A zirconia ceramic membrane tube is a multichannel filtration element for liquid crossflow microfiltration or ultrafiltration. The element consists of a porous ceramic support with one or more selective membrane layers. Feed liquid flows through parallel channels; the membrane retains target solids or solutes while permeate passes through the element wall.
The element specification identifies the porous support, transition/selective layers and end treatment separately. The supply item is a membrane element; housing and system interfaces are defined for the project.
Read Each Membrane Measure for Its Own Purpose
| Measure | Unit or Basis | Selection Use |
|---|---|---|
| Feed-channel geometry | mm; shape defined on the drawing | Flow passage, solids handling and cleaning access |
| MF pore specification | µm; defined method | Candidate separation scale for the feed |
| UF molecular-weight cut-off (MWCO) | kDa; specified test basis | Candidate retention of target components |
| Water permeance | L/(m²·h·bar), with temperature and test conditions | Pressure-normalized water-test baseline |
| Process-feed flux | L/(m²·h), with feed and operating conditions | Throughput evaluation using the agreed effective area |
Keep channel geometry, pore specification and MWCO as separate requirements. Assess production duty with representative-feed performance, active membrane area and cleaning recovery.
Available Zirconia Membrane Tube Configurations
| Zirconia Ceramic Membrane Filter Tube | ||||||||
| Item No. | Bore Quantities | Picture | Bore Diameter (mm) | Membrane Area | Size | Micro filter | Super filter | Fine ultrafiltration |
| AT-YHG-MG1001 | 19 |
|
3.5mm | 0.05 m2 | Outer Diameter:25mm,Length :250mm | 0.14μm,0.2μm,0.45μm,0.8μm,1.4μm | 15KD,50 KD,150KD,300KD | 1 KD,3KD,5KD,8KD |
| AT-YHG-MG1002 | 23 |
|
3.5mm | |||||
| AT-YHG-MG1003 | 7 |
|
6mm | 0.16m2 | ||||
| AT-YHG-MG1004 | 8 |
|
6mm | |||||
| AT-YHG-MG1005 | 19 |
|
3.5mm | |||||
| AT-YHG-MG1006 | 23 |
|
3.5mm | |||||
| AT-YHG-MG1007 | 49 |
|
2.5mm | |||||
| AT-YHG-MG1008 | 19 |
|
6mm | 0.35m2 | ||||
| AT-YHG-MG1009 | 25 |
|
5.5mm | |||||
| AT-YHG-MG1010 | 37 |
|
3.6mm | |||||
Download the Product Catalogue
Choose a Separation Grade and Channel Layout
Match the separation grade to the component you want to retain or recover. Compare product recovery, fouling and cleaning recovery alongside the nominal pore size or cut-off.
Available Separation References
Microfiltration (MF) pore sizes: 0.14 / 0.2 / 0.45 / 0.8 / 1.4 µm
Match the listed pore reference to particle distribution, solids and the target separation.
Ultrafiltration (UF) molecular-weight cut-offs: 1 / 3 / 5 / 8 / 15 / 50 / 150 / 300 kDa
Match the cut-off and test basis to the target components and required retention.
These discrete values are enquiry references. The proposed membrane layer, separation grade and test basis are selected for the feed; each channel layout is specified separately.
Evaluate Membrane Performance for Your Feed
Membrane performance is defined by permeate flux, rejection of target components, and flux recovery after cleaning. These measures depend on feed composition, crossflow velocity, transmembrane pressure, temperature, and the selected membrane grade.
| Performance Parameter | What It Tells You |
|---|---|
| Permeate flux | Throughput per unit area and time under defined feed, TMP, temperature and crossflow conditions |
| Rejection / Retention | Percentage of target solids or solutes retained by the membrane, verified with representative feed |
| Fouling resistance | Flux decline rate and recovery after backwash or chemical cleaning under process conditions |
| Operating life | Cycles to acceptable flux decline, retention loss, or physical damage under defined duty |
Test the proposed membrane grade with your actual feed or a close surrogate. Water permeability is a baseline check; process performance must be verified under production conditions.
Selection Comparison: When to Choose a Zirconia Membrane
Select the membrane route by separation requirement, chemical compatibility, operating conditions and economics. Zirconia ceramic membranes are one option among several; the right choice depends on your specific duty.
| Membrane Route | What to Compare for Selection |
|---|---|
| Zirconia ceramic membrane | Specified selective layer, support and end interfaces under the proposed feed and cleaning duty |
| Alumina ceramic membrane | Layer material, pore options and mechanical strength for the same separation target and cleaning protocol |
| Silicon carbide (SiC) membrane | Thermal conductivity, abrasion resistance and module format under high-solids or thermal-cycling conditions |
| Polymeric membrane | Separation quality, module format, chemical/cleaning fit and replacement economics for the process |
Use the ceramic membrane range for a broader material and format comparison.
Match the Element to the Housing
| Fit Decision | Dimensions or Features to Match |
|---|---|
| Feed passages | Channel shape and size; solids handling and cleaning access |
| Element envelope | OD and overall length for physical fit; active length and effective area for filtration duty |
| End interfaces | End profiles, sealing zones, insertion depth and critical tolerances |
Packaging for Zirconia Membrane Tubes
Zirconia Ceramic Membrane Tube is securely packed in foam-lined wooden crates to prevent damage during international transit. Each tube is individually wrapped with shock-resistant cushioning to avoid surface scratches or impact stress. Custom-fit compartments ensure stability and separation throughout handling and shipping.





