-150B | 110 | Aviation fuel | 155 | 2950 | 76 | |||
| Normally two-wire pump | 100Y120×2C | 150 | 0.15 | 1.39 | Diesel oil | 150 | 79 | 2950 | 55.5 |
| Device name | 100Y120×2C | 150 | 0.11 | 1.1 | medium | 250 | 79 | 2950 | 55.5 |
| Normal three-wire pump | 100AY120×2C | 150 | 0.06 | 0.65 | Heavy diesel oil | 330 | 79 | 2950 | 55.7 |
| Jacking oil pump | 50Y-60×2A | 105 | 0.11 | 0.95 | Coping oil | 20 | 12.5 | 2950 | 9.82 |
| Reducing line pump | 100Y120×2C | 105 | 0.21 | 1.65 | Wax oil | 80 | 79 | 2950 | 55.5 |
| Reducer pump | 200AY150 | 150 | Wax oil | 270 | 300 | 2950 | / | ||
| Reducing three wire pump | 250AYS150 | 150 | Wax oil | 320 | 500 | 2985 | 259 | ||
| Minus four wire pump | 80Y100×2A | 175 | 0.06 | 1.2 | Wax oil | 370 | 47 | 2950 | 44.8 |
| Reducing slag oil pump | 200×150R2DM | 300 | residuum | 370 | 300 | 2980 | 245 | ||
| Anti-viscosity slag oil pump | 200×150R2DM | 300 | residuum | 370 | 300 | 2950 | 245 | ||
| Viscosity reducing condensate pump | 50AY-35×5 | 190 | 1 | 4 | Condensed oil | 40 | 12.5 | 2950 | 15 |
| Constant furnace blower | G4-73-11No1190 | 0.35 | air | Normal temperature | 60100 | 1450 | |||
| Normal furnace induced draft fan | Y4-73-11No1290 | 0.16 | smoke | 120 | 89500 | 1450 | |||
| Reduced furnace induced draft fan | Y4-73-11No14135 | 0.163 | smoke | 120 | 89500 | 960 |
List of project construction and investment
| Order NO. | Device name |
| Phase I construction content | |
| 1 | 1750000 tons / year atmospheric and decompression device |
| Phase II construction content | |
| 4 | 1750000 tons / year atmospheric and decompression device |
| 5 | 250,000 tons / year (~ 150,000 tons / year) hydrorefining unit (hydrogenation pressure 16 Mpa) |
| 6 | 3000 Nm ³ / h methanol hydrogen production plant (local green methanol) |
| 7 | Heavy-oil deep-processing unit |
| Storage and transportation and auxiliary public works | |
| 8 | Tank area (80,000 cubic meters) and loading and unloading vehicle facilities, wharf tank area 50,000 cubic meters, a total of 130,000 reserves |
| 9 | Supporting sewage treatment system, fire control system, heating system, flare system, air suppression nitrogen and other systems |































