{"id":754,"date":"2026-09-28T09:10:41","date_gmt":"2026-09-28T01:10:41","guid":{"rendered":"https:\/\/anchor-filter.com\/ceramic-filter-selection-guide\/"},"modified":"2026-10-07T12:23:02","modified_gmt":"2026-10-07T04:23:02","slug":"%ec%84%b8%eb%9d%bc%eb%af%b9-%ed%95%84%ed%84%b0-%ec%84%a0%ed%83%9d-%ea%b0%80%ec%9d%b4%eb%93%9c","status":"publish","type":"post","link":"https:\/\/anchor-filter.com\/ko\/ceramic-filter-selection-guide\/","title":{"rendered":"\uc138\ub77c\ubbf9 \ud544\ud130 \uc5d8\ub9ac\uba3c\ud2b8 \uc120\ud0dd \uac00\uc774\ub4dc: \ud06c\uae30, \uc555\ub825 \uac15\ud558 \ubc0f \ud654\ud559\uc801 \ud2b9\uc131"},"content":{"rendered":"

Good ceramic filter element selection<\/strong> is three calculations and one chemistry check, and most specifications get the order wrong: they pick a size, then discover the gas does not fit the material. This guide works the other way round. Read the stream first, then convert gas volume into element count using the standard \u03c6150 \u00d7 \u03c6110 \u00d7 3,000 mm geometry, then build the pressure-drop budget against your fan, then screen the chemistry against the four boundaries that decide whether the element survives. Every number below is one you can put into an enquiry.<\/p>\n

\"Rows<\/figure>\n

Step 1: Read the gas stream before the catalogue<\/h2>\n

Four stream properties drive everything else: temperature profile, dust loading, moisture and acid or alkali content. Record the continuous temperature, the peak and how long peaks last, because a ceramic element rated for 600\u00b0C continuous and 1000\u00b0C peak still needs a controlled ramp to avoid thermal shock. Record dust loading in g\/m\u00b3 and the particle size distribution, since fine sticky dust pushes you to the lower end of the velocity band. Record moisture, because above 20% by volume capillary condensation will mask itself as blinding. And record the species that matter chemically \u2014 HF, H\u2083PO\u2084, free alkali and SO\u2082.<\/p>\n

Step 2: Geometry, area and element count<\/h2>\n

What the standard element gives you<\/h3>\n

The standard candle is \u03c6150 \u00d7 \u03c6110 \u00d7 3,000 mm with a 20 mm wall and porosity >80%. Manufacturing tolerance is OD \u00b12 mm and length \u00b120 mm, and both belong on your purchase order, because the hold-down and tubesheet design depend on them. The porosity figure is not a curiosity: above 80% open pore is what allows the element to hold 300 Pa at 1 m\/min face velocity (clean) while still carrying its own weight and the pulse load at temperature. Filtration area comes from the outer surface \u2014 roughly 1.41 m\u00b2 per standard element \u2014 and that is the number you divide into your gas volume. Confirm against the published element dimensions<\/a> before you commit a layout.<\/p>\n

Converting gas volume into an element count<\/h3>\n

Design the face velocity at 2\u20135 cm\/s, which is about 1.2\u20133.0 m\u00b3\/min per m\u00b2. Divide the actual gas volume at operating temperature by the chosen velocity to get filter area, then divide by 1.41 m\u00b2 to get the element count. The table below shows the spread for a 60,000 m\u00b3\/h stream; the point is how much vessel size you trade for pressure drop and, in catalytic duty, for residence time inside the wall.<\/p>\n

Always round the count up, then lay it out on the tubesheet before you accept it. A count that is correct on paper can still fail on pitch: elements need enough spacing for the pulse jet to travel to the closed end and for one person to lift a candle out without touching its neighbours. Check the peak, not just the average, gas volume as well \u2014 if a process upset doubles the flow for ten minutes each cycle, size for the upset or specify a bypass, because the element will not forgive it.<\/p>\n

Handling weight is part of the same calculation. A standard non-catalytic candle weighs about 7.5 kg, and the catalytic version about 8.5 \u00b1 0.5 kg, which sets the lifting method, the packing specification and the number of people you need for a changeout. Ask for elements packed with the seal faces protected; most transport damage arrives at the end of the candle, not in the wall.<\/p>\n\n\n\n\n\n\n\n\n\n
Design velocity<\/th>\nEquivalent loading<\/th>\nFilter area needed<\/th>\nApprox. elements (60,000 m\u00b3\/h)<\/th>\n<\/tr>\n<\/thead>\n
2.0 cm\/s<\/td>\n1.2 m\u00b3\/min per m\u00b2<\/td>\n833 m\u00b2<\/td>\n590<\/td>\n<\/tr>\n
2.5 cm\/s<\/td>\n1.5 m\u00b3\/min per m\u00b2<\/td>\n667 m\u00b2<\/td>\n472<\/td>\n<\/tr>\n
3.0 cm\/s<\/td>\n1.8 m\u00b3\/min per m\u00b2<\/td>\n556 m\u00b2<\/td>\n393<\/td>\n<\/tr>\n
4.0 cm\/s<\/td>\n2.4 m\u00b3\/min per m\u00b2<\/td>\n417 m\u00b2<\/td>\n295<\/td>\n<\/tr>\n
5.0 cm\/s<\/td>\n3.0 m\u00b3\/min per m\u00b2<\/td>\n333 m\u00b2<\/td>\n236<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n
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Rule of thumb:<\/strong> choose the lower half of the band for fine or sticky dust, for catalytic duty where residence time matters, and whenever your dust loading is high enough that the cake, not the element, will dominate resistance. Choose the upper half only when vessel footprint is the binding constraint.<\/p>\n<\/div>\n

