Flue Gas Filtration: How to Clean Hot Industrial Exhaust Above 260°C
- Flue gas filtration removes dust, acid gases, NOx and dioxins from industrial exhaust before the stack — the technology choice is decided first by gas temperature.
- Above roughly 260°C, fabric bags fail and the classic answer is an ESP plus a chain of reactors; a rigid ceramic fiber filter handles 600°C continuously (1,000°C peak) and captures >99.9% of dust in one vessel.
- In its catalytic grade, the same ceramic element also destroys NOx (up to 95%) and dioxins (up to 99.5% TEQ), collapsing filter, scrubber and SCR tower into a single unit.
- Measured plant data: a 120,000 m³/h float glass furnace holds dust at 4 mg/Nm³, NOx at 36 mg/Nm³ and SO₂ at 35 mg/Nm³ at the outlet.
Contents: What is flue gas filtration · What must be removed · Technology comparison · Why temperature decides · Ceramic fiber filtration · System design · Applications · Measured data · FAQ
Flue gas filtration is the removal of particulate and gaseous pollutants from industrial exhaust before it reaches the chimney. If your process gas leaves a kiln, furnace, boiler or incinerator at 300–600°C, the filtration decision is different from a standard baghouse specification: fabric media is already past its limit, and every degree you cool the gas to protect it is energy you pay to move and then lose. This guide is written for plant engineers and EPC teams specifying hot gas cleaning — it compares the three realistic technology routes, explains where ceramic fiber filtration fits, and shows measured outlet data from operating plants.
What Is Flue Gas Filtration?
Flue gas filtration is the stage of an exhaust system that captures particulate matter — dust, ash, soot and condensable aerosols — from combustion or process gas. In a wider sense it also covers the removal of gaseous pollutants (SOx, NOx, HCl, HF, dioxins) that regulations treat together with dust at the stack. A complete flue gas filtration system therefore combines a particulate barrier with, where the permit requires it, acid-gas neutralization and NOx destruction.
The term is often used loosely for the whole gas cleaning train. In this guide we use it precisely: the filtration stage is the barrier that stops particles; everything else — quench towers, scrubbers, SCR reactors — exists either to protect that barrier or to do the chemistry the barrier cannot.
What Needs to Be Removed from Flue Gas
Four pollutant families drive the specification of any flue gas filtration system. Each has a different capture mechanism, which is why the classic answer is a chain of separate units — and why an integrated element changes the economics.
| Pollutant | Typical sources | Classic removal unit | In a ceramic fiber system |
|---|---|---|---|
| Dust / particulate (PM) | All combustion and mineral processes | Baghouse or ESP | Captured on the tube surface at >99.9% |
| Acid gases (SOx, HCl, HF) | Coal, waste, glass, metallurgy | Wet or semi-dry scrubber | Dry sorbent reacts on the filter cake — no sewage |
| NOx | High-temperature combustion | Separate SCR tower | Catalytic grade reduces NOx inside the tube wall, up to 95% |
| Dioxins (PCDD/F) | Waste incineration, metallurgy | Activated carbon injection | Catalytic destruction up to 99.5% (TEQ) in the same element |
Emission limits for these pollutants are set by frameworks such as the EU Industrial Emissions Directive (2010/75/EU) and national standards like China’s GB 4915 for cement — the permit text, not the equipment catalogue, is where a specification should start.
Main Flue Gas Filtration Technologies Compared
Three technologies dominate particulate removal in industrial flue gas. They differ less in efficiency than in what they force you to build around them.
| Factor | Fabric bag filter | Electrostatic precipitator | Ceramic fiber filter |
|---|---|---|---|
| Continuous temperature | Up to ~260°C (fabric limit) | Wide, but drifts with gas conditions | 600°C continuous / 1,000°C peak |
| Collection efficiency | 99.5–99.9% with stable cake; dips after each pulse | Weak on sub-micron and high-resistivity dust | >99.9% at 1 μm, outlet < 5 mg/Nm³ |
| Gas-phase removal | None | None | Catalytic grade: NOx up to 95%, dioxins up to 99.5% (TEQ) |
| Service life (hot, acidic duty) | 1–3 years | Long, but skilled high-voltage maintenance | 5+ years with written warranty |
| What it forces upstream | Quench / dilution air above 260°C | SCR + scrubber downstream for NOx and acid gas | Dry sorbent injection only, when acid gases require it |
Below 260°C with easy dust, a baghouse remains the lowest-cost answer and no honest supplier should tell you otherwise. The interesting territory is above the fabric limit, where the baghouse needs protection and the ESP needs companions. For the element-level economics of the first two columns, see our ceramic filter vs bag filter analysis.
