Fired Heater Training Curriculum
Module from the Fired Heater Training Curriculum curriculum.
MODULE 1: FIRED HEATER FUNDAMENTALS · Learning Objectives · After completing this module, you will be able to: 1. Identify major heater components and their functions 2. Classify heater types by geometry and application 3. Explain the three modes of heat transfer in a fired heater 4. Define key heater parameters (duty, efficiency, flux, bridgewall temperature) 5. Read and interpret a heater design data sheet · Heater Type Classification
| Type | Geometry | Tube Arrangement | Typical Application | Firing | Advantages | API 560 Class |
|---|---|---|---|---|---|---|
| Vertical Cylindrical | Cylindrical shell, vertical tubes | Vertical, against wall | Process heaters, reboilers | Floor-fired (upward) | Even heat distribution, compact footprint | Radiant wall |
| Cabin/Box | Rectangular box | Horizontal, multiple rows | Large process heaters, crude units | Wall-fired (horizontal) | High capacity, multiple passes | Box type |
| Arbor/Wicket | A-frame or inverted V | Horizontal, A-frame | Reformer furnaces | Top-fired (downward) | Very even tube-side temperature | Special |
| Helical Coil | Cylindrical, helical tubes | Helical coil around burner | Small duties, regen gas heaters | Center-fired | Compact, high surface/volume | Special |
| Double-Fired | Rectangular, tubes in center | Horizontal, center-fired both sides | Large capacity, crude/vacuum | Wall-fired from both sides | Maximum capacity per unit | Box type |
| Heat Transfer Modes in a Fired Heater | ||||||
| 1. RADIATION (dominant in radiant section): Q_rad = σ × ε × A × (T_flame⁴ - T_tube⁴) • σ = Stefan-Boltzmann constant (0.1713 × 10⁻⁸ BTU/hr·ft²·R⁴) • ε = emissivity (flame gas: 0.3-0.6, tube: 0.8-0.95) • Fourth-power temperature dependence: small T change = large Q change • Radiant section absorbs 60-75% of total duty 2. CONVECTION (dominant in convection section): Q_conv = h × A × LMTD • h = convective heat transfer coefficient • Enhanced by extended surface (fins): 2-5× bare tube area • Convection section absorbs 20-35% of total duty 3. CONDUCTION (through tube wall): Q_cond = k × A × ΔT / t • Usually not limiting (thin metal wall, high k) • Becomes important with thick coke layer inside tubes (low k = insulating) |
Source: Fired_Heater_Training_Curriculum_v1.xlsx · Sheet: Module 1 - Fundamentals
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