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Cavitation Technology Development for Oil Sands Processing Cavitation Technology Development for Oil Sands Processing

Cavitation Technology Development for Oil Sands Processing - PowerPoint Presentation

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Cavitation Technology Development for Oil Sands Processing - PPT Presentation

Deepak M Kirpalani and Nishi Bhatt August 2012 Energy Mining and Environment Portfolio NRC Canada Presented at the 8th International Symposium on Cavitation CAV2012 Cavitation Studies at ID: 235632

sonication cavitation oil acoustic cavitation sonication acoustic oil yield sands water frequencies bitumen viscosity time extraction research power measurements

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Slide1

Cavitation Technology Development for Oil Sands Processing

Deepak M. Kirpalani and Nishi Bhatt

August 2012

Energy Mining and Environment Portfolio –NRC Canada

Presented at the 8th International Symposium on Cavitation - CAV2012 Slide2

Cavitation Studies at NRCC

High Speed Imaging of Cavitation Bubbles

Laser

Interferometry

of Acoustic Cavitation

Phase Field Modeling of Cavity Under ShearSlide3

Oil sands are unconventional heavy oil deposits composed of water 4-6%, sand, clay and bitumen (12%) and other minerals. Mineral matter -80-85%Extraction technology:Mined Oil sands 

Crushed &Screened  mixed with hot water in cyclofeeder

to 50-55 deg. C Pumped (hydrotransported)  separation vessels where bitumen froth (60% bitumen, 30% water, 10% fines) floats on the surface.

Processing Issues: pumping costs and sand erosionTailings Requirements:Energy Resource Control Board of Alberta, Canada Directive ‑ 074 requires that the oil sands industry minimize and eventually eliminate long-term storage of fluid tailings in the reclamation landscape.

Commercial Thickeners are currently used.Slide4

Acoustic Cavitation for Bitumen ExtractionEarly stage research (Sadeghi, 1990) showed that acoustic cavitation at 40KHz. can be applied for extracting bitumen from oil sands.

The reaction rate was further enhanced by the addition of H202

.Benefits:Eliminates the need for surfactants or alkaline chemical agents during extraction

Circumvents hot water and steam useSlide5

Cavitation Benefits to Oil Sands Processing

Homogenization of Liquids

Breakage of solid particles

Radicalization of Molecules

Local temp change and availability of free radicals

Emulsion preparation

Acceleration of chemical conversion

Suspension Preparation

Depolymerization

,

Lyzing

, ReactionSlide6

Research Focus1. Determine viscosity changes on model rheological fluids by applying acoustic cavitation methods using a broad spectrum transducer

2. Perform Cavitation Yield Measurements to determine the effect of change in Acoustic Frequency and Power on C

hemical Conversion using a single broad spectrum transducer. Slide7

Experimental Setup for Acoustic Cavitation

Ultrasonic waves were generated at 378, 574, 850, and 1125 kHz using a broad spectrum transducer

for a solution volume of 200 ml held within a jacketed glass water cooled column.

Laboratory experiments were performed (1) to determine viscosity changes with a CMC-Water 0.7 wt % mixture at 1000 cP

at 2.5 RPM and (2) Cavitation yield determination with 0.1 and 1% (wt) KI solution.Slide8

Visualization of 850 KHz. SonicationSonication at high frequencies (850Khz. and above),

leads to the formation of a fountain jet at the surface of the liquid, releasing droplets from the surface of the jet.

Sonication Frequency

Jet Diameter

Jet Height

850KHz.

3 cm.

3 cm.

1.125

MHz.

1.5 cm.

4 cm.Slide9

Results –Change in Viscosity as a function of Sonication Time

Change in viscosity for 0.7 wt% CMC-water mixture over a range of

sonication frequenciesSlide10

Results - Cavitation Yield Measurements

Cavitation yield

over a range of sonication frequencies using

(a) 0.1

wt

%

KI solution and (b) 1% KI solution at constant power input

(a)

(b)

Cavitation Yield as a Function of Sonication TimeSlide11

Results – Cavitation Yield Measurements

Cavitation Yield increases at higher power input. Sonication time influences the

KI decomposition.

Cavitation Yield as a Function of Input PowerSlide12

Summary of FindingsLower

sonication frequencies during acoustic cavitation generate larger rheological changes.

Viscosity

reduces rapidly with sonication time

at lower acoustic frequencies as compared to higher frequencies.

Cavitation yield measurements do not follow the same trend

.

KI decomposition was

determined to be the highest at a sonication time of 25 minutes at a frequency of 574 kHz. Slide13

ConclusionRheological changes and KI decomposition were examined and found to be uncorrelated using

a broad spectrum acoustic system in the present study.The application of

acoustic cavitation to model fluids is to be further extended to oil sands feed and tailings to

develop the criteria for extraction and/or transportation of oil sands at the laboratory scale up for commercial processing.Slide14

Acknowledgements:This Research is Funded by Eco-EII Canada Research Fund