Lubricant Additives - Ashless Dispersants Series (Final Grade): Low Viscosity Dispersant completes the Sinolook dispersant series as the lowest-viscosity grade (100–250 cSt @100°C) - engineered specifically for the viscosity-critical application space where conventional bis-succinimide dispersants (typically 200–600 cSt) cannot be used without pushing the finished oil above its SAE viscosity grade ceiling. Built on a low-MW PIB backbone (~400–600) instead of the standard 900–1300 MW PIB of conventional bis-succinimide grades, this dispersant delivers full ashless soot/sludge dispersancy while consuming the minimum possible viscosity budget in the finished formulation - enabling maximum treat-rate flexibility in SAE 0W-16, 0W-20, 5W-20, and other fuel-efficiency-targeted low-viscosity grades. Zero ash, zero sulphur, zero phosphorus.
Lubricant Additive · Lowest-Viscosity Ashless Dispersant · Low MW PIB ~400–600 · SAE 0W-16/0W-20 Enabled · Cold-Climate Blending · Automated Plants · Zero Ash/S/P · PCMO · HDEO · Hydraulic · Compressor
Low Viscosity Dispersant
Low Molecular Bis-Succinimide / PIB MW ~400–600 / N 1.0–2.5 wt% · Viscosity 100–250 cSt@100°C / Lowest-Viscosity Grade in Sinolook Dispersant Series · Zero Ash · Zero S · Zero P
| Chemical Class | Low molecular weight polyisobutylene bis-succinimide - same chemistry as standard bis-succinimide (two PIBSA units + polyamine double imidation) but synthesised using short-chain PIB (MW ~400–600) instead of standard HR-PIB (MW ~900–1300); the shorter PIB tails reduce molecular weight and viscosity dramatically while preserving the dual succinimide polar head architecture; free terminal –NH₂ groups provide active dispersant adsorption sites (image formula: H₂N–O–C(=O)–N–C(=O)–NH₂ represents the polar bis-succinimide head group with flanking free amino groups); mineral oil diluent; NO metals / NO sulphur / NO phosphorus / NO boron |
| Why Low MW PIB? | PIB MW is the primary driver of dispersant viscosity: at equivalent N%, a PIB MW ~500 grade has approximately 1/3 to 1/5 the kinematic viscosity of a PIB MW ~1100 grade (due to the polymer chain's hydrodynamic volume relationship with MW - roughly ∝ MW¹·⁸ for PIB in mineral oil). By reducing PIB MW from ~1100 to ~500, viscosity drops from 300–600 cSt to 100–250 cSt @100°C - while dispersancy N% and polar head architecture are largely preserved. The trade-off: shorter PIB tail = smaller steric exclusion zone per molecule = slightly lower soot-holding capacity at high soot concentrations vs high-MW grades; compensated by using slightly higher treat rates (5–8 wt% vs 4–6 wt% for standard high-MW Bis). |
| ★ Defining Property | ★ Lowest viscosity in series - 100–250 cSt@100°C ★ Enables SAE 0W-16 / 0W-20 max treat rate ★ Pumpable at ambient without heating |
| SAPS Status | S/A = 0 S = 0 P = 0 - purest SAPS status in series |
| GHS Hazards | Combustible liquid FP ≥180°C H315/H319 skin/eye irritant |
What Is Low Viscosity Dispersant?
Low Viscosity Dispersant (Low Molecular Bis-Succinimide) addresses the primary formulation barrier to using succinimide dispersants in modern low-viscosity engine oils: the viscosity contribution of the dispersant itself. As OEM specifications have driven finished engine oil viscosity grades progressively lower - from SAE 10W-40 (typical HDEO in 2000s) → 5W-30 (GF-4 era) → 0W-20 (GF-5/API SN era) → 0W-16 (GF-6B/ILSAC 2020) → emerging 0W-8 - the kinematic viscosity window of the finished oil has narrowed from ≥12 cSt to 5.6–7.1 cSt @100°C (for 0W-16). At these viscosity targets, every additive's viscosity contribution is a formulation constraint.
