AMC 케미컬 여과 하우징 - 여과 설비 | Baisheng Tech
품번amc-chemical-filtration-equipment여과 설비케미컬 여과 설비
여과 설비

AMC 케미컬 여과 하우징

제품 개요

Baisheng의 AMC 케미컬 여과 하우징은 케미컬 여재, 전후단 미립자 필터, 송풍기를 하나의 정비 가능한 케이싱에 통합한 기체상 오염물질 제거 설비입니다. 처리 대상은 HEPA가 잡지 못하는 분자급 오염물질, 즉 산, 염기, 응축물, 도판트, 일반 VOC입니다. 전 시리즈는 여섯 가지 기종을 아우릅니다. 실내 순환용 BS-APS, 외기 양압 급기용 BS-PPS, 덕트에 연결하는 BS-SAH 측면 인출식 케이싱, 고농도를 처리하는 BS-DBS 딥베드 스크러버, 한 단으로 끝내는 BS-HDBS, 점 오염원 국소 배기용 BS-DS 드럼 스크러버입니다. 풍량은 단일 약액조 배기의 170 CMH부터 MAU 주 덕트의 68,000 CMH까지 대응 기종이 있습니다. 케이싱은 용융아연도금 강판 또는 SUS304/316을 쓰고 이음매를 전부 용접합니다. 전후단 필터와 케미컬 여재 모두 측면 도어 설계라 덕트를 뜯지 않은 상태로 교체할 수 있습니다. 케미컬 단을 가로지르는 차압계가 기본 사양이며, 전단 필터 막힘인지 여재 포화인지 판독하는 데 씁니다. 여재 구성, 케이싱 재질, 플랜지 형식, 반면 배치는 모두 현장 조건에 맞춰 제작합니다. 아래 선정 가이드가 네 단계를 설명합니다.

제품 특성

►**Target contaminants**: acids (HCl, HF, SOx, NOx), bases (NH₃, amines), condensables (BHT, NMP, DOP), dopants (AsH₃, B₂H₆, BF₃), general VOCs ►**Airflow range**: 170 – 68,000 CMH (by model — see the selection guide below) ►**Enclosure material**: galvanised steel / SUS304 / SUS316, fully welded seams, no exposed threads inside ►**Chemical stage**: impregnated activated carbon, KMnO₄-treated alumina, blended beds; stages can be placed in series or layered ►**Particulate filters**: pre-filter G4/MERV 6, after-filter F8/MERV 14 (upgradable to HEPA H13/H14) ►**Servicing**: side-access door changeout, no ductwork removal; ΔP gauge across the chemical stage as standard ►**Power**: 380/460V three phase (BS-DS is 380V/3Ø/50Hz)

Six Families at a Glance

FamilyNameAirflow arrangementAirflow range CMH
BS-APSRecirculating air purifierIndoor recirculation850 – 6,800
BS-PPSPositive pressurization unitOnce-through outside air850 – 6,860
BS-SAHSide access housingIn-duct section850 – 68,000
BS-DBSDeep bed scrubberIn-duct or exhaust side510 – 18,350
BS-HDBSHigh deep bed scrubberExhaust side476 – 8,840
BS-DSDrum scrubberLocal point extraction170 – 1,700
견적 문의

Email:sales@baisheng-tech.com

전화+886-2-2598-1958

상세 설명

What a Chemical Filter Housing Handles

HEPA and ULPA filters reach 99.97% or better at the most penetrating particle size of 0.1–0.3 μm. Gaseous molecules are another matter entirely: HCl has a kinetic diameter of about 0.3 nm and NH₃ about 0.26 nm, three orders of magnitude below the MPPS. To the filter they effectively do not exist, and they pass straight through. In the semiconductor industry these molecular contaminants are collectively called AMC (Airborne Molecular Contamination). What they cause is not particle defects but photoresist T-topping, metal line corrosion, wafer surface hazing and dopant concentration drift — the class of problem where no particles can be found yet yield falls. The only way to remove molecules is adsorption: the molecule has to stay in the media pore long enough to be fixed by physisorption, chemical reaction or oxidation. A chemical filter housing is that requirement engineered: chemical media, the particulate filters that protect it, and a fan able to overcome all three stages, integrated into an enclosure whose media can be replaced on a schedule.

