For Design, Supply, Installation and Commissioning of 25 T/H Steam Boilers
1. |
Fuel |
|
1.1. |
Fuel for equipment selection |
Natural gas |
1.2. |
Fuel lower heating value, mJ/m3 (ckal/m3), at 20°С 101,325 kPa. Min.
|
31.8 (7600) |
1.3. |
Wobbe number range of values (upper). mJ/.m3 (ckal/m3)
|
41,2-54.5 (9850-13000) |
1.4. |
Permissible tolerance of Wobbe number from a rated value, %, max
|
±5 |
1.5. |
Hydrogen sulphide mass concentration, g/mЗ, max.
|
0,02 |
1.6. |
Mercaptan sulphur mass concentration, g/mЗ, max. |
0.036 |
1.7. |
Oxygen volume ratio, %, max
|
1.0 |
1.8. |
Mass of mechanical impurities in 1 m3, g, max
|
0.001 |
1.9. |
Natural gas composition: hydrogen content, % vol. |
0
|
|
Carbon monoxide content %, vol.
Carbon dioxide content Methane content , %, vol Ethane content, %, vol . Ethylene content, %, vol Propane content, %, vol Propylene content, %, vol iC4 content % vol. nС4 content, %, vol Isobutylene content %, vol. t- buten -2 content, %, vol. С- buten-2 content, %, vol. 1,3 – butadiene content, %, vol. Buten-1 content-1, %, vol. iC5 content, % vol. nС5 content, % vol. Amount of С5 and С6, %, vol.
|
0
0 96.8-99.3 0.5-2.2 0 0,1-0,7 0 0-0,1 0-0,1 0 0 0 0 0 0 0 0
|
2. |
Feed water (chemically demineralized water from TPP) |
|
2.1. |
Temperature of feed water at the inlet of a boiler unit, °С
|
100±5 |
2.2. |
Composition of feed water for boilers |
|
2.2.1. |
Ferrum, μ/dm3 |
≤20.0 |
2.2.2. |
Oil products, mg/dm3 |
≤0,3 |
2.2.3. |
Dissolved oxygen, μ/dm3 |
≤30,0 |
2.2.4. |
Hardness, uEg/dm3 |
≤1,0 |
2.2.5. |
Silicic acid, μ/dm3 |
≤20 |
2.2.6. |
Transparency, cm |
≥40 |
2.2.7. |
pH at 25°С |
9,1-9,5 |
2.2.8. |
Sodium compounds, μ/dm3 |
≤80 |
2.2.9. |
Specific electrical conductivity, mmhos/cm |
2 |
2.2.10. |
Dissolved solids concentration |
≤10 |
2.3. |
Feed water pressure, MPa |
1±0,2 |
2.4. |
Boiler steam specification |
|
2.4.1. |
pH at 25°С |
6.0-9.0 |
2.4.2. |
Relative dissolved solids concentration (expressed as NCl), μ/kg |
200 |
2.4.3. |
Free ammonia content |
Not allowed |
2.4.4. |
Sodium content, μ/l |
≤60 |
2.4.5. |
Silicic acid concentration expressed as SiO2, μ/kg |
≤50 |
2.4.6. |
Electric conductivity, mmhos /cm |
≤1 |
2.4.7. |
Ferrum content, μ/kg |
≤50 |
2.4.8. |
Cuprum content, μ/kg |
≤10 |
3. |
Steam boiler |
|
3.1. |
Application |
Steam output with 3.9 MPa pressure, temperature max. 350 for the needs of the plant
|
3.2. |
Steam boiler type |
watertube |
3.3. |
Number of steam boilers |
4 |
3.4. |
Boiler rated output, t/h |
25 |
3.5. |
Steam pressure under rated load at the main steam stop valve, MPa
|
Max. 3,9 |
3.6. |
Superheated steam temperature at the main steam stop valve, °C |
Max. 350 |
3.7. |
Efficiency |
Min. 94% |
3.8. |
Output control range |
20-100% |
3.9. |
Boiler automatic blowdown |
yes |
3.10. |
Anticipate sample points |
yes |
3.11. |
Point of utilization of flue gas heat |
yes |
3.12. |
Provide operation under the load of 110%
|
yes |
4. |
Burner |
yes |
4.1. |
Gas heater |
yes |
4.2. |
Heating of air coming for burning |
yes |
4.3. |
Cleaning of air used for burning |
From mechanical impurities |
4.4. |
Flue gas recirculation through a burner
|
Yes
|
4.5. |
Air supply |
forced |
4.6. |
Automatic regulation of capacity by means of gas flow rate regulation depending on steam boiler pressure
|
yes |
4.7. |
Fuel-air automatic regulation
|
yes |
4.8. |
Automatic ignition |
yes |
4.9. |
Flare stack control system |
yes |
4.10. |
Reducing of high inlet pressure to working pressure
|
yes |
4.11. |
Control of maximum and minimum gas pressure
|
yes |
4.12. |
Fan frequency regulation |
yes |
4.13. |
Smoke exhauster frequency regulation |
yes |
4.14. |
Shut-off valves leakage monitoring |
yes |
4.15. |
Regulation by residual oxygen in flue gas
|
yes |
5. |
Deaerating plant |
|
5.1. |
Type |
atmospheric |
5.2. |
Anticipate a damp condenser |
yes |
6. |
Economizer |
yes |
7. |
PRDS |
2 pcs. |
7.2. |
Parameters at the outlet |
|
|
- max. allowable |
1,5 MPa, 295 °С; |
|
- working |
1,1 MPa, 270 °С
|
7.3. |
Maximum flow rate through each PRDS |
50 t/h |
7.4. |
Anticipate automatic and manual valve control |
yes |
8. |
Metering unit |
yes |
8.1. |
Output of overheated steam from the boiler |
yes |
8.2. |
Output of reduced steam from the plant
|
yes |
8.3. |
Feed water supply to the boiler |
yes |
8.4. |
Gas supply to the boiler |
yes |
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