\"Dimensioned<\/figure>\n

Step 3: Build the pressure-drop budget<\/h2>\n

Do not hand the fan vendor a single number. A clean element is 300 Pa at 1 m\/min face velocity (clean); the complete system settles between 900 and 1,500 Pa, with 900\u20131,300 Pa typical in glass furnace duty. Split the budget so that when resistance drifts you know which contribution moved. Remember that the clean figure is quoted at 1 m\/min and scales with velocity, so a vessel running near the top of the band starts higher before any dust arrives.<\/p>\n\n\n\n\n\n\n\n\n\n
Contribution<\/th>\nDesign value<\/th>\nComment<\/th>\n<\/tr>\n<\/thead>\n
Clean element at reference velocity<\/td>\n300 Pa at 1 m\/min face velocity (clean)<\/td>\nScales with the chosen face velocity<\/td>\n<\/tr>\n
Dust cake and residual layer<\/td>\n250\u2013500 Pa<\/td>\nSet by cleaning frequency and dust stickiness<\/td>\n<\/tr>\n
Tubesheet, plenum and element support<\/td>\n150\u2013300 Pa<\/td>\nA layout problem shows up here first<\/td>\n<\/tr>\n
Ducting, damper and hopper<\/td>\n200\u2013400 Pa<\/td>\nUsually inherited from the existing plant<\/td>\n<\/tr>\n
Total system resistance<\/td>\n900\u20131,500 Pa (900\u20131,300 Pa glass furnace)<\/td>\nConfirm against the ID fan curve with margin<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n

Then decide how you will read the trend, because that is what the budget is for. A slow rise in the floor after cleaning means the cake is not releasing, which points at moisture, at ABS, or at a pulse that is too short. A step change means a broken element or a failed seal. A falling resistance together with rising stack emissions almost always means a sealing or tubesheet problem rather than a media problem, and it is the one condition that spare elements will not fix.<\/p>\n

Step 4: Chemistry \u2014 the boundaries that decide survival<\/h2>\n

This is the step that voids warranties when it is skipped. Sustained HF above 5 ppm attacks the fibre bond. Phosphoric acid (H\u2083PO\u2084) mist is excluded from the duty outright. Free Na\u2082O or K\u2082O alkali will flux the surface at temperature unless an alkaline sorbent is dosed upstream. Where a catalytic section operates below 280\u00b0C, SO\u2082 must stay under 35 mg\/m\u00b3. Moisture stays below 20% by volume. Each of these is checkable before purchase, and each is far cheaper to fix upstream than to argue about afterwards.<\/p>\n\n\n\n\n\n\n\n\n\n\n
Component<\/th>\nBoundary<\/th>\nWhy it matters<\/th>\n<\/tr>\n<\/thead>\n
HF<\/td>\nBelow 5 ppm sustained<\/td>\nAttacks the fibre bond and shortens element life<\/td>\n<\/tr>\n
H\u2083PO\u2084 mist<\/td>\nExcluded<\/td>\nReacts with the fibre phase; no safe operating band<\/td>\n<\/tr>\n
Na\u2082O \/ K\u2082O<\/td>\nOnly with alkaline sorbent present<\/td>\nFree alkali fluxes the surface at temperature<\/td>\n<\/tr>\n
SO\u2082 below 280\u00b0C<\/td>\nUnder 35 mg\/m\u00b3<\/td>\nBisulphite condensation and catalyst masking<\/td>\n<\/tr>\n
Moisture<\/td>\nBelow 20% by volume<\/td>\nCapillary condensation reads as blinding<\/td>\n<\/tr>\n
ABS deposits<\/td>\nRegenerate at 350\u00b0C for 12 h periodically<\/td>\nDecomposes the deposit and restores baseline resistance<\/td>\n<\/tr>\n<\/tbody>\n<\/table>\n

Get the chemistry confirmed by analysis rather than by process description. A material safety sheet or a design basis from five years ago is not a gas analysis, and the species that cause trouble \u2014 HF, phosphoric mist, free alkali \u2014 are rarely the ones a process engineer volunteers. Sample at the filter inlet, at operating temperature, and repeat the sample in the worst season, because moisture and acid dew point move with ambient conditions and with fuel or raw-material changes.<\/p>\n

Where ammonia slip is present in the same temperature band, ammonium bisulphite is inevitable rather than optional. Treat it as a maintenance cycle: plan regeneration at 350\u00b0C for 12 hours at an interval set by the slip rate, and log the differential pressure before and after so you can see whether the interval is right.<\/p>\n

