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Tri-Soap with Benzoate · NLGI 1–2 · Drop Point >240°C

Aluminium Complex Grease Manufacturing
Formulation SOP, NLGI Range & Plant Equipment

The dominant tacky-adhesive grease chemistry and the workhorse NSF H1 food-grade thickener — aluminium complex (AlX) grease combines aluminium isopropoxide with stearic acid and benzoic acid to form a translucent, stringy, naturally tacky tri-soap with drop point above 240°C. The chemistry serves three distinct markets: open-gear and wire-rope grease for mining and infrastructure, NSF H1 food-grade for the food and pharmaceutical industries, and specialty industrial applications where extreme adhesion is the primary performance need. This guide covers the in-situ saponification SOP, raw-material specifications, NLGI grade range, ASTM performance targets, and reactor equipment.

>240°C
ASTM D2265 Drop Point
NLGI 1–2
Consistency Range
10–14 wt%
Soap for NLGI 2
NSF H1
Workhorse Food-Grade Thickener
Chemistry Overview

What Aluminium Complex
Grease Actually Is

Aluminium complex grease is a soap-thickened grease in which the soap is an aluminium tri-soap — specifically, an aluminium complex of stearic acid and benzoic acid — dispersed in mineral or white oil base. The chemistry exploits aluminium's tri-valent oxidation state: each aluminium atom can bond with three carboxylate groups, allowing a mixed soap structure where two stearate and one benzoate are bonded to each Al atom (typical formulation), giving a thermally stable complex.

The in-situ reaction is straightforward: 2 R-COOH + C₆H₅COOH + Al(OiPr)₃ → Al(OOC-R)₂(OOC-C₆H₅) + 3 iPrOH. The aluminium isopropoxide (the most controllable aluminium source) reacts with the mixed acid charge to form the aluminium tri-soap, releasing isopropanol which is stripped off and recovered. The reaction occurs in the base oil; the soap forms as fine fibres that re-crystallise on cool-down into the characteristic translucent, stringy, tacky gel.

The tackiness is intrinsic to the chemistry, not a property of an added tackifier. The aluminium tri-soap fibres are short and ribbon-like, with strong inter-fibre cohesion driven by the benzoate aromatic stacking. This gives the grease its unique combination of high yield strength (it does not flow under gravity) and very high tack (it sticks aggressively to metal surfaces). The translucent appearance — another distinctive feature — comes from the small fibre size and high refractive-index matching with the base oil.

Three application properties make AlX commercially important: (1) natural tackiness for open gears, wire ropes, slide ways and any application where grease throw-off is a problem; (2) NSF H1 compliance — all raw materials (aluminium isopropoxide, stearic acid, benzoic acid, USP white oil) are HX-1 listed, making AlX the workhorse food-grade thickener; (3) good water resistance with drop point >240°C, enabling marine and outdoor industrial applications.

Raw Materials

Raw Material Specifications
& Suggested Treat Rates

ComponentGrade / SpecificationTreat Rate (NLGI 2)Function & Sourcing
Base oil — primaryUSP white oil (NSF H1) or Group II SN500, KV40 90–110 cSt55–65%USP white oil for NSF H1 variant; Group II for industrial open-gear AlX. The base oil drives application suitability.
Base oil — secondaryUSP technical white oil 70/80 or Group II SN15015–25%Diluent for acid dissolution. Match the primary base oil for NSF H1 compliance.
Stearic acidTech grade or USP (for NSF H1), AV 195–205, SV 200–2108–10%Primary fatty acid. NSF HX-1 listed grade required for food. Specify saturated (IV <5).
Benzoic acidUSP / FCC grade, >99.5% pure, AV 458–4632–4%Complexing aromatic acid. NSF HX-1 listed grades available. Drives the complex drop-point gain.
Aluminium isopropoxideAl(OiPr)₃, technical grade, ≥95% pure, white solid or solution in iPrOH1.5–2.5%The aluminium source. Stoichiometric ratio: 1 mol Al per 3 mol total acid (2 stearate + 1 benzoate). Sourced from Sasol, domestic chemical suppliers.
AntioxidantHindered phenol (BHT) + aryl-amine (HX-1 for NSF)0.5–1.0%Standard antioxidant package. HX-1 listed grade for NSF H1.
Rust inhibitorSorbitan monooleate + amine carboxylate (HX-1)0.3–0.6%Standard rust package. Modest dose since AlX already has good rust resistance.
Tackifier (open gear / wire rope)PIB 2400 cSt or polyisobutylene1–5%For open-gear and wire-rope variants. AlX is naturally tacky but PIB enhances it dramatically for harsh service.
Bitumen extract (mining only)Asphaltic residue or extract0–10%Used in cost-driven mining wire-rope grease for ultimate adhesion and load capacity. Not for NSF H1.
Solid lubricant (optional)PTFE micropowder (HX-1 for NSF) or MoS₂ (industrial only)1–5%PTFE for NSF H1 high-load variants; MoS₂ for non-H1 open-gear loaded service.
Manufacturing SOP

In-Situ Aluminium Saponification —
6 Steps, Isopropanol Recovery

The aluminium complex SOP follows the soap-grease pattern with one critical difference: isopropanol is generated as a by-product and must be stripped off through a condenser. The reactor must have a condenser with isopropanol recovery on the vent line — both for environmental compliance and to recover the alcohol for re-use. Total cycle time for a 200–400 kg batch is approximately 8–10 hours.

