Technology Comparison

The membrane that doesn't need cartridges.

Traditional diesel polishing relies on disposable filter elements and coalescers that load up, blind, and get thrown away. The CIS rigid composite polymer membrane is regenerated through the designed backwash procedure — so the operating cost shifts from consumables to a little electricity.

Side by side

CIS membrane vs cartridge / coalescer.

Every claim here is traceable to the published datasheet (DS-FUEL-EN, Rev.01). Figures describe the Jingyuan skid-mounted lineup, 5–60 m³/h.

DimensionTraditional cartridge / coalescerJingyuan CIS membrane
Particle captureStrong when fresh; degrades as the element loads≥98% @ ≥5 µm, stable via regeneration
Free-water removalNeeds a separate coalescer stage; element-dependent≥95% free water, no separate stage
Sludge / microbial loadBlinds elements quickly → frequent change-outsGas-pulse clears the surface; no blind-up
ConsumablesRecurring cartridge purchasesNo disposable cartridges
RegenerationManual element swap — labor and downtime30-second gas-pulse, automatic
Service lifePer change-out (weeks–months)Membrane core 2–3 years
Hazardous wasteSpent cartridges (oily waste stream)Minimal — no element disposal
Operating cost profileConsumable-dominated, scales with useEnergy-dominated, low and predictable
Explosion-proof optionVaries by buildExplosion-proof configuration available (JY-Q325 and JY-DX40 standard)
Scope: Dissolved water is not removed by either approach. Capture efficiency is stated on an ISO 16889 basis. Actual consumable savings depend on your contamination load and change-out interval — use the Lifecycle Cost Assessment for a duty-specific estimate.
Failure Analysis

Why Cartridges Fail in Stored Diesel.

Stored fuel is the hardest duty for a consumable element — here is what actually happens in the field.

01
Load & Blind
Elements capture contamination until they clog — differential pressure spikes, flow drops, and change-out interrupts duty. In sludge-heavy tanks this cycle repeats every few weeks.
02
Channeling & Bypass
Under high contaminant load, flow finds weak paths through the element or bypasses it entirely — fuel passes effectively unfiltered while gauges still read "normal".
03
Hazardous Waste Stream
Every spent element is oily hazardous waste — storage, manifesting and disposal add a cost and compliance burden that scales with every change-out.
04
Logistics Chain
Remote sites must stock, ship and schedule the right elements — at a mine or port, cartridge lead time becomes downtime risk, and the wrong element in store is a stopped system.
Visual

One core, two outcomes.

CIS membrane versus cartridge filtration decision diagram
  • 1
    Traditional path

    Buy, install, load, blind, discard — a recurring consumable loop with labor and disposal cost.

  • 2
    CIS membrane path

    Contaminants are separated at the rigid membrane; a gas pulse restores flux in 30 seconds.

  • 3
    Net effect

    Over 2–3 years the membrane core replaces dozens of cartridge change-outs.

Worked Example

Where the Money Goes Over 3 Years.

A mid-size tank farm illustration — 500 m³ processed / month, 12 cartridge changes / year. Event counts illustrate the structure; your own numbers come from the lifecycle assessment.

Cost LineTraditional — 3 yrJingyuan — 3 yr
Consumables36 change-outs × cartridge setsNo cartridges
Labor & downtime36 change-out eventsNone — automatic 30 s regeneration
Hazardous disposal36 oily waste element setsMinimal
EnergyComparable pumping duty (omitted)Membrane regeneration electricity
Membrane refresh1 core at 2–3 yr design life
Cost structureConsumable-dominated — grows with contamination loadNot consumable-dominated — refresh quoted per project

We deliberately do not publish a generic dollar total or savings percentage — those depend on your local cartridge prices, labor rates and disposal costs. Assess your own duty in the Lifecycle Cost Assessment or request a project-specific figure. The structural point stands: a cartridge program's cost scales with contamination load; a membrane system's does not.

Honest Boundary

When a Cartridge Still Makes Sense.

We manufacture membrane systems — and we still tell you where a consumable approach is the reasonable choice.

Very Low Duty
A tank polished a few hours per year with light contamination may never pay back the membrane capex — cartridges stay cheap.
No Compressed Air
Gas-pulse regeneration needs a clean compressed-air source (~0.5–0.7 MPa). Sites without one should factor that in before switching.
One-Off Recovery Jobs
A single emergency tank clean-up with rental hardware can be cheaper than owning a system — though the mobile JY-G100 serves exactly this duty if it recurs.
Migration Path

Switching From a Cartridge System.

01
Duty Review
We review your fuel, tank, contamination baseline and flow — usually from a fuel sample and a short call.
02
Configuration
Model, flow and interface confirmed against your existing pump and piping — much of it is usually retained.
03
Install In Loop
The skid drops into your existing tank circulation loop; cartridge housings are typically decommissioned or kept as final guards.
04
Commission & Baseline
Start-up, regeneration schedule set, and a fuel sample establishes the new cleanliness baseline for tracking.
FAQ

Common questions.

Does the membrane ever need replacement?

The membrane elements have a designed service life of 2–3 years. Within that life they are regenerated in place by gas pulse rather than replaced at every clog like a cartridge; at end of service life the membrane core is replaced — a planned, infrequent maintenance event rather than a recurring consumable stream.

What powers regeneration?

A short pulse of clean compressed air (external 0.5–0.7 MPa source) clears the membrane surface — no hot water, chemicals or solvents.

Does elimination mean lower uptime risk?

Yes. There is no element to stock, ship to a remote site, or fit under time pressure — a meaningful advantage for mining and marine duty.

Is the initial investment higher?

Capex is typically higher than a bare cartridge housing; the payback comes from eliminating the consumable, labor and disposal stream. Most duty cycles recover the difference within the first membrane service life — assess yours in the Lifecycle Cost Assessment.

Can it connect to my existing piping and pump?

In most migrations, yes. Skid interfaces follow standard flange sizes (e.g. DN100 PN16 on the DL60), and much of the existing pump and piping is retained — the skid drops into the tank circulation loop.

What are the membrane's operating limits?

Media boundary: diesel with flash point ≥38 °C — gasoline is strictly prohibited (DX5 additionally handles kerosene, hydraulic and turbine oil). Dissolved water is not removed; free and emulsified water (≥95%) is the design target.

See the numbers for your duty cycle.

Use the selector and lifecycle cost assessment, or send us your tank size and contamination problem.

Open Lifecycle Cost Assessment