4.7 Article

Rheology of Cyclopentane sII Hydrate Slurry in Water-in-Model Oil Emulsions: Effect of Surfactant Concentration and Water Droplet Size Relevant for Flow Assurance

期刊

ENERGY & FUELS
卷 36, 期 12, 页码 6069-6082

出版社

AMER CHEMICAL SOC
DOI: 10.1021/acs.energyfuels.2c00473

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  1. IIT Madras as part of the Institute Research and Development Award (IRDA) [OEC/17-18/835/RFIR/JITE]
  2. IRDA, Mid Career-021 [RF/21-22/0989/OE/RFIR/008450]

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Investigating the effects of surfactant concentration and droplet size distribution on the rheology of water-in-oil emulsion systems is important for understanding the antiagglomeration properties and finding suitable strategies for flow assurance issues. This study focuses on the rheological characterization of hydrate slurries with a mixed surfactant system and demonstrates that the presence of surfactants can increase the viscosity of the slurries up to a certain concentration, but higher concentrations can reduce viscosity and act as antiagglomerants.
Investigation on the effect of surfactant concentration and droplet size distribution in a water-in-oil emulsion system on the hydrate suspension rheology is vital to delineate the antiagglomeration role and formulate a suitable mitigation strategy for flow assurance issues. Though several studies have been reported on the effect of surfactants on hydrate kinetics, rheological characterization of hydrate systems with surfactants and their role as antiagglomerant are scarce. In this study, rheological measurements are carried out to understand the effect of a mixed surfactant system (Span80 and Tween80 with HLB value of 5.9) at varying concentrations (0.5, 1, 1.5, 2, and 3 wt %) on the structure sII cyclopentane hydrate slurry formed in a water-inmodel oil emulsion with varied droplet size distribution at 265.15 K, atmospheric pressure, and gamma?? = 100 s-1. The model oil consists of light paraffin oil and toluene to represent the saturate and aromatic fractions of the crude oil. Viscosity profiles are reported during formation and dissociation of hydrate slurries, while the flow curve and viscoelasticity tests are reported for the stable hydrate slurries. The presence of a mixed surfactant system is observed to increase the maximum peak and steady-state viscosities of the hydrate slurries up to 1.5 wt % surfactant concentration due to an enhanced oil-water interface and the water bridging between hydrate particles and droplets. At higher surfactant concentration (>1.5 to 3 wt %), capillary bridge between hydrate particles in contact is diminished due to steric hindrance provided by the hydrophobic group of the surfactant adsorbed on the hydrate surface, thus reducing the hydrate slurry viscosity and acting as antiagglomerant. At higher surfactant concentration, the yield stress reduction is observed in the range of similar to 44-87% from the base value. The dissociation experiments show a small depression in the hydrate dissociation temperature from 0.5 wt % to 2 wt %. For 3 wt %, the higher dissociation temperature could be due to metastable hydrate formation in addition to the surfactant molecules surrounding the hydrate crystals, delaying their dissociation.

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