Division 01. Oil & lubrication

Oil & lubrication: four disciplines, one data set.

Analyse, Purify, Fortify, Advise. Bought separately they are four line items. Run together against one condition history they become a programme that keeps a charge in service for years rather than months.

01. Analyse

Condition monitoring that produces decisions, not just numbers.

A report full of results is worthless if nobody knows which reading matters. Every Malina panel comes back with the values, the trend, the limit each value is measured against, and the action we recommend.

Malina OilCycle closed-loop diagram Oil flows from the reservoir through the machine, into a Malina purification and monitoring skid, then returns clean to the reservoir. Reservoir IN SERVICE Turbine / Hydraulic HEAT & SHEAR Malina skid CLEAN & REPLENISH MPC SAMPLE POINT OIL STAYS IN THE SYSTEM, DEPOSITS LEAVE IT
Oil stays in the system; the deposits and water are what leave it.

The standard turbine and hydraulic panel

The slate below is our default for critical rotating equipment. It is adjusted for the fluid type, the duty, and whatever the last round of data flagged.

  • MPC varnish potential (ASTM D7843), the deposit-forming tendency of the oil.
  • RPVOT (ASTM D2272), remaining oxidative life against the new-oil baseline.
  • Particle count (ISO 4406), solid contamination, coded per channel.
  • Water content (Karl Fischer, ASTM D6304), free, emulsified and dissolved.
  • Viscosity at 40 °C (ASTM D445), the first sign of the wrong fluid or heavy oxidation.
  • Acid number (ASTM D664), acidic by-products of degradation.
  • FTIR, oxidation, nitration, additive depletion and contamination fingerprints.
  • Elemental analysis (ICP), wear metals, additive elements and contaminant metals.
Example alarm framework for an ISO VG 46 turbine oil. Limits are set per system at baseline.
TestNormalCautionAlarm
MPC ΔE< 1515–30> 30
RPVOT retained> 50 %25–50 %< 25 %
ISO 4406 code≤ 16/14/1117/15/12≥ 18/16/13
Water (ppm)< 150150–300> 300
Viscosity change± 5 %± 5–10 %> ± 10 %
Acid number rise< 0.10.1–0.3> 0.3

Normal Caution Alarm  Thresholds shown are typical starting points; the OEM manual and the system baseline take precedence.

02. Purify

Take the contamination out. Leave the oil in.

Varnish is not filtered out by a finer filter, because at operating temperature it is dissolved, not suspended. Removing it means changing the solubility of the fluid so the deposit releases from surfaces and re-enters the oil, where filtration can finally catch it.

Soft contamination

Deposit control

Live dosing of an oil-soluble cleaning fluid at a controlled treat rate. Deposits already on valve spools, journals and cooler surfaces dissolve back into the fluid and are removed downstream. No outage in most systems.

Hard contamination

Filtration

Kidney-loop depth filtration sized to the reservoir turnover you actually need, plus electrostatic capture for sub-micron degradation products that beta-rated media cannot hold.

Water

Dehydration

Vacuum dehydration for bulk removal, coalescing for free water, and desiccant breathers so humid Nigerian air stops re-wetting the reservoir every time it cools down.

What we will tell you before we quote

Deposit control is not a universal answer. If the varnish is being generated by a mechanical fault, a hot spot, an air-entrainment problem, a failing cooler, cleaning the oil buys time but does not fix the cause.

  • Whether the deposit source is chemical, mechanical, or both.
  • Whether the charge is worth saving or genuinely at end of life.
  • Whether the system can be treated live, or needs a planned outage.
  • What the fluid will look like at 30, 60 and 90 days after treatment.
If the answer is "change the oil", we will say change the oil. Selling a treatment into a system that needs a mechanical repair costs the client twice.
Malina scoping policy

03. Fortify

Base oil outlives its additives. Replace what was consumed.

A Group II or Group III base stock is chemically stable for a very long time. What runs out first is the additive package protecting it, antioxidants above all. Replenishing those is far cheaper than replacing the whole charge, and produces far less waste oil.

Step 01

Measure the shortfall

RPVOT against the new-oil baseline plus voltammetry to see which antioxidant families are depleted and by how much.

Step 02

Confirm the base oil is sound

Viscosity, acid number and FTIR oxidation. If the base stock itself has degraded, replenishment is the wrong call and we say so.

Step 03

Dose to target

Additive package calculated against reservoir volume and the measured deficit, then blended into the running system.

Step 04

Re-measure

Confirmatory RPVOT and full panel after circulation, recorded against the baseline so the trend line stays continuous.

04. Advise

The programme should eventually run without us.

A lubrication programme that depends on a contractor visiting is fragile. We build the routine, then train your people to own it.

Lubrication survey

A full walk-down of every lubricated asset: fluid in use, top-up practice, sample point condition, breather condition, storage and decanting. Output is a ranked corrective list.

Consolidation study

Most plants carry more grades than they need. We map what is actually required, identify safe consolidations, and cut the number of products you stock and can cross-contaminate.

Storage & handling audit

Drum storage, filtration on receipt, sealed transfer, labelling and colour coding. Most contamination enters the system long before the oil reaches the machine.

On-site training

Practical sessions for maintenance technicians and reliability engineers: correct sampling technique, reading a report, when to escalate, and what each alarm actually means.

Next step

Start with one reservoir.

A baseline audit on your most critical system tells you whether there is a programme worth running at all.