Why Temperature Decides Everything
Every flue gas filtration specification starts at one number: the continuous gas temperature at the filter inlet. Below roughly 260°C, polymer and fiberglass felts survive and the choice is economic. Above it, fabric fails by melting, blinding or embrittlement — and the traditional fix is to cool the gas with dilution air, a heat exchanger or a water quench.
Cooling is not free. Dilution air increases the gas volume the fan must move; a quench adds a tower, water treatment and a condensation risk at every cold spot; a heat exchanger adds pressure drop and fouling duty. Worst of all, the heat you remove to protect the filter is heat the process can no longer recover. In hot duty the filtration question is really: how much of the plant do you want to redesign around a fabric limit?
A rigid ceramic fiber filter tube removes that trade. It operates continuously at 600°C with peaks to 1,000°C, so the gas arrives at the filter at process temperature and leaves for waste heat recovery with its energy intact. The cooling stage, its fan power and its footprint simply disappear from the flowsheet.
Ceramic Fiber Flue Gas Filtration: One Vessel for Dust, NOx and Dioxins
The element is a rigid, self-supporting tube vacuum-formed from alumina-silicate ceramic fiber, with a porosity above 80% and a controlled 3–5 μm fiber diameter. Dust-laden gas passes through the porous wall; particles stop on the outer surface; a 0.4–0.7 MPa pulse-jet releases the cake as intact sheets. Because the ceramic body itself is the barrier — not a dust cake on fabric — collection efficiency stays above 99.9% independent of the cleaning cycle, and outlet dust holds below 5 mg/Nm³. The full mechanism is covered in our hot gas filtration principle guide.
The catalytic grade carries a V₂O₅-TiO₂ catalyst inside the tube wall. Dust is captured on the outer surface before it can reach the catalyst, so the catalyst sees only clean gas — this is what eliminates the catalyst poisoning and channel blinding that plague conventional SCR reactors in dusty service. Within its 170–300°C reaction window the catalytic element delivers up to 95% NOx reduction and up to 99.5% (TEQ) dioxin destruction, while acid gases are neutralized by dry sorbent injected upstream and captured on the filter cake. One vessel replaces the baghouse, the scrubber and the SCR tower. Details are on the catalytic ceramic fiber filter page; for dedusting-only duty, see the standard ceramic fiber filter tube.
There are honest boundaries. Sustained HF above 5 ppm and phosphoric acid mist attack the fiber; free alkali requires sorbent dosing upstream; moisture must stay below 20% by volume; and a catalytic section only works if the gas genuinely sits in its temperature window. A supplier who does not ask for your gas analysis before quoting is guessing.
Flue Gas Filtration System Design: The Four Numbers That Matter
Whether the answer is a baghouse, an ESP or a ceramic system, the sizing inputs are the same four: the temperature profile (continuous, peak, and how long peaks last), the dust loading in g/Nm³ with its particle size distribution, the gas chemistry (HF, H₃PO₄, free alkali, SO₂), and the moisture content relative to the acid dew point. Every premature failure we have seen in 40+ installations traces back to one of these four being assumed rather than measured.
From those four numbers the engineering follows: face velocity of 2–5 cm/s sets the element count (a standard φ150 × φ110 × 3,000 mm element offers about 1.41 m² of filter area), and the pressure-drop budget — 300 Pa clean at 1 m/min, 900–1,500 Pa for the complete system — is checked against the ID fan curve. The step-by-step procedure, including the chemistry boundaries and the purchase-order checklist, is in our filter element selection guide. For retrofitting an existing baghouse, the survey and commissioning sequence is in the baghouse retrofit checklist.
Where Ceramic Flue Gas Filtration Is Already Running
The reference base covers the duties where hot, dirty or chemically aggressive gas defeats fabric media: cement kiln tail and clinker cooler lines, container and float glass furnaces, municipal and industrial waste incinerators, biomass and RDF boilers, non-ferrous metallurgy and industrial boilers. Industry-by-industry fit, including the cases where ceramic is not the answer, is mapped on our ceramic fiber filter applications page.
