Tubular Type · Carbon Steel · ND Steel · Enamel-Coated · ASME / GB Code

Tubular Air Preheaters

Shell-and-tube air preheaters for power boilers, industrial boilers, and waste heat recovery systems. Material grade — carbon steel, ND steel, or enamel-coated — is selected against flue gas dew point and fuel sulfur content to match service life to outage interval.

Carbon steel / ND steel / Enamel
ASME S-stamp · GB Grade A
Cold-end replacement supply
Dew point corrosion design
Tubular Air Preheater - ORL Power Manufacturing

Fundamentals

How a Tubular Air Preheater Works

A tubular air preheater (APH) recovers heat from boiler flue gas to preheat combustion air before it enters the furnace. Raising combustion air temperature by 100°C improves boiler thermal efficiency by approximately 2–2.5% and reduces fuel consumption. The trade-off is that the APH cold end operates below the flue gas acid dew point — which is why material selection is the critical design decision.

Construction and Operating Principle

1
Shell-and-tube construction
ORL Power manufactures the tubular type only. Tubes are expanded or welded into upper and lower tube sheets. Flue gas flows inside the tubes from top to bottom; combustion air flows outside the tubes in cross-flow or counter-flow through baffles. The tube sheet and shell form the pressure boundary separating the two streams.
2
Hot end vs cold end
The hot end (flue gas inlet, air outlet) operates at 200–400°C — above the acid dew point, with oxidation and gas-side erosion as the primary concerns. The cold end (flue gas outlet, air inlet) operates at 90–160°C — frequently below the sulfuric acid dew point, making acid condensate corrosion the primary failure mechanism. These two zones sometimes use different tube materials.
3
Acid dew point — the critical design temperature
When SO₃ in the flue gas contacts the tube wall below approximately 130–160°C (depending on SO₃ concentration and moisture content), it condenses as sulfuric acid. Concentrated H₂SO₄ corrodes carbon steel at rates of several millimetres per year. The cold end exit gas temperature must be set above the dew point — or the tube material must tolerate the condensate. This single decision governs APH material selection more than any other factor.
4
Fly ash erosion at the hot end
Coal-fired and biomass boilers carry fly ash in the flue gas at velocities of 8–14 m/s inside the tubes. Ash particles erode the tube wall, particularly at the hot end inlet where velocities are highest. Tube material, flue gas velocity, and tube wall thickness are all specified to achieve the required erosion life between tube replacements.
Tubular air preheater tube bundle detail

Where APHs Are Used

  • Coal-fired power station boilers
  • Bagasse & biomass cogeneration boilers
  • Industrial package boilers (oil & gas fired)
  • CFB boilers — convection pass tail end
  • Waste-to-energy boiler tail gas cooling
  • Cold-end replacement during scheduled outage
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Product Range

APH Types by Corrosion Risk

The right tube material depends on fuel sulfur content and cold-end flue gas exit temperature. These two factors determine whether the cold end will operate above or below the acid dew point — and by how much. Three material configurations cover the full range of industrial boiler applications.

Carbon Steel APH

The standard configuration for natural gas-fired boilers, low-sulfur coal, and applications where cold-end exit temperature is maintained well above the acid dew point. Suitable when fuel sulfur content is below 0.5% and cold-end temperature is held above 130°C. Lowest cost and shortest lead time of the three configurations.

Tube material

20G / SA-178A

Fuel suitability

Gas / low-S coal

Cold-end temp

Above 130°C

Tube sheet

Q345R / SA-516

  • Lowest cost and shortest lead time
  • New build with confirmed low-sulfur fuel
  • Wall thickness sized for erosion life target
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ND Steel Cold-End APH

The most common configuration for coal-fired and heavy-oil-fired boilers. ND steel (09CrCuSb) tolerates acid condensation rather than preventing it — its Cr, Cu, and Sb additions dramatically reduce corrosion rate in dilute H₂SO₄ versus carbon steel. The cold end can operate at or below the dew point without rapid tube loss.