1
Charge base oil and acids (T = 90–100°C)
Charge half the base oil (USP white oil for NSF H1, or Group II SN500+SN150 for industrial) plus the full stearic acid charge and the full benzoic acid charge into the jacketed reactor. Heat to 90–100°C with anchor stirrer at 30–60 rpm. The stearic acid (mp ~70°C) and benzoic acid (mp ~122°C — somewhat slower to dissolve) fully melt and dissolve into the oil to form a clear amber solution. Hold 15–20 minutes after clarity to ensure homogeneous acid distribution.
2
Aluminium isopropoxide addition (T = 95–105°C)
Charge the aluminium isopropoxide slowly to the reactor over 30 minutes — either as solid powder fed through a screw conveyor or as a slurry in cold iPrOH. The reaction begins immediately: aluminium isopropoxide reacts with the carboxylic acids to form aluminium soap, releasing isopropanol. Open the reactor vent through a chilled condenser to capture the isopropanol — vapour evolution is vigorous. Bulk turns from clear amber to opaque cream as the aluminium soap precipitates.
3
Reaction completion and isopropanol stripping (T = 130–150°C, 60 min hold)
Ramp temperature from 105°C to 130–150°C over 30 minutes. Continue condenser operation — remaining isopropanol strips off (iPrOH bp 82°C, fully volatile at 150°C). Hold at 150°C for 60 minutes for reaction completion. Verify acid value drops below 5 mg KOH/g (incomplete reaction means residual fatty acid; verify aluminium dose stoichiometry). Verify isopropanol fully stripped by water content of bulk <0.5%.
4
Top-temperature dispersion (T = 200–215°C, 15 min hold)
Add the remaining base oil. Bulk temperature drops 30–40°C on this addition. Resume heating and ramp to 200–215°C. Hold for 15 minutes. This is the critical fibre dispersion hold — aluminium complex fibres dissolve at top temperature and re-crystallise on cool-down to give the characteristic translucent appearance and tacky texture. Below 200°C, fibre development is incomplete and drop point falls below 240°C; above 220°C, fibres can degrade and grease turns slightly darker.
5
Controlled cool-down and additive addition (T = 215°C → 90°C over 60–90 min)
Begin slow controlled cooling using jacket water. Ramp from 215°C to 90°C over 60–90 minutes. The translucent stringy appearance develops during this cool-down phase — the soap fibres re-crystallise from the dispersed state. At 90°C add antioxidant, rust inhibitor, and tackifier (PIB) if making open-gear or wire-rope variant. Stir 20 minutes to fully disperse additives. Do not add tackifier above 100°C — PIB can degrade.
6
Light milling and packaging (T = 60–70°C)
Cool to 60–70°C and discharge through a coarse screen. Pass through three-roll mill 2 passes (50/25 µm) — light milling for aluminium complex (heavier milling breaks the long stringy fibres and loses the characteristic tacky texture). Test ASTM D217 worked penetration, D2265 drop point (>240°C), D1264 water washout. Pack into clean drums or pails when in spec.
Performance Targets

Typical ASTM Properties —
NLGI 2 AlX (Industrial & NSF H1)

PropertyASTM Test MethodTypical ValueIndustrial / NSF H1 Spec
Worked penetration, 60 strokesASTM D217265–295 (0.1 mm)265–295
Penetration change, 100,000 strokesASTM D217+15 to +35 dmm+50 max
Dropping pointASTM D2265245–260°C240°C min
Water washout @ 79°CASTM D12642–5%10% max
Four-ball wear scarASTM D4172, 40 kg, 75°C, 1h0.45–0.55 mm0.60 max
Four-ball EP weld pointASTM D2783160–250 kgf (with EP additive 250–315)160 kgf min (general); 250 min (industrial)
Oxidation stability, 100h @ 99°CASTM D9423–8 psi pressure drop10 psi max
Oil separation, 24h @ 100°CASTM D1742 / D61843–6%10% max
Copper corrosion, 24h @ 100°CASTM D40481a1b max
Apparent stringiness (visual)Visual assessmentHighly stringy, translucentCharacteristic property — not a numerical spec
Application Matrix

