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Notes
3. Vertical-tubes maximum straight length shall be 183 m (60 ft) |
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Note: Coil sections are in ascending order, going up the convection section.
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Use the datasheet below to input your data and run your performance case
CO₂ | mol % |
H₂O | mol % |
N₂ | mol % |
O₂ | mol % |
SO₂ | mol % |
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APH System
Equipment APH, FD Fan, ID Fan & Ducting
BID / PROJECT VALUE
Heater Duty | ||
Total Heat Release | ||
Efficiency |
SAFETY AND COMPLIANCE
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Materials & Equipment Supply
Steelwork & Fabrication |
Detail Engineering
Process & Thermal Design, Mechanical Design |
Shipping & Delivery
1. Radiant Section - fully modulurised |
Terms
1. Delivery: 54 weeks (28 weeks Detailed Eng. only) |
Our Partners & Vendors
Heater companies:
Birwelco
FEI
GasTech
KT-Technology
Thermax
Burner Vendors:
Callidus (UOP)
Greens Combustion
ICE
John Zink Hamworthy
Zeeco
Fabricators:
Vatana Phisal (VPE)
Vipco
Steelcon Malaysia
AD Demirel
Polimex
Refractory:
Morgan
Linco Baxo
Insulcon B.V.
Zibo Luzhong
1. Fuel Temperature as per project specifications. This value is not reported here.
2. Fuel Pressure typically ~2 barg (29 psig) at maximum burner heat release. This value is not reported here.
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1. Fuel Temperature as per project specifications. This value is not reported here.
2. Fuel Pressure typically ~2 barg (29 psig) at maximum burner heat release. This value is not reported here.
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Online API Fired Heater Software
1. DIMENSIONS TO BE CONFIRMED DURING DETAILED ENGINEERING PHASE |
2. LADDERS AND PLATFORMS SHALL BE IN ACCORDANCE WITH API 56O REQUIREMENTS MINIMUM AND PROJECT SPECIFICATIONS |
3. THIS PROPOSAL DRAWING SHOULD BE CONSIDERED AS A SKETCH AND MAY NOT BE ENTIRELY DRAWN TO SCALE |
4. REFRACTORY MATERIAL AND THICKNESSES SHALL BE AS PER PROJECT HEATER DATASHEET |
5. PLEASE REFER TO COIL CONFIGURATION AND MATERIAL WITHIN THE TABLE BELOW |
6. DOORS SHALL BE PROVIDED IN ACCORDANCE WITH PROJECT HEATER DATASHEET |
REV | DATE | DRAWING DESCRIPTION | BY | CHK |
GENERAL ARRANGEMENT DRAWING |
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Heater Type:
Carbon Dioxide | |
Sulphur Dioxide | |
Carbon Monoxide | <100 ppm |
N2 Oxides (NOx) | <150 ppm |
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1) The max flux calculated on a individual tube basis (see tube profile results data).
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Firing Notes
1. The Lower Heating Value (LHV) of the fuel efficiencies shall be used for efficiency calculations
2. Typical radiation heat loss value of 1.5% is used typically considered. However, in cases with a flue gas/air preheater, a value of 2.5% is normally considered.
3. Typical Excess Air values can be used as follows:
- Natural Draft - 15% excess air
- Forced Draft - 10% excess air
4. API 560 - Pressure at the Arch should be maintained at -2.5mmH₂Og (-0.1inH₂Og)
Tube Support Notes
1. Design temp. for tube supports should be Arch temp + 100 C (180 F)
2. No credit should be considered for shielding effect of tube supports by refractory
3. API 560 states if fuel the Vanadium + Sodium content in fuel exceeds 100ppm, supports to be either:
- 50Cr-50Ni metallurgy, without any coating
- Covered with 50 mm (2 in) of castable refractory (see API 560)
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Notes
1. One UV scanner per burner is recommended (if total no. burners < 20)
2. One Pilot per burner is recommended
3. Electric spark ignition is recommended for each pilot
4. Forced draft system
Notes
1. The Lower Heating Value (LHV) of the fuel efficiencies shall be used for efficiency calculations
2. Typical radiation heat loss value of 1.5% is used typically considered. However, in cases with a flue gas/air preheater, a value of 2.5% is normally considered.
3. Typical Excess Air values can be used as follows:
- Natural Draft - 15% excess air
- Forced Draft - 10% excess air
4. API 560 - Pressure at the Arch should be maintained at -2.5mmH₂Og (-0.1inH₂Og)
HeaterSIM - Fired Heater Simulation Results
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HeaterSIM - Fired Heater Simulation Results
Online API Fired Heater Software
HeaterSIM - Fired Heater Simulation Results
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HeaterSIM - Fired Heater Simulation Results
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HeaterSIM - Fired Heater Simulation Results
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HeaterSIM - Fired Heater Simulation Results
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Notes
1. For vertical-tube, vertical-fired heaters, the maximum radiant straight tube length shall be 18,3 m (60 ft)
2. For horizontal heaters fired from both ends, the maximum radiant straight tube length shall be 12,2 m (40 ft)
3. API 560 - The tube-wall thickness should be in accordance with ISO 13704 (unless otherwise mutually agreed)
4. API 560 - Tube-wall thicknesses should include the minimum allowances for corrosion and/or erosion as follows:
- Carbon Steel Tubes - 3mm (0.125in)
- P Grade Tubes Tubes - 2mm (0.08in)
- Stainless Steel Tubes - 1mm (0.04in)
5. The unsupported length of horizontal tubes shall not exceed 35 times the outside diameter or 6 m (20 ft), whichever is less.
Calculation of Heater-tube Thickness in Petroleum Refineries
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BPVC Section I Rules for Construction of Power Boilers
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BPVC Section VIII Rules for Construction of Pressure Vessels
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Notes
1. Environmentally friendly body-soluble fibre is the recommended choice for fire insulation
2. HW and MW Castable is strong enough to be used on floor without a top brick layer
3. Ceramic fibre insulation are typically used in all areas except stack and ducting.
4. Ceramic fibre not suitable for convection sections with sootblowers or steam lances are used for cleaning.
5. Vapour barrier protective coating is required behind all areas lined with ceramic fibre
6. SS foil barrier is required for ceramic fibre lined areas if the sulphur content exceeds 500ppm by mass.
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Emissions Control Unitincludes automatic pressure control system |
£ | 67,000 |
BMS Engineeringincludes Control Philosophy, Cause & Effects, BMS Definition and Permissives Table |
£ | 9,200 |
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CO2 | H2O | N2 | O2 | SO2 |
Mol% | Mol% | Mol% | Mol% | Mol% |
CO2 | H2O | N2 | O2 | SO2 |
Mol% | Mol% | Mol% | Mol% | Mol% |
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Ridiyah Refinery
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Enter properties for the inlet and outlet only, then our Wizard create a Properties Table for you.
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- Detailed combustion performance
- Flue gas flow patterns
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MixStreamName | Name your Fluid | ||
ProName | Select Process | ||
ProFlow | Process Flow | kg/s | |
SteamFlow | Steam Flow | kg/s | |
SteamTemp | Steam Temperature | °C | |
SteamPress | Steam Pressure | kPa | |
ProMassFlowsToMix | |||
ProcessNamesToMix |
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