Tube material

09CrCuSb (ND)

Fuel suitability

Coal / heavy oil

Corrosion resistance

~5–8× vs C-steel

Common use

Cold-end / full APH

  • Cold-end only, or complete APH in ND steel
  • Matched to original geometry for drop-in fit
  • Most common coal-fired plant replacement
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Enamel-Coated APH

For the most severe corrosion environments — high-sulfur coal, waste-to-energy flue gas containing HCl and SO₃, or where cold-end temperature must be set very low to maximise heat recovery. A fused glass enamel coating on inner and outer tube surfaces is chemically inert to both sulfuric and hydrochloric acid. The smooth surface also resists ash fouling.

Tube material

CS + glass enamel

Acid resistance

H₂SO₄ + HCl

Fuel suitability

High-S coal / WtE

Surface

Smooth / low fouling

  • Maximum dew point corrosion resistance
  • Suitable where HCl is present (WtE / refuse)
  • Smooth surface reduces soot deposits
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Quick Material Selection Guide

Fuel / Application Sulfur Content Cold-End Risk Recommended Tube
Natural gas Negligible None Carbon steel (20G)
Low-sulfur coal (< 0.5%S) Low Low — manage exhaust temp Carbon steel (20G)
Bituminous coal (0.5–2%S) Medium Moderate dew point risk ND steel (09CrCuSb)
High-sulfur coal / heavy oil (> 2%S) High Significant corrosion ND steel (09CrCuSb)
Waste-to-energy / municipal refuse Variable + HCl Severe — H₂SO₄ + HCl Enamel-coated
Bagasse / biomass (mixed fuel) Low–medium Low–moderate Carbon steel or ND steel

Not sure which applies to your fuel? Tell us fuel type, sulfur content (if known), and cold-end design temperature — we'll confirm the tube material.

Get Material Advice

Quality Assurance

Materials & Standards

Air preheater tube material is selected against dew point corrosion risk, not temperature or pressure alone. The applicable code governs the tube sheet and pressure boundary design — the tube material governs service life between replacements.

Tube Material by Corrosion Environment

20G / SA-178A — standard carbon steel
GB/T 3087 grade 20G or ASME SA-178 Grade A seamless or ERW tube. The baseline for natural gas and low-sulfur coal fired boilers where the cold-end temperature is managed above 130°C. Readily available, lowest cost. Wall thickness is specified to provide adequate erosion life at the hot end — typically 2.5–4.0 mm for industrial boilers. Not suitable where dew point condensation is expected.
09CrCuSb — ND steel
A Chinese standard low-alloy steel (GB/T 3087) developed specifically for air preheater cold-end service. The addition of Cr (0.7–1.0%), Cu (0.25–0.45%), and Sb (0.04–0.10%) raises the pitting resistance of the steel surface in dilute H₂SO₄. Corrosion rate in condensed sulfuric acid is 5–8 times lower than carbon steel under equivalent conditions. This is not a stainless steel — it is a corrosion-resistant low-alloy tube that can be processed on standard tube fabrication equipment. The standard choice for coal-fired industrial boiler cold ends.
Glass enamel-coated carbon steel
Carbon steel tube with a fused borosilicate glass enamel coating applied to the inner (flue gas side) and outer (air side) surfaces. The enamel is chemically inert to both H₂SO₄ and HCl across the pH range found in boiler cold-end condensate. The carbon steel tube provides the mechanical strength. Coating thickness is typically 0.4–0.8 mm; the tube wall remains the structural component. Used where ND steel is insufficient — high-sulfur coal boilers operating with low cold-end temperatures, and waste-to-energy boilers with chlorine in the flue gas. The smooth enamel surface also reduces ash adhesion and soot-blowing interval.
Dual-material bundle — carbon steel hot end, ND steel cold end
For larger APHs, the bundle is split horizontally into a hot-end section (upper, carbon steel) and a cold-end section (lower, ND steel or enamel). The hot end sees erosion but no acid condensate; carbon steel is adequate and cheaper. The cold end sees the dew point zone and requires the corrosion-resistant tube. Replacing only the cold-end section during outages reduces cost significantly compared to replacing the full bundle.

