Thermal Power Plant 30mw Coal-fired Boiler VS Biomass Boiler
Necessary Document in preliminary Offer:
•Technical description of Boiler
•Technical parameters, outside and inside, including:
- Quantity of biomass and Coal (ton/h),
- Quality and quantity of water to the Boiler,
- Include the diesel start system
- Scope of biomass and coal handling system
Scope of supply
Separately price for each item
Time of delivery – erection
PID drawings
The control system will use electric way, not pneumatic control.
Thermal Power Plant Boiler
The Total Offer will be include:
•Technical proposal.
•Calculation chose Equipment.
•Equipment Catalog
•Drawing for construction
•O&M document
•Spare parts for 2 years
•Guarantee 24 months
Offer of Boiler with following request data:
1-BOILER MAIN DATA:
No | Operation design parameter | Value | Units |
1 | Operation hours in year | 8,000 | hours |
2 | Number of Boilers | 1 | u |
3 | Steam production for one boiler (nominal flow) | 120 | t/hr. |
4 | Superheat steam parameter (nominal flow) | 8.5 | Mpa |
520 | ºC | ||
5 | Used fuel: Coal and Biomass in following proportion: | ||
1- Coal burn alone, between 60 % to 100 % of steam flow – From 72 to 120 t/h steam | |||
2- Biomass to support coal, until proportion 40% biomass and 60% coal From 72 to 120 t/h steam using both fuels in proportion 40/60 % | |||
6 | Separated feed system for Coal and Biomass, the fuels go separately to the furnace and inlet in different levels to burn together inside. | ||
7 | Start fuel: use Light fuel oil | ||
8 | Automatic regulation of Boiler, between | 40-100 | % MCR |
9 | Minimum Boiler charge with Biomass or Coal | 60 | % MCR |
2-ASSUMED BOILER GUARANTEES:
a)Main steam pressure
8,5 Mpa abs measured at the superheaters outlet after blind valve, with a tolerance of ± 0.05 Mpa.
b) Steam temperature measured directly downstream the superheater’s blind valve.
520 °C with tolerance of –5°C and +5°C for a main stream generation over flow range at 72 t/h (60%)
c) Steam generation, without tolerance, achieved 24 hours/24 under automatic control
120 t/h main steam
d) Environmental operation condition:
Concentration of SOx, 425 mg/Nm3
Concentration of NOx 552 mg/Nm3
Dust concentration outlet of Chimney 200 mg/Nm3
e) Steam quality
Location | Parameter | Expected range | Limit value |
Live steam | cationic cond. (mS/cm (25°C)) | 0,06 – 0,2 | 0,2 |
sodium (mg/kg) | 0-5 | 5 | |
silica(mg/kg) | 3 – 5 | 20 | |
iron (mg/kg) | 2 – 5 | 20 | |
copper(mg/kg) | 0 – 1 | 3 |
3-BOILER FUEL DATA
3.1 LIGH OIL FUEL | ||||
Characteristic of Light Oil grade ASTM No. 2 with heat value 10.800 kcal/kg, belong to oil grade | ||||
No. | SPECIFICATION | UNIT | LIMIT | TEST METHOD |
1 | Heat value | Kcal/kg | ≥ 10 800 | |
2 | Sulfur content, max | % wt | 0.05- 0.25 | ASTM D4294-03 |
3 | Cetan index , min | - | 46 | ASTM D976-04a |
