A Course on Hydrophilic-Lipophilic Deviation (HLD/HLDN)

Module 2: Deconstructing the HLD/HLDN Equation

2.1 The Multivariable HLD Equation

The core quantitative tool developed through extensive experimental studies is the Hydrophilic-Lipophilic Deviation (HLD) equation. This equation emerged from quantifying the conditions required to achieve optimum formulation (Winsor's R=1 equivalent) in surfactant-oil-water systems.4 The HLD equation is fundamentally semi-empirical, representing a linear correlation derived from observing systematic phase behavior transitions during formulation scans.

Recognizing that different types of surfactants respond differently to formulation variables, distinct forms of the HLD equation were initially proposed. These equations represent the specific condition where HLD = 0 (optimum formulation)14. Hover over the terms for brief explanations:

For Anionic Surfactants (e.g., Sulfonates):

LnSNatural logarithm of Salinity (often wt% NaCl). Increasing S makes surfactant more lipophilic (increases HLD). - KCoefficient reflecting oil phase influence. ACNAlkane Carbon Number of the oil (lipophilicity). Higher ACN requires more lipophilic surfactant for balance. - f(A)Function accounting for alcohol/cosurfactant effects. Can increase or decrease HLD depending on alcohol type. - aTTemperature coefficient (usually small for ionics). (TSystem Temperature (°C or K). - TrefReference Temperature (e.g., 25°C).) + σCharacteristic parameter of the anionic surfactant (intrinsic hydrophilicity/lipophilicity). = 0

Here, the LnS term captures the strong dependence on electrolyte concentration. Increasing salinity (S) screens head group repulsions, making the surfactant effectively more lipophilic.14 ACN represents the oil's lipophilicity, f(A) accounts for alcohol effects, aT represents temperature sensitivity (often small for ionics), and σ is the surfactant's characteristic parameter.14

For Nonionic Surfactants (e.g., Ethoxylates):

bSLinear Salinity term (effect usually smaller than for ionics). 'b' is the coefficient. - KCoefficient reflecting oil phase influence. ACNAlkane Carbon Number of the oil. - f(A)Function accounting for alcohol/cosurfactant effects. + cTTemperature coefficient (significant for ethoxylates). (TSystem Temperature. - TrefReference Temperature.) + βCharacteristic parameter of the nonionic surfactant (related to EON, alkyl chain). = 0

For these surfactants, the effect of salinity is often modeled linearly (bS). The most significant variable is usually temperature (T). Increasing temperature reduces ethylene oxide (EO) group hydration, making the surfactant more lipophilic (positive cT coefficient).14 β is the characteristic parameter, often related to EO number (EON).14

These equations linearly combine the effects of the major variables influencing the hydrophilic-lipophilic balance. The remarkable success of these linear equations across a wide range of experimental conditions, despite representing a first-order approximation of potentially more complex relationships,7 underscores their practical utility. Decades of experimental validation supported this linear framework as robust for modeling and predicting SOW system behavior.1 While potential deviations, particularly with complex mixtures,7 were acknowledged, the evidence supported the linear HLD equation as a powerful tool for formulation tasks.14

2.2 Normalization: The HLDN Equation and its Advantages

While the original HLD equations proved highly effective, their existence in slightly different forms, along with various definitions for the surfactant characteristic parameter (σ, β, Cc, etc.), sometimes led to confusion.7 Applying them to complex systems like surfactant mixtures or natural oils also presented challenges.12

To address these issues and create a more unified framework, the **Normalized Hydrophilic-Lipophilic Deviation (HLDN)** equation was introduced.1 The normalization involves dividing the entire original HLD equation by the absolute value of the coefficient associated with the Alkane Carbon Number (ACN), often denoted as |K| or |KACN|.12

HLD to HLDN Normalization (Conceptual)

Original HLD = 0 Equation (Example Form)

Term(S) - K*ACN + Term(T) + Term(A) + Param(Surf) = 0

Normalized HLDN = 0 Equation

(+1)*SCP (-1)*ACN + kS*Term(S) + kT*Term(T) + kA*Term(A) ... = 0

Normalization divides by |K|, setting the ACN coefficient to -1 and the Surfactant Contribution Parameter (SCP) coefficient to +1. Other coefficients (kS, kT, etc.) become relative to the ACN effect.

