Abstract
Objectives
To determine the basic physiochemical properties and rheological activity of detergent sclerosants.
Methods
Sodium tetradecyl sulphate and polidocanol liquid and foam sclerosants were investigated in a range of concentrations (0.1–3%), liquid-plus-air fractions (1+2 to 1+8) and dilutions in water (stock solutions) or in normal saline. The embolic agent ethanol was investigated for comparison. Density was measured using a digital balance. Surface tension was measured by the Du Nuoy ring method and used to determine the critical micellar concentration. Viscosity was measured using a cone-plate rheometer for liquid and a modified parallel plate method for foam.
Results
Liquid sclerosant density decreased as the sclerosant concentration increased while foam density decreased with the increasing air fraction. The critical micellar concentration of polidocanol was 0.002% in both normal saline and water while that of sodium tetradecyl sulphate was 0.075% in normal saline and 0.200% in water. Viscosity of liquid sodium tetradecyl sulphate was lower than that of polidocanol. Foam sclerosants were at least 10,000-fold more viscous than liquid sclerosants and ethanol. All agents demonstrated a Non-Newtonian shear-thinning behaviour with a fall in viscosity at lower shear rates (<10 s–1). Polidocanol (but not sodium tetradecyl sulphate) foam viscosity progressively increased with increasing sclerosant concentration and liquid-plus-air fractions.
Conclusions
Liquid and foam sclerosants and ethanol are Non-Newtonian shear thinning fluids. Foam sclerosants are significantly more viscous than liquid agents.
Keywords
Introduction
Sodium tetradecyl sulphate (STS) and polidocanol (POL) are sclerosing agents used to permeabilise endothelial membranes with the ultimate aim of removing the intimal lining of target vessels and inducing endovascular occlusion. Prior to this study, little was published on the basic physiochemical or rheological parameters that influence the clinical activity of these agents. In this study, we investigated properties such as surface tension, density and viscosity. The surface tension of a fluid is the cohesive force at the surface of a substance that creates a surface film. The effect on surface tension determines the minimum concentration at which detergents possess maximal activity as sclerosants. The density of a substance is the mass of the substance per unit of volume. The viscosity of a fluid is the resistance of a fluid to shear. The density and viscosity influence the flow and distribution of sclerosants in the target vessels and the degree of mixing with the intra-vascular blood. These fundamental physiochemical properties may influence the clinical activity and in particular the potential for recanalization, treatment failure and complications secondary to the embolic ascent of foam-generated bubbles to the cranial circulation.
Both STS and POL are surface-active agents (surfactants). Surfactants are amphiphilic compounds that possess a polar hydrophilic head and a non-polar hydrophobic tail and therefore have a remarkable chemical resemblance to membrane phospholipids. Surfactants reduce the surface tension and ultimately solubilise cellular membranes. These agents are routinely used in membrane biochemistry to solubilise lipids. Surfactants are subdivided into four groups based on the chemical structure of the hydrophilic head, namely anionic, cationic, non-ionic and Zwitterionic (both negatively and positively charged heads). STS is an anionic and POL is a non-ionic surfactant.
Surfactants have limited solubility in polar solvents such as water. At low concentrations, they disperse in the solvent as monomers but as the concentration of surfactant increases, individual monomers aggregate to form micelles. Beyond a particular concentration specific for each surfactant, the critical micellar concentration (CMC), all additional surfactant added to the solution will aggregate in micelles. Due to their Amphiphilic nature, surfactants concentrate at gas/liquid or liquid/liquid interfaces and have the effect of reducing the surface (interfacial) tension. Increasing the concentration of surfactant has the effect of reducing the surface tension further until the CMC of the surfactant is reached. Beyond the CMC, any additional surfactant in the solution has no further effect in reducing the surface tension.
The interfacial activity of surfactants gives rise to a wide range of surface chemistry functions such as emulsifying, solubilising and foaming. Aqueous foams are dispersions of gas in liquid stabilized by surfactant adsorbed at the gas-liquid interface. These fluids are considered viscoelastic, possessing both the viscousness of liquids and the elastic properties of plastics. 1
The flow dynamics of foams depend on a number of key factors and in particular their viscosity. Viscosity is an inherent property that determines the fluid’s resistance to flow and is affected by factors such as density (mass per unit volume) and shear rate (the velocity gradient across the diameter of the vessel). 2 When viscosity remains constant irrespective of the shear rate, the fluid is termed a ‘Newtonian’ fluid and when it changes with the shear rate, the fluid is termed ‘Non-Newtonian’. Non-Newtonian fluids may be ‘shear thinning’, where the viscosity decreases at higher shear rates or ‘shear thickening’, where viscosity increases at higher shear rates. Water is a Newtonian fluid while blood and aqueous foams are examples of Non-Newtonian shear thinning fluids.3,4
In this study, we aimed to determine some of the most fundamental physiochemical and rheological properties of detergent sclerosants such as their surface tension, CMC, density and viscosity. We compared these properties with that of the embolic agent ethanol and also investigated the influence of sclerosant type, format, concentration and foam composition.