A standard bis-succinimide (PIB MW ~1100, viscosity 300–600 cSt @100°C) treated at 6 wt% in a 0W-20 formulation contributes approximately +8 to +15 cSt to the finished oil - consuming 10–20% of the entire available viscosity window. A low-MW bis-succinimide (PIB MW ~500, viscosity 100–250 cSt @100°C) at the same 6 wt% treat contributes only +3 to +6 cSt - freeing up substantial viscosity headroom for a lower-viscosity base oil blend or a higher dispersant treat rate. This viscosity budget advantage is the defining value proposition of the low-viscosity dispersant grade and the primary reason for its existence as a distinct product in the series.
| Grade | Viscosity @100°C | Approx. ΔKV contribution @6 wt% | 0W-20 headroom used (target 6.9–9.3 cSt) |
|---|---|---|---|
| Poly-Succinimide (high end) | 1000 cSt | +24 cSt | Exceeds grade - reformulate |
| BP Bis-Succinimide | 450 cSt | +11 cSt | ~46% of window |
| Borated Bis-Succinimide | 300 cSt | +7 cSt | ~29% of window |
| Standard Bis-Succinimide | 400 cSt | +10 cSt | ~42% of window |
| ★ Low Viscosity Dispersant | 175 cSt (mid-range) | ★ +4 cSt | ★ ~17% of window - maximum treat-rate flexibility |
Calculation note: Viscosity contribution estimated using ASTM D341 blending index method; 0W-20 base oil blend assumed at 5.5 cSt @100°C (Group III/IV); window = target upper limit 9.3 cSt – base 5.5 cSt = 3.8 cSt total available headroom for all additives. The Low Viscosity Dispersant consumes only ~17% of this total headroom at 6 wt% treat - leaving 83% for detergents, ZDDP, VI improver, and other additives. Standard Bis-Succinimide at the same treat rate would consume over 40% of the window, severely constraining the remaining additive package.
Technical Specification
The dispersant's value in any formulation can be expressed as a ratio: dispersancy delivered per unit of viscosity consumed. Dispersancy is primarily proportional to N% × treat rate (moles of active adsorption sites delivered). Viscosity budget consumed is proportional to the dispersant's kinematic viscosity × treat rate × a blending index factor.
| Grade | N% | KV@100°C | Dispersancy/viscosity index (N%÷KV×1000) | Assessment |
|---|---|---|---|---|
| Mono-PIBSI (std) | 1.5% | 300 cSt | 5.0 | Baseline |
| Bis-Succinimide (std) | 2.0% | 400 cSt | 5.0 | Same ratio as Mono (higher N% offset by higher KV) |
| Poly-Succinimide (N 4.0%) | 4.0% | 500 cSt | 8.0 | Best for high-N delivery per viscosity unit |
| ★ Low Viscosity Dispersant | 1.8% | 175 cSt | ★ 10.3 | ★ Highest dispersancy-per-viscosity of any grade - the defining advantage for low-viscosity oil formulation |
Interpretation: The Low Viscosity Dispersant achieves the highest dispersancy-per-viscosity-unit ratio in the series - not because it has the highest N% (it doesn't), but because its KV @100°C is disproportionately lower than the decrease in N%. This is the mathematical expression of why low-MW dispersants are the preferred grade for low-viscosity engine oil formulations: they deliver more dispersant N per cSt of viscosity budget consumed than any other grade in the series.