When to Choose
Aluminium Complex

NSF H1 FOOD
Food & Pharma Processing
NLGI 2 AlX on USP white oil is the workhorse NSF H1 grease for food machinery bearings, dairy fillers, bottling lines, packaging machinery, baking equipment — the largest market for AlX globally. HX-1 listed at every component level.
HX-1 listed
OPEN GEAR
Mining Shovels, Kilns, Cement Mills
NLGI 0/1 AlX + bitumen + tackifier for large open gear drives — cement kiln girth gears, mining shovel slewing gears, sugar mill drives. Spray-applied with solvent diluent. Adhesion prevents throw-off; load capacity from solid lubricant package.
Spray applied
WIRE ROPE
Mining Headrope, Crane Wire, Cables
NLGI 0/1 AlX + tackifier + bitumen for wire rope penetration grease. Must penetrate the rope core during application and resist throw-off at speed. Hot-applied or cold-applied formulations. Mining hoist ropes, port cranes, suspension bridges.
Adhesive
CONVEYOR CHAIN
Heavy Conveyor & Slat Chains
NLGI 1/2 AlX + EP for industrial conveyor chains, slat chains, drag chains — tackiness prevents fling-off at chain return; thermal margin handles ambient/process heat. Common in cement, mining, glass plants.
Tacky chain
SLIDE WAY
Machine Tool Slide Lubrication
NLGI 0 AlX for machine tool slide ways and gibs — the natural tackiness gives stick-slip control and prevents grease squeeze-out at slow speed. Industrial machine shop standard for box-way lubrication.
Stick-slip control
NOT FOR
High-Speed Bearings, Severe EP
High-speed roller bearings (the tackiness causes drag and heat generation), or severe shock-load steel-mill bearings (limited EP without additive top-up) — for these, switch to LiX, CaSX or polyurea. AlX is the chemistry for adhesion-critical applications.
Choose Li / CaSX
Failure Modes

Common Failure Modes
& Production Fixes

Failure ModeRoot CauseDiagnostic TestFix
Drop point below 240°CTop temperature below 200°C; or benzoic acid ratio too lowD2265 drop point; recheck stoichiometryRaise top hold to 215°C, 15 min; verify benzoic acid:stearic molar ratio 1:2 minimum; verify Al stoichiometry covers both
Grease opaque / not translucentCool-down too fast; or top temperature too low for fibre developmentVisual; D2265 drop pointSlow cool to 90 minutes from 215°C; ensure top hold at 210°C minimum; verify benzoic acid contributing to complex
Grease not tacky / stringyOver-milled (broke long fibres); or insufficient soap contentSensory; D217 penetrationReduce mill passes to 1–2; widen final gap to 50 µm; consider raising soap content to 12–14%
Severe foaming during Al isopropoxide additionRapid isopropanol generation overwhelming condenser; or acid mass too viscousVisual; reactor vent flow rateSlow Al isopropoxide addition to 45 min; oversize condenser capacity; verify acids fully melted before Al addition
Acid value remains high after step 3Al isopropoxide degraded (moisture-aged); or aluminium dose stoichiometrically lowAcid value; check Al supplier CoAVerify Al(OiPr)₃ stored in dry sealed condition; recalculate Al dose at 1 mol per 3 mol total acid + 5% excess
Discolouration (yellow / brown)Top temperature exceeded 220°C; or oxidation during high-temp holdVisual / colour scaleControl top hold strictly at 210°C; add antioxidant earlier; use nitrogen blanket if persistent
Isopropanol not fully strippedDehydration hold insufficient; or vent restrictedWater/iPrOH content of bulk <0.5%; flash point checkExtend hold at 150°C to 90 min; verify condenser not flooded; sample bulk and confirm iPrOH below detection
Plant Equipment

Pilot & Production
Plant Equipment for AlX

An aluminium complex grease plant is similar to a lithium soap plant with two specific additions: a condenser system for isopropanol capture (both environmental compliance and isopropanol recovery), and (for NSF H1 variants) dedicated stainless reactor and packaging segregation to maintain H1 cleanliness. See our Plant Setup service for complete specification and ISO 21469 facility planning.

Equipment List · 200–500 kg/batch AlX plant
Aluminium Complex Grease Plant — Indicative Equipment & Sizing
A jacketed reactor 400–700 L volume in 304 stainless steel (mandatory for NSF H1; preferred for industrial AlX), rated for 220°C operation. Heating by thermal oil (preferred) or high-pressure steam capable of 210°C. Anchor stirrer with frame agitator at 30–60 rpm, variable-frequency drive. Sealed head with vent line connected to a chilled-water condenser (10–30 L/min cooling capacity) for isopropanol capture — the condenser typically recovers 70–90% of the isopropanol for re-use, paying back its cost in 1–2 years.
A three-roll mill (Indian fabricated, light-duty 1–2 TPH capacity, 6–10 lakh) or homogeniser — AlX needs only light milling so the equipment can be smaller than for LiX. Drum filling station. For NSF H1 production, dedicated mill, packaging line, and storage area to maintain ISO 21469 segregation. Lab: penetrometer, drop-point apparatus, four-ball wear rig (industrial AlX), copper corrosion bath. Total plant capex band ₹60 lakh to ₹2 crore for 300–700 kg/batch — broadly similar to LiX with the condenser and NSF H1 segregation premium.
Reactor
400–700 L stainless, 220°C rated
Critical addition
Condenser for isopropanol recovery
NSF H1
Dedicated reactor + packaging segregation
Capex band
₹60 lakh to ₹2 cr pilot to production
Questions & Answers