Tube Sheet, Shell, and Pressure Boundary

TS
Tube Sheet — Q345R / SA-516 Gr.70
Upper and lower tube sheets are the primary pressure boundary elements. Material is Q345R (GB/T 713) or SA-516 Gr.70 (ASME). Thickness calculated from design pressure, tube pitch, and tube diameter per ASME Section I PG-52 or GB/T 16507. Tubes are either expanded into the tube sheet (low pressure service) or seal-welded (pressure code applications). All tube-to-tube-sheet welds are inspected by dye penetrant or magnetic particle after fabrication.
SH
Shell and Air Casing — Q235B / A36
The outer shell and air-side casing are fabricated from structural steel plate (Q235B or A36 equivalent). The shell is designed for air-side operating pressure — typically 5–30 kPa above atmospheric — and is a non-pressure-code component. Baffles inside the air casing direct cross-flow over the tube bundle to increase heat transfer and minimise air-side bypass.
EJ
Expansion Joints
Thermal differential between the hot flue gas duct and the cooler air casing requires expansion joints at the duct connections. Metallic bellows or fabric compensators are specified based on operating temperature and movement requirements. ORL Power supplies the APH complete with expansion joints and flange connections ready for site bolting.

Cold-end replacement supply: If only the cold-end tube section has failed, ORL Power can supply replacement cold-end tubes and tube sheets matched to the original APH geometry — without replacing the shell, casing, or hot-end section. This requires the existing APH drawing or field measurements to confirm tube OD, pitch, and tube sheet thickness.

Certifications & Compliance

Grade A Boiler

Grade A Boiler

ISO 9001

ISO 9001

ISO 14001

ISO 14001

ISO 45001

ISO 45001

EN 1090

EN 1090

EN 3834

EN 3834

ASME S

ASME S

ASME U

ASME U

Our Advantage

Why Choose ORL Power

An air preheater that fails between outages forces an unplanned shutdown. The points below reflect what ORL Power does differently to make early failure uncommon — starting with material selection, not ending with it.

Dew Point Check Before Material Confirmation

Before we confirm a tube material, we ask for fuel sulfur content and cold-end design temperature. If a customer specifies carbon steel for a coal-fired boiler running at 120°C cold-end exit — below the dew point — we flag it in writing before taking the order. We are not interested in supplying an APH that will corrode out in 18 months.

ND Steel MTC Verification — Every Heat

ND steel (09CrCuSb) is only effective if the Cr, Cu, and Sb additions are within specification. We verify the 3.1 MTC chemistry against the GB standard for every tube heat before it enters production. Tubes from heats outside the Sb range (0.04–0.10%) are rejected — the corrosion resistance depends on getting that number right.

Tube-to-Tube-Sheet Joint Quality

The tube-to-tube-sheet joint is the most common leak location on an in-service APH. We qualify the expansion procedure (or seal weld procedure) against the applicable code before production. Each joint is tested in the hydrostatic test, and a dye penetrant check is run on all seal welds. Tube pitch and projection length are verified by dimensional inspection report against the drawing.

Cold-End Replacement Geometry Match

Replacement cold-end sections must fit the existing APH shell without modification. We manufacture to the original drawing dimensions — tube OD, wall, pitch, tube sheet thickness, flange drilling, and nozzle locations. If no drawing exists, we work from field measurements and photographs. The replacement section is pre-assembled and dimensionally verified before crating.

Complete APH from One Source

ORL Power supplies the complete APH assembly — tube bundle, tube sheets, shell, air-side casing, baffles, access doors, expansion joints, and all nozzle connections — under a single code data report. For boiler OEMs and EPC contractors, this eliminates the coordination risk between a tube fabricator and a casing fabricator that is common when splitting the supply.