| Parameter | Specification | Test Method | Note |
|---|---|---|---|
| Appearance | Clear to brownish liquid | Visual | Clearer and more fluid-like than high-MW grades; the lower MW means less light scattering from polymer aggregates; may be pourable at room temperature without warming - check grade-specific pour point on TDS |
| Kinematic Viscosity @100°C ★ | 100–250 cSt | ASTM D445 | ★ Lowest in series - key selection criterion for 0W-16/0W-20 formulations; include in SAE viscosity grade calculation; no pre-heating required at ambient ≥15°C |
| Nitrogen Content | 1.0–2.5 wt% | ASTM D5291/D3228 | Sufficient for effective dispersancy at 5–8 wt% treat; grade-specific N% on COA; effective N delivery per kg of additive comparable to standard grades due to lower diluent oil content needed (product already has manageable viscosity) |
| PIB Molecular Weight | ~400–600 | GPC | Approximately 1/2 the MW of standard Bis grades (900–1300); shorter PIB tail = smaller steric exclusion zone = use slightly higher treat rate (5–8 wt%) vs standard Bis (4–6 wt%) for equivalent soot-holding at moderate soot levels |
| Flash Point (COC) | ≥ 180°C | ASTM D92 | Combustible liquid; not DG; standard storage and transport |
| Density @20°C | 0.90–1.00 g/cm³ | ASTM D4052 | Lower density vs borated/phosphated grades; use for volumetric treat rate conversion |
| Sulphated Ash / S / P | 0 / 0 / 0 | ASTM D874 / D2622 / D4047 | Purest SAPS-zero status in series - no B, no P addition; fully usable in all ACEA C-series and API SP specifications without any SAPS budget impact |
| Packaging | 180 kg drum · 900–1000 L IBC · Flexitank | - | Store 0–45°C sealed; hygroscopic –NH₂ groups - keep sealed; 24-month shelf life; lower-viscosity product may flow more readily at high ambient temperatures - ensure drums are sealed upright; no heating required for winter blending in most climates |
Performance Profile
Viscosity Budget - The Enabling Function for 0W-16/0W-20
The fundamental performance advantage of Low Viscosity Dispersant is not a traditional additive function (dispersancy, AO, AW) but rather an enabling function: it makes it possible to include adequate dispersant treat rates in finished oil formulations where the kinematic viscosity window is so tight that standard dispersants would push the formulation above the SAE grade ceiling. In SAE 0W-16 (KV target 5.6–7.1 cSt @100°C) with a base oil blend at 4.8 cSt, the total headroom for all additives is only 2.3 cSt - insufficient for 6 wt% of standard bis-succinimide (contributing ~10 cSt) but comfortably accommodating 6 wt% of Low Viscosity Dispersant (contributing ~4 cSt). This enabling function is irreplaceable - no other approach (lower treat rate, higher-N grade) can simultaneously maintain dispersancy performance and fit within the 0W-16 viscosity window.
Cold-Climate Blending - Ambient-Temperature Pumpability
In blending plants operating in cold climates (northern Europe, Canada, northeast China, Russia) where ambient temperatures can reach −10 to −20°C during winter production, standard bis-succinimide dispersants (viscosity 300–600 cSt @100°C, which equates to thousands of cSt at −10°C) require drum heating to 40–60°C before transfer - adding energy cost, heating time, and operational complexity. Low Viscosity Dispersant's lower MW and lower viscosity means it remains pumpable at significantly lower ambient temperatures, potentially eliminating the need for drum preheating in many cold-climate blending scenarios. For automated blending systems with precise volumetric metering (Coriolis flow meters, gear pump blenders), lower-viscosity additives also provide better measurement accuracy and faster dissolution in the base oil charge.
Dispersancy in Precision Systems - Hydraulic & Compressor Oils
In precision hydraulic systems (ISO 32/46 HM, vane/piston pumps) and reciprocating air compressor oils (ISO 46/68/100), the dispersant must: (a) keep polar oxidation by-products suspended to prevent valve reed stiction and filter plugging; (b) not contribute excessive viscosity to a tightly specified ISO VG grade (ISO 46 hydraulic oil target KV 41.4–50.6 cSt @40°C - far less headroom than engine oils). The Low Viscosity Dispersant's compact molecular architecture is advantageous in these applications: smaller PIB tails reduce the molecular cross-section in flow-restricted components (close-tolerance hydraulic pump clearances, compressor valve passages) while the bis-succinimide polar head maintains effective deposit dispersion. At 1–3 wt% treat, its viscosity contribution is negligible for most ISO VG hydraulic grades.
GDI Engine Oils - Preventing LSPI-Era Deposit Challenges
In modern turbocharged GDI (gasoline direct injection) engines covered by API SP and ILSAC GF-6A/B specifications, two challenging deposit phenomena - LSPI (Low-Speed Pre-Ignition, linked to oil droplet ignition) and intake valve deposits (IVD, from oil mist on port injection systems retrofitted to GDI) - require dispersant chemistries that simultaneously provide excellent deposit dispersion without contributing excess viscosity (fuel economy ASTM Sequence VIII) or increasing LSPI propensity (ASTM Sequence IX). Low Viscosity Dispersant's lower MW means smaller oil droplets from piston ring blow-by into the combustion chamber - and smaller droplets have lower LSPI ignition probability (lower auto-ignition reactivity per unit volume). The zero-ash, zero-phosphorus character also ensures no interference with the GDI catalytic converter system at any treat rate.