Methods
Definitions
Liquid-plus-air fraction (LAF) was defined as the relative volumes of liquid and air constituents used in foam preparation. Reference foam of 1 + 4 consisted of one part liquid and four parts air. LAF investigated in this study included 1 + 2, 1 + 3, 1 + 4, 1 + 5, 1 + 6, 1 + 7 and 1 + 8. ‘Wet’ and ‘dry’ were defined in comparative terms to 1 + 4 reference foam. Hence ‘wet’ foams were those containing less air (1 + 2 and 1 + 3) while ‘dry’ had a higher air component (e.g. 1 + 8). LAF should be differentiated from liquid volume fraction (LVF), commonly used in physiochemical and engineering literature, which refers to the volume fraction of liquid in aqueous foams and presented as a percentage.
Materials
These included: STS 3.0%, 1.0%, 0.5% (FIBRO-VEIN, Australasian Medical and Scientific, NSW, Australia); POL 3.0%, 1.0%, 0.5% (Aethoxysklerol, Chemische Fabrik Kreussler, Wiesbaden, Germany); ethanol (Ethilbloc, Dehydrated Alcohol, Phebra, NSW, Australia); sodium chloride 0.9%w/v (normal saline [NS], Baxter Healthcare, NSW, Australia); 1 mL luer-lock syringe (Becton Dickson [BD], NJ, USA); 3 mL luer-slip syringe (Terumo, NJ, USA); three-way stopcock (BD); 5 micron Sterifix filter (B-Braun, Melsungen, Germany); 25 G (0.260 mm bore) needles (BD); sterile water (Pfizer, NSW, Australia); Nachromix Solution (Godax Laboratories, Maryland, USA); MilliQ Water (Millipore Corporation, MA, USA); Digital scale – Sartorius Analytic – A200S (0.0001 g sensitivity) (Sartorius AG, Goettingen, Germany); KSV Sigma 70 Tensiometer (Attension/Biolin Scientific, Espoo, Finland); Physica MCR 301 Rheometer (Anton Paar GmbH, Graz, Austria).
Sclerosant preparation
Stock solutions of sclerosants were obtained from manufacturers (dilutions in water) and compared with dilutions prepared in NS. Foam was generated using a modified Tessari method. 5 Briefly, liquid sclerosant was drawn up in the 1-mL syringe and air in the 3-mL syringe to achieve the desired LAF. The two syringes were then assembled using a three-way stopcock with a filter placed on both syringes. Stopcock and filter assembly dead-space always consisted of air at start of foam generation. The plungers were moved through 10 full strokes to disperse the air in liquid. A stroke was defined as a movement emptying and re-filling the syringe initially filled with liquid. The assembly was inverted once during foam preparation. The foam was placed onto the measuring equipment immediately (<10 s) following generation for all experiments. The time taken would have an impact on foam stability as shown by this group previously.6,7
Ambient temperature
All experiments were performed at an ambient temperature of 25℃.
Measurements
Liquid density measurement
A fixed liquid volume of 1 mL of liquid sclerosant was pipetted into a beaker on a digital scale and the mass was recorded. Density was determined by recorded mass divided by the fixed volume.
Foam density measurement
An empty 3-mL syringe was placed on the digital scale and tared. The foam was then generated as described above and collected in the same syringe. The mass of the syringe was measured and the density was calculated as mass divided by volume.
Surface tension measurement
Liquid sclerosant surface tension was measured using the Du-Nuoy Ring method in a tensiometer. The sample vessel was thoroughly cleaned by Nacromix Solution and MilliQ water prior to the start of each experiment. The exterior and interior of the tensiometer, magnetic stirrer and temperature probe were cleaned with ethanol. The Du-Nuoy ring was submerged in a small beaker that is filled with ethanol for at least 30 minutes and dried by blowing with compressed nitrogen gas. The CMC was determined by graphical method. 8
Liquid viscosity measurement
Liquid viscosity was measured using a cone-plate method on a Physica MCR 301 Rheometer. The viscosity of 0.04 mL of liquid sclerosant was tested at shear rates of 1 s–1 to 1000 s–1.