Outage Window Delivery

APH replacement is always tied to a planned outage window. We confirm the delivery date at order placement with a production milestone schedule — material receipt, tube expansion, testing, and despatch dates are all fixed, not estimated. For short-window outage replacements, we advise the customer to initiate procurement at least 10–14 weeks before the outage start date for ND steel orders.

Tell us your fuel type, sulfur content, and cold-end temperature.

We'll confirm tube material, geometry, and delivery schedule in one reply.

Start Your Inquiry

Applications

Industries We Serve

Every combustion boiler generates flue gas that can preheat incoming air. The buyer is typically a boiler OEM building a new unit, an EPC contractor specifying the complete boiler island, or a plant owner replacing a corroded cold-end section during a scheduled outage.

Power Plants

Coal-fired and biomass power station boilers. Tubular APHs at the tail end of the flue gas duct, after the economizer. Cold-end replacement supply in ND steel or enamel-coated tubes for boilers burning medium- to high-sulfur coal where the original carbon steel cold end has corroded through.

Coal · CFB · Biomass power

Sugar Mills & Cogeneration

Bagasse-fired cogeneration boilers for the sugar industry. Bagasse has low sulfur content but high moisture, and the flue gas carry-over of fibre and ash makes erosion at the APH hot end the primary concern. Carbon steel tubes at adequate wall thickness for the expected erosion rate are the standard specification.

Bagasse boiler · IBR · Cogeneration

Industrial Package Boilers

Oil- and gas-fired package boilers for process steam supply in chemical, pharmaceutical, food, and general industry. Low sulfur fuel — carbon steel APH with managed exhaust temperature. Boiler OEMs supplying the complete packaged unit specify the APH as part of the pressure parts package.

Oil & gas boiler · Process steam · OEM supply

Waste-to-Energy & High-Sulfur Applications

Municipal solid waste and refuse-derived fuel boilers with chlorine and SO₃ in the flue gas. Enamel-coated tube APHs for the highest corrosion resistance. Also covers high-sulfur coal boilers in markets where fuel quality is variable — cement plants, lime kilns, and industrial coal consumers burning whatever is available.

WtE · High-sulfur coal · Enamel tube
Tell us your fuel and boiler type.

We'll confirm tube material, design approach, and lead time in one reply.

Discuss Your Application

Manufacturing Process

Factory & Process

Tubular APH quality depends on three things that cannot be inspected after the fact: the tube material chemistry, the tube-to-tube-sheet joint integrity, and the dimensional accuracy of the completed bundle. Each production step is documented so that by the time the APH leaves the shop, the quality record is already complete.

Key Production Steps

01
Tube & Tube Sheet Incoming Inspection
Tube OD, wall thickness, and length verified against 3.1 MTC. For ND steel (09CrCuSb), the Cr, Cu, and Sb chemistry is checked against the GB specification for every tube heat — not spot-checked. Tube sheet plate thickness and material grade confirmed. Any material outside specification is rejected before cutting begins.
02
Tube Sheet Drilling
Tube holes are drilled on CNC equipment to the specified tube pitch and pattern (square or triangular). Hole diameter is sized to the tube OD and the expansion or welding tolerance specified by the code. Burrs are removed and hole surface finish is checked — surface finish affects expansion joint quality.
03
Tube Cutting & Bundle Assembly
Tubes are cut to the specified length within ±0.5 mm. Intermediate tube support plates (baffles) are installed at the designed pitch to prevent tube vibration and maintain the cross-flow pattern. Tubes are inserted through support plates and both tube sheets, with projection length controlled to drawing tolerance.
04
Tube-to-Tube-Sheet Joining
Mechanical expansion (rolling) is used for low-pressure industrial boilers. Seal welding (GTAW) is added for ASME Section I and GB/T 16507 code applications. Expansion parameters (torque, wall reduction %) or weld parameters (current, travel speed, filler) are qualified before production and documented in the WPS. Each seal weld receives a dye penetrant inspection after completion.
05
Shell, Casing & Nozzle Assembly
The tube bundle is enclosed in the flue gas shell (upper and lower headers) and the air-side casing. Baffles directing cross-flow are installed and verified for bypass gap control. All gas-side and air-side nozzles are welded, and nozzle welds receive PT or MT inspection. Expansion joints are installed at duct flanges.
06
Hydrostatic Test, Dimensional Check & Despatch
The completed APH is hydrostatically tested at 1.5× design pressure on the gas-side pressure boundary. An air leak test is conducted on the air-side casing at the design pressure. Overall dimensions, nozzle orientations, and flange drilling are confirmed against the drawing in a dimensional inspection report. The unit is drained, dried, end-capped, and crated for sea freight.