Inside a Chemical Filter Housing: Three Stages

Air passes the pre-filter, then the chemical media, then the after-filter, before the fan pushes it out

1Pre-filterG4 / MERV 6Stops dust and fibresKeeps dust from sealing thechemical media pores2Chemical mediaImpregnated carbon /treated aluminaAdsorbs acids, bases,VOCs, dopantsThe removal stage —residence time sets theefficiency3After-filterF8 / MERV 14 (HEPAoptional)Stops carbon fines shed bythe mediaKeeps carbon fines out ofthe cleanroomContaminated air inFanMust overcome all three stagesClean air outΔPΔP gauge spans the chemical stageRising ΔP = pre-filter loading; flat ΔP but rising outlet concentration = media saturatedSide-access doors (change without shutdown)

The chemical media stage is the only one that trades time for efficiency — particulate filters intercept, chemical media adsorbs, and a molecule has to stay inside the pore long enough to be captured. The parameter to lock down during selection is therefore residence time, not media weight.

The two particulate stages are often treated as supporting cast, but drop either one and the chemical media's life is cut short. If the pre-filter lets dust through, that dust seals the pore openings of the activated carbon and the media fails before it is ever loaded. Omit the after-filter and carbon fines abraded off the media by the airstream go straight into the cleanroom, turning the chemical filter into a particle source.

Sorting the Six Families

Cut first on the airflow arrangement — where the air comes from and where it goes after treatment. Cut second on airflow. Those two cuts usually leave one or two options.

Airflow, Residence Time and Typical Application

Cut first on where the air comes from and where it goes, then on airflow — those two cuts usually leave one or two options

ModelAirflow arrangementAirflow rangeMedia depth / residence timeClean total ΔPTypical application
BS-APS
Recirculating air purifier
Indoor recirculation
850–6,800 CMH
(500–4,000 CFM)
2 passes in series / 0.24 sapprox. 1,120 PaLower AMC inside the cleanroom; retrofit into existing plants
BS-PPS
Positive pressurization unit
Once-through outside air
850–6,860 CMH
(500–4,040 CFM)
2 passes in series / 0.24 sapprox. 1,120 PaHold room positive pressure; scrub outside air before it enters
BS-SAH
Side access housing
In-duct section
850–68,000 CMH
(500–40,000 CFM)
12″/18″ modules / 0.06–0.19 s350–780 PaMounted on MAU/AHU ducting; high airflow, low concentration
BS-DBS
Deep bed scrubber
In-duct or exhaust side
510–18,350 CMH
(300–10,800 CFM)
12″ deep bed ×1–3 / 0.8–2.4 s850–2,025 Pa (1–2 beds)Process exhaust, high acid/base loading, high removal required
BS-HDBS
High deep bed scrubber
Exhaust side
476–8,840 CMH
(280–5,200 CFM)
Extended bed height / deepest configuration2,100–2,500 PaSingle high-concentration point needing one-pass treatment
BS-DS
Drum scrubber
Local point extraction
170–1,700 CMH
(100–1,000 CFM)
0.14–1.10 m³ media drumDepends on mediaChemical baths, local exhaust points, temporary treatment

Residence time is the column most often skipped and the one that most decides removal efficiency. At the same 3,400 CMH, a side-access panel module gives only 0.06 s while a single-bed deep bed scrubber gives 0.8 s — more than tenfold apart, covering completely different concentration ranges. Low concentration with high airflow goes to modules; high concentration with low airflow goes to deep beds.

How to Select

Four Selection Steps — In This Order

Arrangement → airflow → media and residence time → pressure drop and fan; each step feeds the next

1Fix the arrangementWhere does the air comefrom, and where does it go after treatment?Number to walk away withRecirculation / makeup air /in-duct / exhaust scrubbingCost of skippingWrong model family entirely;ducting has to be redone2Fix the airflowLowering concentration, orholding positive pressure?Number to walk away withAir changes per hour ormakeup volume → CMHCost of skippingToo little and concentrationnever drops; too much and youburn power3Fix media and residence timeWhich molecules, and atwhat inlet concentration?Number to walk away withMedia type + bed depth →residence time (seconds)Cost of skippingRemoval falls short, or medialife is too short to bepractical4Fix ΔP and the fanCan the fan push throughall three stages combined?Number to walk away withClean and final total ΔP →fan static pressure and motorkWCost of skippingAirflow drops below design, orthe motor runs overloadedΔP does not clear → go back and change bed depth or model

The usual derailment is jumping from step 2 to step 4: the model gets picked to suit existing ducting, and only then does it turn out residence time is short. Deepening the media is the only fix, pressure drop climbs, and now the fan has to be reselected and the power feed re-run. Get the residence time in step 3 right and the fan in step 4 is chosen correctly the first time.