Foam viscosity measurement
Foam viscosity was measured as above. Sandpaper was attached to both plates to stabilise the aqueous foam (plate-plate configuration). 9 Foam viscosity was measured at shear rates of 0.01 s–1 to 1 s–1.
Statistical analysis
Results are expressed as the mean ± the standard error of the mean (SEM). p Values were based on the student’s t-Test with unpaired results and two tails and significance was set at p < 0.05.
Results
Density
Liquid agents
The density of NS, blood and ethanol were determined to be 1007 kg/m3, 1070 kg/m3 and 677 kg/m3, respectively (Figure 1). The density values for liquid sclerosants were higher than ethanol but lower than NS and blood (Figure 1). Density decreased with increasing concentrations of sclerosants declining to approximately 987 kg/m3 (p < 0.05) at 3% concentration for both agents (Figure 2).
The effect of concentration and liquid-plus-air fraction (LAF) on foam sclerosant density. Density was measured for (a) STS and (b) POL foam for a range of LAFs (1 + 2 to 1 + 8) and concentrations. Sclerosant foam density was compared with that of blood ( The effect of concentration on liquid sclerosant density. Density was measured for liquid STS (
), saline (
) and ethanol (
). Results are presented as mean values ± SEM (n > 3).
) and POL (
). Results are presented as mean values ± SEM (n = 3).
Foam sclerosants
Foam sclerosants were 3- to 5-folds lighter than liquid sclerosants (Figure 2). Wet foams (1 + 2 and 1 + 3) were denser than dry foams. Foam density was not influenced by sclerosant concentration.
Surface tension and CMC
There was a progressive fall in surface tension with increasing concentrations of sclerosants until the CMC was reached (Figure 3). The CMC value for STS was graphically determined to be 0.075% when diluted in NS and 0.200% in water. The CMC value for POL diluted in NS or water was approximately 0.002%.
The effect of sclerosant concentration and diluent on surface tension. Sclerosant liquid surface tension was measured using a tensiometer for sodium tetradecyl sulphate (STS) dilutions in normal saline (NS, 
) or water (
) and for polidocanol (POL) dilutions in NS (
) or water (
). The critical micellar concentration (CMC) for STS was 0.075% in NS and 0.200% in water. POL CMC in NS or water was approximately 0.002% (n ≥ 3).
Viscosity
Liquid agents
STS viscosity was comparable with POL while ethanol was more viscous than liquid detergents (Figure 4). Both sclerosants were more viscous when diluted in water than in NS (Figure 5).
Sclerosant liquid and foam viscosity in different diluents. Liquid and foam sclerosant viscosities were obtained for (a) STS (red) and (b) POL (blue) using a Rheometer for a range of concentrations and liquid-plus-air fractions (LAF). Viscosity values for foam sclerosants are compared with those of blood ( Non-Newtonian flow mechanics of sclerosing agents and ethanol. The viscosity as a function of shear rate was determined for (a) embolic agent ethanol and compared with liquid sclerosants (b) sodium tetradecyl sulphate (STS) and (c) polidocanol (POL) diluted in water (n = 3, ▪ and •) or normal saline (n = 3, □ and ○) and 3% foam sclerosants (LAF 1 + 2 to 1 + 8) (d) STS and (e) POL. As the foam viscosity measurements were 10,000-fold higher than liquid, foam viscosity is shown in logarithmic scale and liquid viscosity is shown in linear scale. Results are presented as mean values ± SEM (n ≥ 3).
), saline (
) and ethanol (
). Results are presented as mean values ± SEM (n > 3).
Foam sclerosants
Foam sclerosants were significantly more viscous than liquid agents by at least four orders of magnitude (10,000-fold) (Figure 4). STS foam viscosity was not influenced by changes in concentration or LAFs. By contrast, POL foam viscosity increased at higher sclerosant concentrations and LAFs.
Variations with shear rate
All liquid agents demonstrated a fall in viscosity at lower shear rates (<10 s–1) (Figure 5). Similarly, foam viscosity decreased with an increase in shear rate. Due to breakage and dissipation of bubbles, foam viscosity could not be determined at shear rates > 1 s–1.
Discussion
This study aimed to determine the basic physiochemical and rheological properties of detergent sclerosants and to investigate the role of sclerosant type, concentration, format (liquid vs. foam) and LAF. Liquid sclerosant density was influenced by the sclerosant concentration while the foam density was influenced by the air fraction. The CMC of POL was determined to be 0.002% and not influenced by the solvent while the CMC of liquid STS diluted in NS was found to be lower (0.075%) than that diluted in water (0.200%). Foam sclerosants were found to be approximately 10,000-fold more viscous than liquid agents at very low shear rates but decreased at higher shear rates. While STS foam viscosity was not affected by concentration or LAF, POL foam viscosity increased at higher sclerosant concentrations and LAF.
