Abstract

Spreading kinetics measurements were carried out on crude oils at natural surfactant-containing sea water of well-controlled thermo elastic surface properties in laboratory conditions. It was found that oil lens expansion rates, predicted from the classical surface tension-driven spreading theory, were higher by a factor of 6-9 than those experimentally derived for natural seawater. Previously, in order to explain such a discrepancy, the initial spreading coefficient S0 - entering the lens radius vs time dependence was exchanged with the temporal one St dependent on the water phase surface viscoelasticity of (Boniewicz and Pogorzelski, 2008). Now, natural surfactant concentration and temperature gradients perpendicular to the surface were shown to drive a particular cell-like flow at the surface microlayer, as a result of the classic and thermal Marangoni phenomenon. The balance of interfacial forces was taken as: -µ∂Us/∂z=∂γ/∂T•∂T/∂x+∂γ/∂c•∂c/∂x where: µ is the dynamic viscosity, Us - the velocity, z and x axes oriented perpendicularly and horizontally to the main flow direction, T, γ, c are the temperature, surface tension and concentration of surfactants. Computations performed on original seawater (Baltic Sea) systems, shown that the natural surfactant concentration term ∂γ/∂c is several times lower than the thermal ∂γ/∂T one (Boniewicz and Pogorzelski, 2016). Such a surface tension gradients induce the Benard-Marangoni instability, for high enough the so-called Marangoni numbers that could significantly slow down the spreading process. On the basis of thermo-physical model liquids properties, the critical temperature difference ∆Tc required to initiate the process under an evaporative cooling condition was evaluated.

Highlights

  • IntroductionThe kinetics of spreading various liquid hydrocarbons (including crude oil and petroleum substances) on the surface of the original seawater were investigated using video-microscopy and dynamic tensometry under laboratory conditions

  • The kinetics of spreading various liquid hydrocarbons on the surface of the original seawater were investigated using video-microscopy and dynamic tensometry under laboratory conditions

  • An exemplary radius time history rL(t), for 1-mm3m drops crude oil (Petrobaltic) spreading on sea water collected in Orlowo is depicted in Figure 4 on logarithmic scales, which is characteristic for all the tested volatile liquids

Read more

Summary

Introduction

The kinetics of spreading various liquid hydrocarbons (including crude oil and petroleum substances) on the surface of the original seawater were investigated using video-microscopy and dynamic tensometry under laboratory conditions. The aqueous phase, containing natural surfactants, formed on the surface an adsorption layer with specific viscoelastic properties, which were determined by means of supplementary measurements with the Langmuir technique (Boniewicz-Szmyt and Pogorzelski, 2016). The classic spreading theory, so-called laminar flow theory of the boundary layer (Camp and Berg, 1987; Craster and Matar, 2006) is applicable to the system of immiscible, insoluble, and chemically pure liquids and predicts the rate of expansion of the oil spot 6–9 times higher than that was observed in previous studies (Boniewicz-Szmyt and Pogorzelski, 2008). As a first step made to eliminate the discrepancy between the experimentally measured and theoretically predicted oil on water spreading velocity, the existing model was corrected by replacing the static spreading coefficient S0 with the dynamic one St (Boniewicz-Szmyt and Pogorzelski, 2008). That explained only the observed stopping of the expansion of oil lens edge when St attained 0, and revealed the dependence rL(EAW)

Objectives
Methods
Results
Conclusion
Full Text
Published version (Free)

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call