Two examples frame the range. On a 2,500 t/d cement clinker line in Shandong, retrofitted in 2019, ceramic tubes replaced failing glass fiber bags and have held emissions below 3 mg/Nm³ for over four years at 850°C continuous operation. At a 750 t/d municipal waste-to-energy plant in Guangzhou, the catalytic system consolidated baghouse, acid scrubber and SCR reactor into one vessel.
Measured Performance in Operating Plants
The figures below are measured inlet and outlet values from operating installations — not laboratory projections. Customer names are withheld under confidentiality agreements.
| Plant type | Gas volume | NOx in → out | SO₂ in → out | Dust in → out |
|---|---|---|---|---|
| Float glass furnace, low-temperature DeNOx (Sichuan) | 45,000 m³/h | 3,364 → 11 mg/m³ | 168 → 6 mg/m³ | 865 → 4 mg/m³ |
| Glass furnace, mid-temperature DeNOx (Anhui) | 120,000 m³/h | 2,554 → 36 mg/m³ | 1,050 → 35 mg/m³ | 967 → 4 mg/m³ |
| Marine diesel engine test rig (Shanghai) | 7,289 m³/h | 3,045 → 80 mg/m³ | — | 15.7 → 2.2 mg/m³ |
Full test reports, porosity and pore-diameter documentation are published on our performance & test reports page, and batch-level verification (ISO 9001:2015 production, third-party inspection by SGS, BV or TÜV) is available for any order.
Frequently Asked Questions About Flue Gas Filtration
What is the difference between flue gas filtration and flue gas treatment?
Filtration is the particulate-removal stage — the barrier that captures dust and ash. Treatment is the wider chain that may add desulfurization, denitrification and dioxin control. A ceramic fiber system performs both in one vessel: filtration on the tube surface, gas-phase chemistry inside the catalytic wall.
Can flue gas be filtered without cooling it first?
Yes, with the right media. Fabric bags require cooling above roughly 260°C, but rigid ceramic fiber filter tubes operate continuously at 600°C and tolerate peaks to 1,000°C. The gas is filtered at process temperature and its heat remains available for downstream recovery.
How efficient is ceramic flue gas filtration?
Collection efficiency exceeds 99.9% for particles of 1 μm and above, with outlet dust below 5 mg/Nm³. The catalytic grade additionally removes up to 95% of NOx, up to 95% of SOx with dry sorbent, up to 97% of HCl and up to 99.5% of dioxins (TEQ).
When is an electrostatic precipitator the better choice?
When the dust has favourable electrical resistivity, the gas is already cool, no gas-phase removal is required, and an ESP is already installed and healthy. Above 260°C with high-resistivity dust or a NOx permit, ceramic filtration is usually the smaller and simpler answer.
What does a flue gas filtration system cost to operate?
Operating cost is dominated by fan power against 900–1,500 Pa system resistance, compressed air for pulse-jet cleaning, and sorbent consumption where acid gases require it. Element replacement is a planned five-plus-year item covered by warranty, not an annual outage.
Specifying a Project?
Flue gas filtration above the fabric limit is decided by four numbers: temperature profile, dust loading, gas chemistry and moisture. Send us those four — a gas analysis and a flow rate are enough to start — and our engineers will return an element count, a pressure-drop budget and an honest suitability assessment, including the cases where ceramic is not the right answer. Contact the engineering team — we reply within one working day.
Related Terms: Off-Gas Filters, ESP and Gas-Phase Filtration
An off gas filter in metallurgical and kiln service is the same duty as flue gas filtration: removing dust and acid gases from hot process exhaust before the stack. An electrostatic flue gas filter (ESP) handles large volumes but struggles with high-resistivity dust and cannot be maintained in-house — see the technology comparison above. If you are asking what is gas phase filtration, or how to filter gas at high temperature: it is the separation of solid particles from a gas stream, and above 260°C the practical answer is a rigid ceramic fiber element rather than any textile medium. Typical hot gases examples within our scope: boiler flue gas, kiln off-gas, furnace exhaust and waste-to-energy combustion gas.