This page explains how Tail Gas Heater is classified within Chemical Manufacturing. Technical values and manufacturer relationships are research references; confirm the current specification and supplier evidence for each order.
A heat exchanger that recovers thermal energy from nitric acid plant tail gases to improve system efficiency.
Technical details and manufacturing context for Tail Gas Heater
| Parameter | Typical range | Notes & selection driver |
|---|---|---|
| Design Pressure | 1.0–1.6 MPa | GB/T 150 |
| Design Temperature | 200–450 °C | Above 450°C material creep becomes significantGB/T 150 |
| Heat Transfer Area | 20–200 m² | Select based on required duty |
| Tube Material | 304L/316L | Higher alloys for corrosive environmentsASTM A312 |
| Shell Material | Q345R/304 | Carbon steel for non-corrosive serviceGB/T 713 |
| Tube Wall Thickness | 2.0–3.0 mm | Thicker for higher pressureASTM A312 |
| Shell Wall Thickness | 8–16 mm | Determined by pressure and diameterGB/T 150 |
| Tube Bundle Length | 3000–6000 mm | Longer tubes increase efficiency but require more space |
| Number of Tube Passes | 1–2 | More passes increase velocity and heat transfer |
| Design Code | GB/T 151 | Chinese standard for heat exchangersGB/T 151 |
| Leak Test Pressure | 1.5×design MPa | Hydrostatic test per codeGB/T 150 |
| Weight | 2000–15000 kg | Affects installation and foundation |
Ranges are indicative industry figures for RFQ preparation, not a supplier commitment. Confirm every value and standard with the legal manufacturer before ordering.
| pressure: | Up to 10 bar (145 psi) operating pressure |
| flow rate: | 10,000-100,000 Nm³/h (5,900-59,000 SCFM) |
| temperature: | Up to 600°C (1112°F) inlet, typical ΔT 100-300°C |
| slurry concentration: | Not applicable - gas phase only, particulate loading <50 mg/Nm³ |
Indicative industry ranges for design and RFQ preparation. Confirm the exact figures and applicable standard with the manufacturer before specifying.
Quoted from the published standard.
Manufacturer profiles associated with Tail Gas Heater.
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A practical evidence checklist for RFQ preparation and supplier evaluation.
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The design pressure is typically in the range of 1.0–1.6 MPa, as per GB/T 150. However, the exact value must be confirmed for the specific model and application.
Tube material is often stainless steel 304L or 316L, while shell material may be Q345R or 304. Nickel alloys may be used for high-temperature or corrosive sections. Confirm material suitability with the manufacturer.
It recovers heat from the hot tail gas stream and transfers it to a cooler process stream, such as combustion air, preheating it. This reduces the energy needed for heating, lowering overall energy consumption.
The design typically follows GB/T 151 for heat exchangers and GB/T 150 for pressure vessels. Leak test pressure is 1.5 times the design pressure. Always verify compliance with the manufacturer.
Editorial classification, named public sources where available, and source-reviewed manufacturer records.
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