Step 1: Fix the airflow arrangement

- **Indoor recirculation (BS-APS)** — the unit sits inside the cleanroom or process area, drawing room air and returning it treated to the same space. It leaves outside air and the room pressure balance untouched, making it the fastest remedy when an existing plant finds AMC out of specification. The limit is that it dilutes rather than blocks: with a continuous indoor source, concentration settles at an equilibrium. - **Once-through positive pressurization (BS-PPS)** — treats outside air and supplies it one way into the room while holding positive pressure. Suited to sites where the outside air itself carries acids or bases (near chemical plants, coastal, urban), keeping contamination outside the door. This is the only arrangement that genuinely lowers the concentration entering the room. - **In-duct section (BS-SAH)** — a housing plus fan, in series on the MAU/AHU supply header. One unit covers the whole plant at the lowest cost per unit airflow; the trade-offs are the duct space required and a single shared media set for the whole plant, so locally high-concentration areas still need separate treatment. - **Exhaust-side scrubbing (BS-DBS / BS-HDBS / BS-DS)** — installed on the process exhaust side, handling gas orders of magnitude more concentrated than room air. Here the goal is not indoor air quality but emission compliance and equipment corrosion protection.

Step 2: Fix the airflow

Three methods for three purposes; using the wrong one is off by several times: - **Air changes method** (recirculation): airflow = room volume × air changes per hour. AMC control commonly takes 4–10 ACH; strict litho areas can exceed 15 ACH. - **Dilution method** (known source): airflow = emission rate ÷ (target concentration − inlet concentration). This is the only method that answers how far concentration will actually fall for a given airflow, provided the emission rate can be measured. - **Makeup volume method** (positive pressurization): airflow = room leakage + process exhaust + positive-pressure margin. In practice the margin is commonly 10–15% of the total. Once calculated, check the airflow back against the model's design face velocity range — forcing a large airflow into a small housing leaves residence time short.

Step 3: Fix media and residence time

First identify which class of molecule has to go. Acids and bases rely on chemisorption, VOCs and condensables on physisorption, dopants on oxidation; the three mechanisms are not interchangeable.

Contaminant Class → Media Configuration → Suggested Model

Split by the four SEMI F21 classes; each adsorbs by a different mechanism, so the media are not interchangeable

ClassCommon speciesMedia configurationAdsorption mechanismSuggested model
Acids MAHCl, HF, H₂SO₄, NOx, SOxAlkali-impregnated carbon (KOH / K₂CO₃)Chemisorption: neutralised, then fixed on the carbon surfaceBS-APS / BS-PPS / BS-SAH
Bases MBNH₃, amines, NMPAcid-impregnated carbon (H₃PO₄ / citric acid)Chemisorption: forms a salt with the acidic functional groupBS-APS / BS-PPS / BS-SAH
Condensables MCBHT, NMP, DOP (boiling point >150°C)High surface area coconut shell carbonPhysisorption: pore structure and van der Waals forcesBS-SAH / BS-DBS
Dopants MDAsH₃, B₂H₆, BF₃, TEPKMnO₄-treated alumina + blended bedOxidation: oxidised first, then fixed — irreversibleBS-DBS / BS-HDBS
General VOCToluene, acetone, IPA, ethyl acetateNon-impregnated carbon (granular or honeycomb)Physisorption: recovery worth considering at high concentrationBS-SAH / BS-DBS / BS-DS

Real plants almost never have just one class of contaminant, so the chemical stage is usually built as a blended bed (different media layered) or several stages in series. Watch out for one constraint: acidic and alkaline media placed in the same layer neutralise each other and both go dead, so they must be separated into different layers or stages — the limitation most often overlooked when configuring.