Applications & Formulation Guidance
1. Low-Viscosity PCMO - The Essential Grade for 0W-16 / 0W-20
For OEM-approved 0W-16 and 0W-20 PCMO formulations (Toyota WS, Honda Ultra-Low Viscosity, GM dexos1 Gen3, Ford WSS-M2C961), Low Viscosity Dispersant is the dispersant of choice - or in many cases the only dispersant that enables the required treat rate within the viscosity window. At 5–7 wt% treat, it delivers Sequence VH sludge performance and Sequence VIH varnish control while contributing only +3–6 cSt @100°C to the finished oil. Combined with a low-viscosity Ca salicylate detergent and reduced-P ZDDP (for P ≤0.08%), the formulation can achieve all ILSAC GF-6A pass criteria - sludge, deposits, wear, LSPI, and fuel economy - in the 0W-20 viscosity window.
2. Standard PCMO & HDEO - Cost-Optimised Dispersant Blending
In standard-viscosity formulations (SAE 5W-30 PCMO, 15W-40 HDEO) where the viscosity constraint is less severe, Low Viscosity Dispersant is often used as a blending component - mixed at 30–50 wt% with standard bis-succinimide or borated bis-succinimide to optimise the dispersant package for blending plant operability: (a) the blend viscosity is lower than the standard grade alone, easing winter blending and automated metering; (b) the combined N% is similar to the standard grade; (c) cost is lower than premium borated grades while retaining flexibility. Typical blend: 50% Low Viscosity Dispersant + 50% Borated Bis-Succinimide → combined dispersant viscosity ~220 cSt, combined boron content ~0.15–0.5%, combined cost positioned between the two extremes.
3. Hydraulic Oil & Compressor Oil - Precise Deposit Control at ISO VG
For precision hydraulic oils and compressor oils where the dispersant must prevent polar oxidation deposits at very low treat rates (typically 0.5–2 wt%) without affecting ISO VG grade compliance, Low Viscosity Dispersant's lower viscosity means that even at a 2 wt% treat in ISO 46 hydraulic oil (target KV 41.4–50.6 cSt @40°C), the contribution is negligible. Standard bis-succinimide at the same treat rate would contribute a small but potentially disqualifying viscosity increase in tightly specified ISO VG grades. The zero-ash nature is also critical for turbine and circulating oil applications where ash-forming additives can deposit on bearing surfaces and in lubrication system filters during extended service.
4. Additive Concentrate & Package Formulation - Low-Viscosity Component in Additive Packages
Additive package manufacturers (Lubrizol, Infineum, Afton, and regional formulators) use Low Viscosity Dispersant as the preferred dispersant component in concentrated additive packages (treat at 8–15% in finished oil) where the package itself must remain pumpable and blendable at the treat-in point. High-viscosity dispersants in a concentrate package can cause the package to gel or become non-pumpable in cold ambient conditions - a particular concern for additive packages exported to cold-climate markets or stored in unheated warehouses. Low Viscosity Dispersant's inherently lower viscosity reduces concentrate package viscosity, improving cold-climate usability and automated blending compatibility without sacrificing dispersant performance in the finished oil.
Additive Compatibility & Blending Notes
| Co-Additive / Scenario | Compatibility | Formulation Note |
|---|---|---|
| Standard / Borated Bis-Succinimide | ● Freely miscible | Full miscibility at any ratio; commonly blended 30–70% Low Viscosity Dispersant / 30–70% standard or borated Bis to achieve intermediate viscosity, N%, and B% properties; no heating required for the blend if Low Viscosity Dispersant component is dominant. |
| Group III / PAO Base Oils (0W-20 target) | ● Excellent | Fully soluble in Group III/IV base oils at 5–8 wt% treat; lower PIB MW maintains oil solubility without increased polarity issues; dissolution is faster and requires less blending time vs high-MW grades in PAO. |
| ZDDP + Ca Detergent package | ● Excellent | No known antagonism with ZDDP, Ca sulfonate, Ca salicylate, or Ca phenate. In 0W-16/0W-20 PCMO, the dispersant's zero P contribution leaves the full P budget (ACEA C3/API SP: ≤0.08%) available for ZDDP - unlike the Boron-Phosphated grade which shares the P budget. |
| Cold-climate blending (<10°C ambient) | ★ Advantage vs series | Key operational advantage: Low Viscosity Dispersant remains pumpable without drum heating at ambient temperatures as low as 0–5°C (grade-specific - confirm pour point on TDS); high-MW grades typically require warming to 40–60°C before winter blending. For automated blending systems in cold-climate plants, this eliminates drum preheating as a production bottleneck. |
Frequently Asked Questions
Q: Is Low Viscosity Dispersant simply diluted bis-succinimide (more diluent oil added to reduce viscosity)?
