For a dairy plant already operating a European ceramic membrane system, replacement rarely starts with a blank sheet. The plant has an installed module, an established cleaning regime, production targets and product-quality specifications that cannot be disrupted. A lower-priced membrane tube is of little value if it requires extensive housing modification, changes the separation result, cleans poorly or creates an unplanned shutdown.
The right question is therefore not simply, “Can another supplier provide a ceramic membrane?” It is: “Can the plant establish a technically validated replacement route that protects product quality, production continuity and long-term spare-part availability?”
JIUWU approaches replacement as an engineering evaluation. The existing membrane, module, operating conditions, feed characteristics and CIP procedure are reviewed together. Where necessary, the customer’s dairy stream is tested before a commercial replacement is recommended.
Membrane replacement is often treated as a maintenance purchase. In reality, it can affect several business risks at the same time.
First, a plant that depends on one membrane brand also depends on that supplier’s delivery schedule, technical response and spare-part policy. If availability becomes uncertain, the consequence may not be limited to a higher purchase price. It can include emergency inventory, delayed maintenance or loss of production flexibility.
Second, membrane performance is connected to the entire process. In dairy applications, the feed may contain proteins, fats, minerals, microorganisms and suspended matter. Changes in membrane pore size, surface properties, channel geometry or operating conditions can influence permeate quality, product recovery, flux decline and cleaning requirements.
Third, the cost of replacement extends beyond the membrane element. Engineering work, housing modification, seals, piping, commissioning, cleaning chemicals, energy and downtime all contribute to the total cost of ownership. Business decision makers need a replacement plan that makes these items visible before approval.
Two ceramic membrane tubes may appear similar while differing in length, outside diameter, channel configuration, sealing position or allowable pressure. The module may also use a specific housing material, connection standard or seal design. These details determine whether the replacement can use the existing housing or requires modification.
Nominal pore size is only one selection parameter. Dairy separation is also affected by feed composition, temperature, viscosity, ionic strength, transmembrane pressure, crossflow velocity and concentration factor. Protein interaction with the membrane surface can influence fouling and selectivity. A replacement should therefore be evaluated using the actual process objective, not a catalogue number alone.
A membrane that reaches the required initial flux but cannot recover after cleaning may create shorter production cycles and more downtime. The replacement study should review the existing CIP sequence, chemicals, concentration, temperature and contact time. Cleaning recovery must be verified under conditions relevant to the plant.
Replacing a complete system at once can increase operational risk. A staged path—document review, laboratory screening, pilot validation and controlled line installation—allows the plant to identify problems earlier and plan the shutdown window.
Purchase price per tube does not show the economic result. Decision makers also need to compare expected replacement frequency, membrane area, stable throughput, energy demand, cleaning consumption, modification cost, lead time and inventory requirements. Project-specific figures require test and operating data; they should not be assumed from a generic brochure.
A robust evaluation should cover four groups of indicators.
Separation performance: required permeate quality, microorganism or particle removal, target-component retention, product recovery and concentration factor.
Operating stability: stable flux, flux decline, transmembrane pressure, crossflow velocity, temperature, batch duration and sensitivity to feed variation.
Cleaning and regeneration: cleaning frequency, chemicals, temperature, contact time, water consumption and flux recovery after CIP.
Economics and implementation: membrane quantity, usable membrane area, power consumption, chemical consumption, housing or piping modification, commissioning time, spare-part lead time and planned inventory.
These indicators provide a decision basis for comparing three possible routes: membrane-tube replacement within the existing housing, replacement of complete modules, or upgrade of the membrane system.
The customer provides the current membrane model, tube and module drawings, photographs, housing dimensions, seal details, connection standard and operating history. If complete drawings are unavailable, critical dimensions can be measured on site or from a removed element.
JIUWU’s tubular ceramic membrane portfolio includes multiple module capacities, selectable lengths, housing materials, seal materials, sealing arrangements and connection standards. Available options in the supplied product documentation include SUS304(L), SUS316(L), titanium, PVC and FRPP housings; EPDM, FKM, silicone rubber, PTFE and FFKM seals; and ISO9001, ISO45001, ISO14001, ISO50001. The final combination must be selected for the actual food-contact, chemical and temperature requirements.
The plant clarifies what the membrane must achieve. Examples include microbial reduction, clarification, separation of larger proteins, pretreatment before downstream ultrafiltration or concentration, and recovery of valuable product from process streams. The supplied JIUWU material identifies dairy as a typical CMVS tubular ceramic membrane application and describes a possible dairy process route involving ceramic microfiltration for microbial removal followed by further membrane steps. The exact process must be confirmed for each plant.