The key features and advantages of the HLDN equation include12, 7:

The development of HLDN reflects a pragmatic approach for a robust, unambiguous tool for formulation scientists dealing with real-world complexities.12 It represents a refinement aimed at enhancing usability and consistency, presented as a "semiquantitative tool"1 for practical formulation engineering.2

2.3 The Surfactant Parameter: SCP and PACN

Central to the HLDN equation is the **Surfactant Contribution Parameter (SCP)**.11 This single term encapsulates the overall contribution of the surfactant's molecular structure (both head and tail) to the hydrophilic-lipophilic balance. It replaces parameters like σ, β, Cc from earlier formulations and always carries a coefficient of +1 in the HLDN equation.12

It's crucial to understand that SCP is not an intrinsic constant of the surfactant molecule alone.7 Its numerical value depends on integration constants and the specific reference conditions chosen for other variables (Tref, reference salinity, etc.).

To provide a more tangible measure, the concept of **Preferred Alkane Carbon Number (PACN)** was introduced.11 PACN is the experimentally determined SCP value under standardized reference conditions (e.g., T=25°C, pure water or 1 wt% NaCl, WOR=1). Operationally, PACN is the ACN of the n-alkane oil that results in optimum formulation (HLDN=0) with the surfactant under these reference conditions, often found via an ACN scan.11 PACN serves as a standardized, experimentally accessible descriptor of a surfactant's effective hydrophilicity/lipophilicity.

PACN (and thus SCP) is directly related to the surfactant's molecular structure7:

Conceptual PACN Explorer

See how changing surfactant structure conceptually affects PACN.

Conceptual PACN ≈ 7.0

Longer tail increases PACN; Larger head group decreases PACN.

The introduction of PACN bridges the gap between the abstract SCP term and concrete experimental measurement, providing a practical way to characterize surfactants for HLDN calculations.12

Table 2.3: Experimentally Determined PACN Values (Illustrative)

Surfactant Type/Name Structure Example PACN (ACN units) Reference Conditions Source/Methodology Ref.
Nonionic (CiEj) C10E4 ~8.0 T=25°C, Water Ref 28
Nonionic (CiEj) C12E5 ~6.0 T=25°C, Water Ref 40 (PIT-slope derived)
Nonionic (Polyglycerol) C12Gly2 ~8.2 T=25°C, Water Ref 40 (Dynamic PIT/ACN)
Anionic (Sulfate) SDS (C12 Sulfate) ~13-15* T=25°C, 1% NaCl Estimated range based on HLD correlations, e.g., Ref 14

*Note: PACN values for ionic surfactants are highly sensitive to reference salinity.

2.4 Characterizing the Oil Phase: ACN and EACN

The HLD and HLDN equations require a numerical parameter to represent the lipophilicity of the oil phase.1 For simple linear normal alkanes (n-alkanes), this parameter is the **Alkane Carbon Number (ACN)**, the number of carbon atoms in the chain.1

However, most real-world applications involve complex oils (crude oils, vegetable oils, esters, aromatics, etc.).1 To handle these, the concept of **Equivalent Alkane Carbon Number (EACN)** was developed.11, 29

EACN: The ACN of a hypothetical n-alkane that exhibits the same phase behavior (produces optimum formulation under the same conditions) as the actual complex oil being studied.11

EACN quantifies the effective lipophilicity of a complex oil relative to the n-alkane scale within a SOW system context. Determining EACN is crucial for using HLDN predictively.