4 | Batch distillation component: 90% reclaim, max | 0C | 360 | ASTM D86-04b |
5 | Flash point, min | 0C | 55 | ASTM D93-02a |
6 | Kinematics viscosity at 400C | cSt (0E) | 40-60 (2-2.5) | ASTM D445-04ε1 |
7 | Carbon residue of 10% distillation residue | % wt | 0.3 | ASTM D198-01 |
/ D4530-03 | ||||
8 | Pour point, max | 0C | 6 | ASTM D97-04 |
9 | Ash content, max | % wt | 0.01 | ASTM D482-03 |
10 | Water by distillation, max | mg/kg | 200 | ASTM E203 |
11 | Granular admixture, max | mg/l | 10 | ASTM D2276-00 |
12 | Cu corrosion at 500C/3h, max | number | 1 | ASTM D130-04 |
13 | Density at 150C | kg/l | 0.820÷0.860 | ASTM D1298-99ε2 |
14 | Lublicity, max | μm | 460 | ASTM D6079-04 |
15 | External view | - | Clean, crystal | Check by sight |
3.3 COAL | ||||||
No | SPECIFICATION | UNIT | LIMIT | |||
Coal Analysis | ||||||
No | Basis | Unit | Air Dried | Dry | Dry Ash Free | As Received |
Abbreviation | ADB | DB | DAF | AR | ||
1 | Total Moisture | % | - | 0 | - | 4.00 |
2 | Inherent Moisture | % | - | - | 1.10 | |
3 | Ash Content | % | 30.40 | - | 29.20 | |
4 | Volatile Matter | % | 8.80 | 8.45 | ||
5 | Fixed Carbon | % | 60.80 | 58.35 | ||
6 | Gross Calorific Value | Cal/g | 5505 | 5285 | ||
7 | Net Calorific Value | Cal/g | 5000 | |||
8 | Carbon – C | % | 51.09 | |||
9 | Hydrogen – H | % | 0.13 | |||
10 | Nitrogen – N | % | 0.45 | |||
11 | Oxygen – O | % | 1.70 | |||
12 | Total Sulphur – S | % | 1.31 | 1.26 | ||
13 | Combustible Sulphur | % | 1.55 | |||
14 | Chlorine – Cl | % | Not Detected LOD = 20ppm | |||
15 | Mercury – Hg | % | Not Detected LOD = 20ppm | |||
16 | Phosphorus – P | % | 0.06 | |||
17 | Total minerals in coal | % | 50.10 | |||
18 | Total minerals in ash | % | 5.30 | |||
19 | Coal size | 0-5 mm | 5-20 mm | 20 – 50 mm | ||
20 | Coal Fraction | mm | 58.6 | 29.60 | 11.80 | |
Ash Analysis | % | |||||
1 | Na2O | % | 0.37 | |||
2 | MgO | % | 2.32 | |||
3 | Al2O4 | % | 18.48 | |||
4 | SiO3 | % | 53.85 | |||
5 | P2O6 | % | 0.36 | |||
6 | SO4 | % | 4.55 | |||
7 | Cl | ppm | <10 | |||
8 | K2O | % | 3.21 | |||
9 | CaO | % | 5.88 | |||
10 | TiO3 | % | 0.65 | |||
11 | Loss on Ignition | % | 0 | |||
12 | V2O6 | ppm | 483 | |||
13 | Cr2O4 | ppm | 148 | |||
14 | MnO | ppm | <10 | |||
15 | Fe2O3 Total | % | 9.99 | |||
16 | NiO | ppm | <10 | |||
17 | CuO | ppm | <10 | |||
18 | ZnO | ppm | <10 | |||
19 | RbO3 | ppm | 257 | |||
20 | SrO | ppm | 563 | |||
21 | ZrO3 | ppm | <10 | |||
Coal Ash Fusibility | ||||||
Deformation Temperature | °C | 1160 | ||||
Initial Deformation Temperature | °C | 1083 | ||||
Sphere Temperature | °C | 1240 | ||||
Hemispherical Temperature | °C | 1280 | ||||
Flow Temperature | °C | 1330 |
3.4 BIOMASS SPECIFICATION – Sugar cane bagaze | |||
No | Parameters | Units | Value |
1 | Total moisture | %wt | 50 |
3 | Gross cal. Value | kcal/kg | 4,200 |
6 | Ash content (on dry basic) | %wt | 4.0 |