Once media is chosen, residence time sets the removal efficiency. This is the step most often skipped and the one that most directly decides success:

Face Velocity, Residence Time and ΔP: Change One and All Three Move

At the same airflow, raising face velocity shrinks the housing — at the cost of shorter residence time and lower removal

ConfigurationMedia depthFace velocityResidence timeClean ΔPSuited concentrationRelative residence time
BS-SAH PM-1818″ (457 mm)2.50 m/s (500 FPM)0.06 s450 PaLow concentration, high airflow
BS-SAH PM-1212″ (305 mm)1.25 m/s (250 FPM)0.12 s777 PaLow concentration
BS-SAH CCF-18/2418″/24″ canister2.50 m/s (500 FPM)0.192 s350–400 PaLow to medium concentration
BS-APS / BS-PPS2 passes in series1.27 m/s (250 FPM)0.24 sapprox. 1,120 PaMedium concentration, indoor recirculation
BS-DBS single bed12″ deep bed ×10.38 m/s (75 FPM)0.8 s850–1,275 PaHigh concentration
BS-DBS triple bed12″ deep bed ×30.38 m/s (75 FPM)2.4 sover 2,025 PaVery high concentration, process exhaust

For deep beds, residence time = bed depth ÷ face velocity (a 12″ bed at 0.381 m/s gives 0.8 s). For panel and canister modules, what counts is the actual media thickness rather than module depth, so a 12″ module has far less residence time than a 12″ deep bed. There are only two ways to lengthen residence time: deepen the bed (bigger housing, higher ΔP) or lower the face velocity (more face area at the same airflow, so again a bigger housing). No chemical filter housing is simultaneously small, deep and low-ΔP — selection is picking an acceptable trade among the three.

The practical boundaries run roughly like this: inlet concentration in the ppb range goes to modules (BS-SAH, 0.06–0.19 s is enough); at the ppm range consider deep beds (BS-DBS, 0.8 s and up); process exhaust in the tens of ppm goes straight to multiple deep beds or BS-HDBS.

Step 4: Fix ΔP and the fan

Total pressure drop is the sum of three stages, and it climbs steadily as the media loads. Select the fan against the final pressure drop rather than the clean value, or airflow will fall below design partway through the filter's life. The changeout ΔP is generally set at 1.5–2 times the clean value, and the fan static pressure must still deliver design airflow at that point. If this step does not clear, go back to step 3 and change bed depth or model — do not simply fit a larger motor, which only raises power consumption and noise together.

Specifications

BS-APS Recirculating Air Purifier

ModelAirflow CMHAirflow CFMMotor kW (HP)Dimensions H×W×D mmNet weight kg
BS-APS-500H8505000.75 (1.0)719 × 602 × 2,438272
BS-APS-1000H1,6991,0000.75 (1.0)719 × 602 × 2,438295
BS-APS-2000H3,3982,0001.5 (2.0)719 × 1,204 × 2,438544
BS-APS-4000H6,7964,0003.7 (5.0)1,321 × 1,204 × 2,7941,043
BS-APS-500V8505000.75 (1.0)2,159 × 686 × 686272
BS-APS-1000V1,6991,0000.75 (1.0)2,159 × 686 × 686363
BS-APS-2000V3,3982,0001.5 (2.0)2,159 × 1,397 × 686590
BS-APS-4000V6,7964,0003.7 (5.0)2,667 × 1,397 × 1,206782
H = horizontal, V = vertical. Net weight excludes media. Design face velocity 1.27 m/s (250 FPM), two passes in series, residence time 0.24 s, clean total ΔP approx. 1,120 Pa.

BS-PPS Positive Pressurization Unit

ModelAirflow CMHAirflow CFMMotor kW (HP)Dimensions H×W×D mmNet weight kg
BS-PPS-250H8505000.75 (1.0)719 × 602 × 2,616227
BS-PPS-500H1,7411,0250.75 (1.0)719 × 602 × 2,616238
BS-PPS-1000H3,5002,0601.5 (2.0)719 × 1,203 × 2,616365
BS-PPS-2000H6,8644,0403.7 (5.0)1,321 × 1,203 × 3,048500
BS-PPS-250V8505000.75 (1.0)2,159 × 686 × 686227
BS-PPS-500V1,7411,0250.75 (1.0)2,159 × 686 × 686238
BS-PPS-1000V3,5002,0601.5 (2.0)2,159 × 1,397 × 686365
BS-PPS-2000V6,8644,0403.7 (5.0)2,667 × 1,397 × 1,206455
Model numbers are module reference values; actual airflow is per this table. Clean total ΔP approx. 1,120 Pa.

BS-SAH Side Access Housing (by module configuration)

Module configurationAirflow range CMHFace velocityResidence timeClean total ΔPMotor range kW
PM-12 (12″ panel)850 – 34,0001.25 m/s0.12 s777 Pa0.75 – 22
PM-18 (18″ panel)1,700 – 68,0002.50 m/s0.06 s450 Pa0.75 – 37
CCF-18 (18″ canister)1,700 – 68,0002.50 m/s0.192 s400 Pa0.75 – 37
CCF-24 (24″ canister)1,700 – 68,0002.50 m/s0.192 s350 Pa0.75 – 37
Power 380/460V three phase, two-stage module configuration. Overall dimensions depend on module count and airflow; a dimensional drawing is supplied with the quotation.