The primary experimental method is the "fish-tail method" (FTM).11 This involves constructing a phase diagram ("fish diagram") for the oil with a reference nonionic surfactant (e.g., C10E4) and water, typically plotting Temperature vs. Surfactant Concentration.16 The key point is the "fish tail temperature" (T*), where the three-phase region (WIII) meets the single-phase microemulsion region (WIV).20

To find EACN, the T* measured for the unknown oil is compared to a calibration curve (T* vs. ACN) generated using the same reference surfactant with a series of n-alkanes.28 The ACN corresponding to the oil's T* on this curve is its EACN. Studies showed EACN values determined this way were consistent.41

Conceptual Fish Diagram (T vs. Conc.)

Conceptual Fish Diagram Diagram showing phase regions (WI, WII, WIII, WIV) as a function of temperature and surfactant concentration. Used for EACN determination via T*. Surfactant Concentration → Temperature → WII + Water WI + Oil WIII (3φ) WIV (1φ) T* (Tail Point)

This diagram plots Temperature vs. Surfactant Conc. The "fish tail" temperature (T*) where the 3-phase (WIII) and 1-phase (WIV) regions meet is key for determining EACN.

While reliable, the FTM can be time-consuming,29 motivating efforts to develop predictive models for EACN using QSPR, COSMO-RS, or machine learning.20 The EACN concept, coupled with rigorous experimental methods, was essential for extending the HLD/HLDN framework to complex industrial oils.19

2.5 Variable Effects: Salinity (S), Temperature (T), Alcohol (f(A)), Pressure (P)

The HLDN equation explicitly quantifies how different formulation variables shift the hydrophilic-lipophilic balance. Understanding these effects is key to manipulating formulations:

The Compensation Principle

A fundamental concept arising from these relationships is **compensation**. Because multiple variables influence HLDN, a change in one variable shifting the system away from optimum (HLDN=0) can often be counteracted by adjusting another variable.1

Example: If salinity increases (making an ionic system more lipophilic, HLDN > 0), balance (HLDN=0) can be restored by using a more lipophilic oil (increasing ACN) or a more hydrophilic surfactant (decreasing SCP).1

The HLDN equation provides the quantitative basis for predicting these compensations.

Interactive HLDN Calculator & Compensator

Explore the HLDN equation and the compensation principle. Set initial values, see the HLDN, then change one variable and calculate the required compensation in another to return to HLDN ≈ 0.

1. Set Parameters

2. Calculate HLDN

Calculated HLDN: --

3. Compensate to HLDN ≈ 0

Change one value above, then select which *other* parameter to adjust for compensation.

Results

Initial HLDN calculation result will appear here. After changing a value and clicking 'Calculate Compensation', the required adjustment will be shown.

2.6 HLDN Coefficients: Meaning and Typical Values

The coefficients (kS, kA, kT, kP) in the HLDN equation represent the sensitivity of the system's hydrophilic-lipophilic deviation to a unit change in the corresponding formulation variable, normalized relative to the ACN effect.11 Their values depend significantly on the surfactant type and system components.

Obtaining accurate coefficient values is essential for quantitative HLDN application. While comprehensive tabulation requires consulting broader experimental work,14, 48 understanding typical relative magnitudes is pedagogically important.

Table 2.6: Typical HLDN Coefficient Magnitudes (Illustrative)

Coefficient (Normalized) Variable Typical Sign Relative Magnitude (Ionic) Relative Magnitude (Nonionic CiEj) Units (Normalized) Methodology Ref.
kS (for LnS) Salinity + Large N/A (usually linear) ACN / Ln(wt%) Ref 11
kS' (for S) Salinity + Small Small ACN / wt% Ref 11
kT Temperature + Small Large ACN / °C Ref 11
kA Alcohol +/- Variable Variable ACN / f(conc) Ref 11
kP Pressure - Small Small ACN / atm Ref 11

*Note: "Large" and "Small" are relative terms for typical formulation ranges. Specific values depend heavily on the exact surfactant structure and system.

The HLDN framework provides a general structure, but its practical predictive power hinges on having reliable values for these system-dependent coefficients, often determined experimentally for specific systems or surfactant series.14