Customer Visits & Factory Evidence

Customer Visit Quality Inspection Production Line Engineering Discussion Technical Review

Customers review tube material certifications, inspect tube-to-tube-sheet joints, and witness the hydrostatic test during factory visits.

15+
Years Manufacturing
Since 2009
300+
APH Units Supplied
New build & replacement
50+
Countries Served
Export network
24h
Technical Response
Engineering team direct

Frequently Asked Questions

Air Preheater FAQ

Common questions from plant engineers, EPC contractors, and boiler OEMs about tubular APH design, material selection, and cold-end replacement.

How do I choose between carbon steel, ND steel, and enamel-coated tubes?

The decision is determined by two numbers: fuel sulfur content and cold-end flue gas exit temperature. These two inputs determine whether the tube wall will operate above or below the acid dew point during normal operation.

The acid dew point for a boiler burning 1%S coal is typically around 130–140°C. If your cold-end exit temperature is 150°C — 10–20°C above the dew point — carbon steel is adequate with managed combustion and boiler start-up procedures. If your cold-end temperature is 120°C, acid condensation is continuous during operation, and carbon steel will corrode rapidly.

ND steel (09CrCuSb) is the right choice when your coal sulfur content is 0.5–3% and the cold-end temperature will operate at or near the dew point for significant periods. It does not prevent condensation — it survives it far longer than carbon steel. Typical life improvement is 4–8 times over carbon steel in the same service.

Enamel-coated tubes are specified when ND steel is insufficient — specifically when the flue gas contains HCl (waste-to-energy, high-chlorine coal), when sulfur content is consistently above 3%, or when the cold-end temperature must be set very low to maximise heat recovery from the flue gas. If you send us your fuel analysis and cold-end temperature, we will advise the tube material in writing.

Can you supply only the cold-end replacement without replacing the entire APH?

Yes — cold-end replacement supply is one of ORL Power's most frequent APH orders. When only the low-temperature tube section has corroded through, replacing the entire APH (including the still-serviceable hot-end section and shell) is unnecessary and costly. We supply a replacement cold-end tube bundle that installs directly into the existing APH shell using the existing flanges.

To supply a matched replacement cold end, we need from you: the existing APH drawing (or field-measured tube OD, tube pitch, tube length, tube sheet thickness, and flange drilling), the number of tubes in the cold-end section, the current tube material (to confirm what failed and what upgrade is appropriate), and the required delivery date relative to your outage window.

If the original drawing is not available, we work from field measurements and photographs. We generate a detailed drawing for your approval before fabrication begins. The replacement section is dimensionally verified against the drawing before despatch.

What is the difference between a tubular APH and a rotary regenerative APH?

A tubular APH (the type ORL Power manufactures) is a recuperative heat exchanger — the two gas streams are permanently separated by the tube wall. Flue gas flows inside the tubes; air flows outside. There is no moving parts and no leakage path between the gas streams. The heat transfer surface is fixed in place. Maintenance involves replacing tubes or tube sections that have corroded or eroded.