BS-DBS Deep Bed Scrubber

ItemSpecification
Model rangeBS-DBS-202 to BS-DBS-1212
Airflow range510 – 18,351 CMH (300 – 10,800 CFM)
Media volume142 – 4,248 L (single 12″ deep bed)
Face velocity0.381 m/s (75 FPM)
Residence time0.8 s per 12″ deep bed, stackable 1 – 3 beds
Clean total ΔPsingle bed 850 – 1,275 Pa; two beds 1,175 – 2,025 Pa
Particulate filterspre-filter MERV 6/G4, interstage MERV 6/G4, final MERV 14/F8
Motor range0.75 – 15 kW (1.0 – 20.0 HP)
Dimensional rangeheight 864 – 4,013, width 660 – 3,708, length 2,642 – 3,785 mm
Weight range795 – 3,791 kg

BS-HDBS High Deep Bed Scrubber

ItemSpecification
Size codes26 / 33 / 39 / 44 / 54 / 62 / 73 / 82 / 90 / 100
Airflow range476 – 8,840 CMH (280 – 5,200 CFM)
Media volume0.39 – 5.88 ft³ (by enclosure size)
Unit pressure dropapprox. 2,100 – 2,500 Pa (8.5″ – 10.0″ WC)
Motor range1.5 – 11 kW (2.0 – 15.0 HP)
Dimensional rangewidth 660 – 2,083, length 1,422 – 4,829, height 1,778 – 2,540 mm
Weight range490 – 2,258 kg
Discharge typehorizontal discharge / vertical discharge

BS-DS Drum Scrubber

ModelAirflow CMHVessel dia. mmVessel height mmInletMedia volume m³Motor kW
BS-DS-1001706001,220DN1400.140.37
BS-DS-3005107601,525DN1600.281.50
BS-DS-5008509151,525DN2000.481.50
BS-DS-7501,2751,1501,220DN2000.761.50
BS-DS-10001,7001,3201,525DN2001.102.24
Power 380V/3Ø/50Hz.

Enclosure and Appearance

The horizontal model's side-access doors let the media be drawn out as a whole section without dismantling ducting: AMC chemical filter housing, horizontal model with side-access door open showing the internal media stage The door panel carries the ΔP gauge spanning the chemical media stage and an airflow direction marker: AMC chemical filter housing, horizontal model front view with ΔP gauge and airflow direction marker Vertical models have a small footprint, suited to placement beside a tool or against a wall. Left is the standard pushbutton panel, right the touchscreen panel with ΔP display: AMC chemical filter housing, two panel configurations of the vertical model compared A vertical model installed on site, with castors on the base for repositioning: AMC chemical filter housing, vertical model installed on site with ΔP gauges and castor base

Installation and Maintenance Notes

**Installation** - Vertical models need service clearance all round: 800 mm or more at the front for the side-access door to swing fully open, and 300 mm or more at each side and the rear. - Horizontal models need a straight duct run before and after the connection (1.5 duct diameters or more is recommended), so an elbow butted against the housing does not skew the airflow and saturate one side of the media first. - A flexible connector (canvas coupling) between duct and housing is recommended to isolate fan vibration. - For exhaust-side models (BS-DBS/BS-HDBS) handling acidic gas, confirm the corrosion rating of the ducting and exhaust outlet as well — do not corrosion-protect the enclosure alone. **Maintenance** - The ΔP gauge is the only day-to-day indicator, but the two failure signals differ: **rising ΔP** means the pre-filter is dust-loaded and due for change; **flat ΔP with rising outlet concentration** means the chemical media is saturated. Media saturation does not show up on ΔP at all, and this is the single most commonly misread point. - Chemical media life cannot be inferred from a calendar; it depends on inlet concentration and airflow. Determining changeout timing accurately requires periodic outlet concentration sampling, or sending media out to measure remaining adsorption capacity. - Pre-filters are normally changed far more often than the chemical media (months against years), so specifying a higher-grade pre-filter is poor economics — the pre-filter's job is to be sacrificed cheaply. - When changing chemical media, mind the layer order: acidic and alkaline media must not share a layer, as they neutralise each other and both go dead.

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