Step 5: Temperature and whether you need catalysis<\/h2>\n

If the requirement is filtration only, the non-catalytic ceramic fibre filter elements<\/a> run continuously at 600\u00b0C and survive peaks to 1000\u00b0C, which covers kilns, furnaces and most metallurgical streams without any cooling stage. If the requirement includes NOx or dioxins, the catalytic ceramic fibre filter elements<\/a> work in a 170\u2013300\u00b0C window with the optimum at 220\u2013260\u00b0C: about 90% DeNOx at 200\u00b0C and about 98% at 280\u00b0C with the low-temperature formulation, and dioxin destruction up to 99.5% (TEQ) by selective catalytic oxidation. Dust collection stays above 99.9% in either case. The mistake to avoid is specifying catalytic elements for a stream that only enters the window during upsets.<\/p>\n

\"Top<\/figure>\n

Step 6: Cleaning air, life and warranty<\/h2>\n

Cleaning air and differential pressure control<\/h3>\n

Specify 0.4\u20130.7 MPa of dry, oil-free compressed air, a pulse duration of 0.1\u20130.15 s, and differential-pressure triggering rather than a fixed timer. The pulse is short because the element is rigid: it releases the cake by shock, not by flexing. Size the receiver so a full cleaning sequence completes without the header falling below 0.4 MPa, and make sure the triggering transmitter is on the clean side with a logged trend, because it is both the control input and the condition monitor for the next five years.<\/p>\n

Life, warranty and spares<\/h3>\n

Service life is more than 5 years, backed by a 5-year written warranty, so the commercial question is not replacement frequency but what the warranty actually measures: document the clean baseline at commissioning and keep it with the warranty record. Hold enough spare elements to replace a row, since individual candles are replaceable and the realistic loss mechanism is handling damage rather than wear. Anchor Filter has been manufacturing these elements since 2019 and has delivered 40+ projects; the inspection routine we apply before shipment is described on our quality and inspection page<\/a>.<\/p>\n

Frequently asked questions<\/h2>\n

How do I convert my gas volume into a number of ceramic filter elements?<\/h3>\n

Divide the operating gas volume by your design velocity of 1.2\u20133.0 m\u00b3\/min per m\u00b2 to get filter area, then divide by the outer area of one standard \u03c6150 \u00d7 \u03c6110 \u00d7 3,000 mm element, about 1.41 m\u00b2. For 60,000 m\u00b3\/h at 1.5 m\u00b3\/min per m\u00b2 that is roughly 667 m\u00b2, or about 472 elements. Always round up and then check the count against the tubesheet pitch.<\/p>\n

What clean pressure drop should go into the fan datasheet?<\/h3>\n

Quote 300 Pa at 1 m\/min face velocity (clean) for the element and 900\u20131,500 Pa for the complete system including ducting and hopper, with 900\u20131,300 Pa typical in glass furnace duty. Because the clean figure is referenced to 1 m\/min, scale it to your actual design velocity before adding the rest of the budget, and confirm the fan still has margin at the top of the range.<\/p>\n

Which chemical components disqualify a ceramic element?<\/h3>\n

Sustained HF above 5 ppm, any phosphoric acid mist, and free Na\u2082O or K\u2082O alkali without an alkaline sorbent upstream. In catalytic duty below 280\u00b0C, SO\u2082 above 35 mg\/m\u00b3 and moisture above 20% by volume are also outside the envelope. All four are fixable upstream with sorbent dosing, gas conditioning or better insulation \u2014 they are not reasons to abandon the technology.<\/p>\n

Catalytic or non-catalytic: how do I choose?<\/h3>\n

Choose on the gas temperature and the permit. Non-catalytic elements handle 600\u00b0C continuously and 1000\u00b0C peak. Catalytic elements only work in the 170\u2013300\u00b0C window, optimum 220\u2013260\u00b0C, but they add about 90% DeNOx at 200\u00b0C, about 98% at 280\u00b0C and dioxin destruction up to 99.5% (TEQ). If your stream cannot hold the window, buy non-catalytic and treat NOx separately.<\/p>\n

What tolerances and inspection items belong on the purchase order?<\/h3>\n

State the geometry as \u03c6150 \u00d7 \u03c6110 \u00d7 3,000 mm with a 20 mm wall and porosity >80%, and the tolerances as OD \u00b12 mm and length \u00b120 mm. Add the clean pressure drop acceptance of 300 Pa at 1 m\/min face velocity (clean), a visual and dimensional check on delivery, and packing that protects the element ends, since most transport damage occurs at the seal face rather than in the wall.<\/p>\n

Send us your gas volume, temperature profile and gas analysis and we will return an element count, a pressure-drop budget and a chemistry screen for your stream \u2014 request a selection calculation<\/a>.<\/p>\n

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Related guides:<\/strong> ceramic filter installation steps<\/a><\/p>\n<\/div>\n<\/div>\n

Need a hot gas filtration solution?<\/strong> Tell us your gas temperature, dust load and flow rate \u2014 our engineers will reply with a sizing suggestion. Contact us<\/a>: sales@anchorgd.com | WhatsApp: +86 135 3986 0818<\/div>\n