The density values for STS and POL were similar and lower than that of water. The hydrophobic non-polar tails of both detergent molecules contain long hydrocarbon chains. The relatively smaller water molecules can pack together more tightly and hence water has a higher density compared with detergents. As expected, the density of detergents decreased at higher concentrations due to the increased number of detergent molecules present. This fall in density was more rapid at concentrations below the CMC, demonstrating a steep slope. At concentrations above the CMC, the decline in density was more gradual. This is due to the tighter packing of detergent micelles compared with monomers at such concentrations.2,10
The density of foam sclerosants was significantly less than that of liquid agents. The major determinant in foam density was the LAF, while the concentration of sclerosant had little influence. In a previous study, 11 the density of sclerosant foam was determined to be between 160–200 kg/m3 for STS and 180–240 kg/m3 for POL. This is in line with our measurements of 197 ± 2.9 kg/m3 for STS and 200 ± 6.4 kg/m3 for POL foams (3%, 1 + 4). By comparison, blood density was determined to be 1070 kg/m3 and liquid sclerosants to be 987 kg/m3 for both agents at 3%. Hence, foam sclerosants were much lighter per unit volume compared with liquid sclerosants, which in turn were slightly lighter than blood. In a recent study, 6 we reported on the formation of three relatively distinct horizontal layers of foam, liquid sclerosant and blood following the injection of a wet foam preparation in an experimental model of a superficial vein. Given its lighter density, foam ascends to the top of the vessel and advances over blood. In time, liquid sclerosant drains down due to gravity and remains sandwiched between foam and blood at the foam front. 6 Clinically, the presence of a distinct blood layer at the bottom wall of the target vessel would predispose to non-closure and recanalization. Hence, care should be taken to ensure exposure of the bottom wall of the target vessels to adequate volumes of the injected sclerosant.
Despite the clinical use of detergent sclerosants for many decades, the CMC values for these agents were previously not published. In this study, we determined the CMC value for the stock solution of STS to be 100-fold higher than that of POL (0.2% vs. 0.002%). This is due to a number of reasons. Firstly, ionic surfactants have higher CMC values compared to non-ionic surfactants.8,12,13 Furthermore, the hydrophobic tail length influences the CMC, with longer tail lengths resulting in lower CMC values. 14 POL is a non-ionic detergent and has a much longer tail compared to STS and hence a much lower CMC. Given the higher CMC values for STS, this sclerosant may be considered less efficient than POL in reducing surface tension and achieving maximal surfactant activity. However, given the smaller molecular weight of STS, there are more surfactant molecules present per unit volume of STS compared with POL for the same sclerosant concentration. Therefore, target endothelial membranes are exposed to more STS molecules per unit volume compared with POL. This partly explains the increased potency of STS as a membrane solubilising agent compared with POL.
CMC of surfactants is significantly affected by the addition of buffer additives. 6 High salt concentrations strongly decrease the CMC of ionic (anionic or cationic) surfactants and the CMC of anionic surfactants, in particular, is significantly decreased when these agents are diluted in saline compared with water.8,15 Here, we investigated whether dilutions in NS (sodium chloride 0.9% w/v) had a different CMC to those supplied by the manufacturers prepared in water. While POL had the same CMC value in water and saline, STS showed a much lower CMC in saline (0.075%) compared with water (0.2%). It may not be surprising that the lowest concentration of STS manufactured by STD Pharm (preparation in water) is 0.2%, 16 which is the CMC of this agent in water. Clinically, most practitioners dilute the stock solutions in NS. Based on our present findings, the choice of diluent would make no difference for POL. However, when STS is diluted in NS, concentrations as low as 0.075% would still maintain maximal surfactant activity.
We investigated a number of physiochemical and rheological properties of sclerosant foams. Aqueous foams are mixtures of a gas phase, a liquid phase and a surfactant. In general, liquids are significantly less viscous than aqueous foams and the higher the gas content of the foam (dry foams), the higher the viscosity. In very wet foams, spherical bubbles float in the liquid and move easily. By contrast, dry foams have a tightly packed structure of polyhedral bubbles. With the increasing gas fraction, the foam cells become more polyhedral in structure and more difficult to move. 9 Hence, as a general rule, wet foams are less viscous while dry foams have a higher viscosity.17,18 In this study, POL followed this general pattern and showed a higher viscosity at higher LAFs.