A rotary regenerative APH (Ljungström type) uses a rotating matrix of corrugated metal plates that alternately passes through the hot flue gas stream and the cool air stream, transferring heat through the matrix mass. Rotary APHs are more compact and can transfer more heat per unit weight — which is why they are dominant in large coal-fired power stations above 200 MW. However, they have inherent air-to-gas leakage (through the rotating seals), require continuous maintenance of the drive mechanism and seals, and the corrugated plate elements corrode at the cold end in the same way as tubes.

For industrial boilers (typically below 100 MW equivalent thermal output), package boilers, sugar mill boilers, and waste heat boilers, the tubular design is standard — simpler, more reliable, and easier to maintain or partially replace.

What information do you need for a quotation?

The fastest route is to send your APH drawing. If no drawing exists, we need the following minimum information:

  • • Fuel type and sulfur content (determines tube material)
  • • Flue gas inlet and outlet temperature (°C)
  • • Air inlet and outlet temperature (°C)
  • • Flue gas flow rate (kg/h or Nm³/h)
  • • Air flow rate (kg/h or Nm³/h)
  • • Flue gas side design pressure (kPa)
  • • Air side design pressure (kPa)
  • • Tube OD and wall (or allow us to calculate)
  • • Applicable code (ASME Section I / GB/T 16507 / EN 12952 / IBR / other)
  • • Supply scope: complete APH, or cold-end replacement only
  • • Quantity and required delivery date

For cold-end replacement: additionally tube pitch, tube sheet thickness, shell ID, and flange drilling, so that the replacement section matches the existing APH geometry.

What are typical lead times?

Lead times from drawing approval (or from our issued drawing if we generate from design conditions):

  • Carbon steel cold-end replacement (ND steel tubes, standard sizes): 8–12 weeks
  • Complete carbon steel APH, new build: 10–14 weeks
  • Complete ND steel APH, new build: 12–16 weeks
  • Enamel-coated tube APH: 14–18 weeks (enamel coating adds process time)

Lead times are confirmed at order placement with a fabrication milestone schedule. For outage replacement orders, initiate procurement at least 10–14 weeks before your outage start date to allow adequate time for drawing approval, fabrication, and sea freight.

Do you supply the complete APH or just the tube bundle?

ORL Power can supply either. The standard supply scope for a new APH is the complete assembly: tube bundle (tubes, tube sheets, baffles), flue gas shell (upper and lower headers or box headers), air-side casing, all nozzle connections, access doors, and flue gas duct expansion joints. The complete assembly arrives on site ready to bolt into the duct system.

For cold-end replacement, the supply scope is typically: replacement cold-end tube bundle with tube sheets and connecting flanges, sized to fit directly into the existing APH shell without modification to the hot-end section or shell. In this case the air-side casing and shell are retained from the existing unit. We confirm the supply scope in writing at quotation stage — there should be no ambiguity about what is and is not included.

Have a technical question not covered here?

Ask Our Engineering Team

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Contact Our Engineering Team

Send your APH drawing, or tell us your fuel type, gas temperatures, flow rates, and applicable code. We reply within 24 hours with tube material recommendation, pricing, and lead time.

Get Your APH Quote

Share your fuel type and design conditions — we reply within 24 hours with material recommendation, pricing, and lead time.

Email
orl@orlpower.com
Phone / WhatsApp
+86-187 5115 1030
Location
Jiangsu, China

What to Include in Your Inquiry

  • • Fuel type and sulfur content (%)
  • • Flue gas inlet / outlet temperature (°C)
  • • Air inlet / outlet temperature (°C)
  • • Flue gas and air flow rates (kg/h)
  • • Design pressure — gas side and air side
  • • Supply scope: complete APH or cold-end replacement
  • • Applicable code (ASME / GB / EN / IBR)
  • • Quantity and required delivery date
  • • Drawing (if available) — attach or email