No - this is a critical distinction. Low Viscosity Dispersant achieves its lower viscosity by using a fundamentally lower-MW PIB backbone (~400–600 MW vs ~900–1300 for standard bis), not by adding extra diluent oil. Adding diluent oil to a standard bis-succinimide reduces the dispersant's N% content proportionally while the polymer chains themselves remain high-MW (and thus high-intrinsic-viscosity) - requiring even higher diluent levels to achieve lower product viscosity, and resulting in a product with very low N% and very high diluent content that is essentially a diluted standard-grade product. By contrast, Low Viscosity Dispersant's low viscosity comes from the polymer's own lower intrinsic viscosity (lower-MW chains) - so the N% remains adequate (1.0–2.5%) at a commercially normal diluent content. The two products - diluted standard-grade vs purpose-synthesised low-MW grade - have the same product viscosity but very different polymer architecture, N% per unit weight, and performance characteristics at equivalent finished oil treat rates.
Q: Does the shorter PIB tail significantly reduce dispersancy performance vs standard Bis-Succinimide?
At moderate soot concentrations (≤3 wt%), the difference in dispersancy is small and practically insignificant. The polar head group architecture (bis-succinimide + free –NH₂) is preserved in the low-MW grade - the adsorption affinity of the succinimide heads for soot particle surfaces is unchanged. The PIB tail's role is primarily steric stabilisation (creating a physical barrier between suspended soot particles to prevent agglomeration) - and shorter PIB tails provide a proportionally smaller steric exclusion zone. At high soot concentrations (>4–5 wt%, as in severe EGR HDEO applications), this smaller steric zone means earlier soot particle flocculation onset - requiring slightly higher treat rates (6–8 wt% vs 4–6 wt% for standard bis) or blending with higher-MW bis-succinimide to compensate. For PCMO (typical soot concentration 0.5–2 wt%), this limitation is largely irrelevant - Low Viscosity Dispersant performs equivalently to standard bis-succinimide at matched N% delivery. The grade selection guidance is straightforward: primary application constraint is viscosity (0W grades, cold blending, hydraulic/compressor) → choose Low Viscosity Dispersant; primary performance constraint is high-soot capacity (severe EGR HDEO >4% soot) → choose standard or Poly-Succinimide.
Q: How does Low Viscosity Dispersant compare to Poly-Succinimide for low-viscosity oil formulations?
This is a frequently misunderstood comparison. Poly-succinimide is often recommended for low-viscosity oils because its high N% (2.0–6.0%) means that the same dispersancy can be achieved at a lower treat rate - and therefore lower viscosity contribution. At N 4.0%, poly-succinimide at 2.5 wt% delivers the same N as Low Viscosity Dispersant at ~6 wt%; the poly-succinimide's viscosity contribution at 2.5 wt% treat is approximately +1.5–2.5 cSt vs Low Viscosity Dispersant's +4 cSt at 6 wt% treat - favouring poly-succinimide slightly on the viscosity budget. However, Low Viscosity Dispersant has several practical advantages over poly-succinimide in many 0W-grade formulation scenarios: (1) significantly lower cost per kg; (2) much easier handling (100–250 cSt vs 200–1000 cSt for poly); (3) better cold-climate blendability; (4) more predictable viscosity contribution (narrower range); (5) better Sequence VH sludge performance (free –NH₂ terminal groups, similar to mono-PIBSI). The optimal choice depends on the specific formulation's N requirement, viscosity budget, and blending plant constraints. In practice, a three-component dispersant blend (Low Viscosity Dispersant + standard Bis + trace Borated Bis for TBN) often provides the best combination of viscosity management, dispersancy, and cost for premium 0W-20 PCMO formulations.