The viscoelastic properties of foams are also influenced by the concentration and the ionic nature of the surfactant. For non-ionic surfactants, an increase in surfactant concentration results in a decrease in surface tension, an increase in foam stability, a tightly packed structure and a higher viscosity.
19
Once again, POL followed this predictable pattern and demonstrated higher viscosity values at higher sclerosant concentrations. The positive correlation between POL concentration and foam viscosity, foam half-time
7
and bubble size
6
is shown in Figure 6.
Relationship between sclerosant concentration and foam viscosity, foam half-time and bubble diameter. Sclerosant foam viscosity(♦), half-time (▪) and bubble diameter (•) were plotted against sclerosants concentration for (a) STS and (b) POL. Viscosity data from the current study are correlated with foam half-time and bubble diameter data from this group’s other recent studies6,7 for a 1 + 4 liquid-plus-air fraction (LAF).
In contrast to POL, STS foam viscosity did not increase at higher LAFs or concentrations of the surfactant. This is most likely due to the anionic nature of STS. The adsorption of anionic surfactants on the liquid/gas interface produces a diffuse electrostatic double layer which generates repulsive forces within the liquid lamella separating the gas bubbles. With an increase in surfactant concentration, the charged surfaces repel any additional surfactant molecules. This repulsive force slows down the adsorption process and as a result the liquid lamellae in ionic surfactants drain at significantly slower rates compared with non-ionic surfactants.15,20,21 Hence, despite the rise in surfactant concentration, the relative wet structure and a stable viscosity is maintained. As shown in Figure 6(a), foam viscosity, half-time or bubble size is not significantly influenced by STS concentration. Microscopic studies are underway to further investigate the effect of the ionic nature of the surfactant on the three-dimensional architecture of the sclerosant foams.
While viscosity is not a function of shear rate for Newtonian fluids, it decreases at high shear rates for Non-Newtonian shear thinning fluids. Here, we demonstrated that STS and POL in both liquid and foam formats as well as the embolic agent ethanol are shear thinning Non-Newtonian fluids. The measured viscosity values for STS and POL liquid and ethanol reached that of water (1 m Pa.s) at higher shear rates (>10 s–1). This implies that at high shear rates, such as in a high-flow blood vessel, the viscosity of the liquid agent will be close to that of blood resulting in propagation away from the intended site of action. At low shear rates, the foam sclerosant viscosity was at least 10,000-fold higher than that of the liquid agents but still decreased at high shear rates. This is most likely due to the lack of foam stability and disruption of the foam structure at high shear rates. This implies that at low shear rates, such as in superficial veins, foams are much more preferable to liquid sclerosants as they are more likely to stay at the intended site of action and less likely to mix with the intra-vascular blood. By contrast, liquid sclerosants have a comparable viscosity to that of blood and are more likely to mix. In high shear rates, such as in an arterio-venous malformation (AVM), the viscosity of the sclerosant or embolic agent will be close to that of blood, resulting in propagation away from the intended site of action. It would be clinically prudent to reduce the velocity and volume flow in such vessels to benefit from the clinical effect of these agents at the intended site of action. This can be achieved by using methods such as infiltration of tumescent fluid in the perivascular space before the administration of the sclerosing or embolic agent.
This study had a number of limitations. Foams were generated in this study using room air as the foaming gas, filters and a modified Tessari technique. Other techniques and gases may yield different results and should be investigated in comparative studies. The effect of temperature on foam viscoelastic properties has been investigated by the authors in a recent study. 7 Future projects will explore the effect of the anionic nature of sclerosants on the structure of the foam bubbles,
In summary, sclerosant foams demonstrated lower densities but significantly higher viscosities compared with liquid sclerosants. The CMC of STS was significantly influenced by the choice of diluent while POL was not affected. POL (but not STS) foam viscosity progressively increased at higher LAF and sclerosant concentrations.
Footnotes
Conflict of interest
All the authors have no conflict of interest and nothing to disclose.
Funding
This research received no specific grant from any funding agency in the public, commercial, or not-for-profit sectors.
Acknowledgements
The authors thank Dr Brian Hawkett, Dr Hank de Bruyn and Dr Binh Pham of Key Centre for Polymers & Colloids (KCPC) and Dr Shaocong Dai of Rheology Laboratory, University of Sydney; Dr Thomas Exner for preliminary experiments to determine the CMC of sclerosants, Prof. Lourens Bester for supplying Ethibloc used in these experiments and Prof. Alun Davies for providing the authors valuable suggestions.