JIUWU’s alumina ceramic membrane range covers microfiltration, ultrafiltration and nanofiltration levels, with 0.01-1 μm candidate pore sizes referenced in the technical manual. The appropriate pore size and configuration are selected through process analysis and, when needed, laboratory testing.
Testing should record permeate quality, retention or recovery, flux decline, transmembrane pressure, temperature and cleaning recovery. JIUWU’s technical methodology treats the test as a small process system rather than an isolated membrane check. It includes pretreatment, filtration, process monitoring, fouling control and cleaning regeneration.
For a replacement decision, the test plan should reproduce the relevant industrial boundaries as closely as practical. Project-specific acceptance criteria—such as target flux, product quality, recovery and cleaning recovery—must be agreed before testing.
After technical validation, the plant can select the least disruptive route:
● replacement membrane tubes for an existing compatible module;
● replacement modules while retaining part of the installed system;
● system modification where hydraulics, controls, cleaning or capacity need improvement; or
● a new ceramic membrane system for expansion or process redesign.
JIUWU system documentation includes functions such as filtration, circulation, online backwash, system rinse, product displacement, wash-water operation, CIP, temperature control and automation. Not every function is required in every dairy project; the configuration should match the plant’s process and cleaning philosophy.
The first value is supply resilience. A qualified alternative source reduces dependence on a single membrane supplier and gives procurement more options for planned inventory and future expansion.
The second value is controlled operational risk. Compatibility review and material testing identify mechanical, separation and cleaning issues before a full line conversion.
The third value is better cost visibility. Instead of comparing tube price alone, the plant can evaluate modification cost, stable capacity, cleaning demand, energy, planned downtime, replacement frequency and lead time as one decision.
The fourth value is a scalable path. The plant may start with one sample, one test, one module or one line and then expand after defined acceptance criteria are achieved.
Actual savings, shutdown reduction and membrane life depend on the installed system and process data.
This evaluation approach may be relevant for:
● plants using imported tubular ceramic membrane elements that require a second source;
● microbial reduction or clarification of milk and dairy process streams;
● separation steps involving larger proteins or suspended components;
● pretreatment before downstream organic membrane concentration or desalting;
● recovery or clarification of dairy by-product streams;
● capacity expansion where the existing supplier’s module or delivery model is restrictive; and
● systems with recurring cleaning, flux or spare-part problems that require a broader upgrade review.
Final suitability must be confirmed from the feed, product target, installed equipment and cleaning conditions.
The supplied JIUWU technical documentation confirms dairy as a typical application for CMVS tubular ceramic membrane modules and provides a technical route covering membrane screening, operating-condition optimisation, extended stability testing, cleaning validation and scale-up.
For this Campaign, no public Russia/CIS dairy case with approved operating data was included in the supplied source set. A publishable case should only be added after the business unit confirms the project, customer disclosure level, original process, reason for replacement, JIUWU scope, operating result and replacement economics.
Please provide as many of the following items as possible:
1. Current membrane brand and model.
2. Tube drawing: length, outside diameter, channel number and channel diameter.
3. Module drawing, housing dimensions, seal material and sealing arrangement.
4. Connection standard and piping interface.
5. Feed description, composition range, solids, viscosity and temperature.
6. Current feed flow, permeate flow, pressure, crossflow velocity and batch cycle.
7. Required permeate quality, retention, recovery or microbial target.
8. Current CIP recipe, temperature, duration and cleaning frequency.
9. Current problems: lead time, cost, flux decline, breakage, leakage, cleaning or capacity.
10. Photos of the module and nameplate, plus an available used element or representative sample.
Not without verification. Mechanical dimensions, seals, module hydraulics, membrane characteristics and process conditions must be checked. Where compatibility is confirmed, a tube-level replacement may be possible; otherwise a module or system modification may be safer.
No. Nominal pore size is only one factor. The plant should also validate product quality, retention, stable flux, pressure behaviour and cleaning recovery with the actual dairy stream.
Possibly, but it must be reviewed against the membrane material, seals, foulants, chemical concentration, temperature and cleaning result. The aim is to retain a practical plant routine without assuming compatibility.
JIUWU documentation covers tubular ceramic membrane elements, modules and systems. The replacement scope can therefore be assessed at tube, module or system level.
Start with a preliminary compatibility review. Send the existing membrane model, drawings or measurements, process data and CIP conditions. If process performance cannot be confirmed from existing evidence, the next step is sample testing.
Planning a replacement or second-source qualification? Send JIUWU your current membrane model, module drawing and process conditions. Our team can prepare a preliminary compatibility checklist and identify whether the next step should be dimensional matching, sample testing, module replacement or a system-upgrade study.




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