Complete Sinolook Ashless Dispersant Series - Grade Selection Guide
| # | Grade | N% | B% | P% | KV @100°C | ★ Choose when… |
|---|---|---|---|---|---|---|
| 1 | PIBSI (Mono) | 0.8–2.5 | 0 | 0 | 100–500 cSt | Sequence VH sludge critical; standard PCMO cost-target; free –NH₂ performance |
| 2 | Bis-Succinimide | 1.5–3.5 | 0 | 0 | 100–600 cSt | HDEO long-drain; ATF primary; shear stability needed; cost-balanced |
| 3 | Poly-Succinimide | 2.0–6.0 | 0 | 0 | 200–1000 cSt | Maximum N/kg; high-soot EGR HDEO; aviation; long industrial service |
| 4 | Borated PIBSI | 1.5–2.5 | 0.5–1.5 | 0 | 100–300 cSt | SAPS-constrained PCMO needing boron TBN+AO; fuel additive; gas engine |
| 5 | Borated PIB Bis | 1.5–3.0 | 0.3–1.0 | 0 | 150–400 cSt | ATF+shear; HDEO long-drain boron retention; gas engine AO; premium consolidation |
| 6 | Boron-Phosphated Bis | 1.5–3.0 | 0.3–1.0 | 0.2–0.7 ⚠ | 200–450 cSt | Max anti-wear (FePO₄); HDEO severe-duty; industrial no-P-limit; 5-in-1 function |
| 7 | Low Viscosity Dispersant ★ | 1.0–2.5 | 0 | 0 | 100–250 cSt ★ | ★ 0W-16/0W-20; cold-climate blending; hydraulic/compressor; additive concentrate; max treat-rate flexibility within viscosity window |
Technical & Regulatory References
D5291/D3228 (N 1.0–2.5%) · D445 (KV 100–250 cSt - key metric) · D4052 (density 0.90–1.00) · D92 (FP ≥180°C) · D874 (S/A=0) · D2622 (S~0) · D4047 (P=0) · KFT (water) · D7843 (blotter soot dispersancy) · ASTM Sequence VH (sludge - good for low-MW bis) · ASTM Sequence VIH (fuel economy - critical for 0W-16/0W-20) · ASTM Sequence IX (LSPI - 0W-20 requirement) · ASTM D341 (viscosity blending index for grade calculation)
Primary applications: API SP SAE 0W-16/0W-20 · ILSAC GF-6A/GF-6B · GM dexos1 Gen3 · Toyota 0W-16/0W-20 · API SN/SP 5W-30 · API CK-4 (blending component) · ACEA C1/C2/C3/C5 (all S/A zero, P zero - no restrictions) · ISO 32/46 HM hydraulic · ISO 46/68/100 compressor · ISO 6743-4 · DIN 51517 CLP (low-viscosity additive component) · ATF additive package component
REACH registered · TSCA listed · No SVHC · S/A = 0 · S = 0 · P = 0 - purest SAPS status of any grade in the series · DPF/GPF/SCR fully compatible · GHS SDS available · No special disposal classification
Low Viscosity Dispersant · Low MW Bis-Succinimide · PIB ~400–600 · 100–250 cSt · N 1.0–2.5% · Zero Ash/S/P · 0W-16/0W-20 Essential
Request Pricing, TDS & Qualification Sample
Specify target N% (1.0–2.5%), target KV @100°C range, PIB MW grade, application (0W-16/0W-20 PCMO · 5W-30 HDEO blending · hydraulic/compressor · additive concentrate), volume, and destination port. Full COA (N%, KV, density, FP, S/A=0, S=0, P=0, water), TDS, and SDS within 12 hours. Qualification samples (1–5 kg) available.
🎉 Complete Ashless Dispersant Series - All 7 Grades Available:
PIB Mono-Succinimide (PIBSI) ✅ · PIB Bis-Succinimide ✅ · PIB Poly-Succinimide ✅ · Borated PIBSI ✅ · Borated PIB Bis-Succinimide ✅ · Boron-Phosphated PIB Bis-Succinimide ✅ · Low Viscosity Dispersant ✅
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