Frequently Asked About
Aluminium Complex Grease

What makes aluminium complex grease tacky and adhesive?

The aluminium tri-stearate + benzoate complex soap forms a translucent, stringy, gel-like structure that is naturally tacky — this is an intrinsic property of the aluminium soap chemistry, not from added tackifier. The tackiness gives the grease excellent adhesion to vertical and high-vibration surfaces, preventing throw-off in open gear, wire rope, and slide-way applications.

PIB tackifier (1–5%) and bitumen (mining only) can be added for extreme adhesion in wire rope cores and open gears. The natural tackiness comes from the short ribbon-like fibres held together by aromatic stacking of the benzoate groups.

Why is benzoic acid used in aluminium complex grease?
Benzoic acid (C₆H₅COOH) is the complexing aromatic monobasic acid that, combined with stearic acid and aluminium, gives the complex soap structure with drop point >240°C. The aromatic ring stabilises the aluminium soap fibre matrix at higher temperature than simple aluminium stearate (which has drop point only ~100°C). Some formulations use mixed aromatic-aliphatic dibasic acids instead, with similar effect. Benzoic acid is also NSF HX-1 listed, making it suitable for food-grade.
What is the aluminium source — isopropoxide or stearate?
Both are used commercially. Aluminium isopropoxide (Al(OiPr)₃) reacts in-situ with stearic + benzoic acid to form the complex soap, releasing isopropanol which must be stripped. Aluminium tri-stearate (pre-formed) can be used as a simpler input — no isopropanol generation — but limits the complex chemistry control. Aluminium hydroxide (Al(OH)₃) is occasionally used but less reactive. Isopropoxide gives the most controllable chemistry and best fibre development, and is the standard in modern AlX production.
Is aluminium complex grease NSF H1 compatible?
Yes — aluminium complex is the workhorse NSF H1 thickener and accounts for the majority of NSF H1 grease produced globally. Aluminium isopropoxide, stearic acid, benzoic acid and USP white mineral oil are all HX-1 listed. It is the lowest-cost H1 thickener and gives good general-purpose H1 NLGI 2 performance for food machinery bearings. See our NSF H1 grease page for the full food-grade formulation framework.
Why does aluminium complex have such high water resistance?
The aluminium complex fibre structure is highly oleophilic and contains aromatic benzoate groups that do not interact with water. Water washout per ASTM D1264 is typically 2–5% at 79°C — excellent. Combined with the natural tackiness, this makes aluminium complex ideal for marine applications, wire rope grease that must survive splash water, and outdoor open gears exposed to rain. The hydrophobic complex is fundamentally different from simple aluminium stearate which has poor water resistance.
Can aluminium complex be made very tacky for wire rope service?
Yes — the standard wire rope grease formulation adds 2–5% PIB 2400 tackifier and 1–3% bitumen (for cost-driven mining variants) or polymer modifier (for premium variants). The grease must penetrate the wire rope core during application yet not throw off during operation — both requirements served by adhesive aluminium complex chemistry. We can formulate wire-rope variants for hot-applied (drum-melted at 80°C) or cold-applied (room-temperature spray with solvent).
What is the typical drop point and how is it achieved?
240–260°C typical for NLGI 2 AlX. Achieved by the aluminium tri-stearate + benzoate complex structure which is significantly more thermally stable than simple aluminium stearate (drop point ~100°C). The benzoate component stabilises the matrix against melting. Top temperature dispersion at 210°C is critical — below this, the complex structure is incomplete and drop point falls. The slow controlled cool-down further consolidates the fibre matrix.
How is isopropanol handled during AlX manufacturing?
Aluminium isopropoxide releases approximately 3 mol of isopropanol per mol of Al consumed — significant volume from a 2 wt% Al dose. The reactor vent is connected to a chilled-water condenser that captures the isopropanol vapour. Recovered isopropanol can be re-used for fresh isopropoxide slurry preparation or sent to solvent recovery. This is both an environmental requirement (no atmospheric VOC release) and an economic benefit — the recovered isopropanol is typically worth several lakh rupees per batch in larger production.
Related Pages

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