Petroleum disperse systems. (Lecture 3) презентация

Classification of disperse particles in ODS 14/09/16 lecture 3

Слайд 1Petroleum disperse systems

The PDS classification
Nanoparticles in PDS
Lyophilic and lyophobic

PDS. Shchukin-Rehbinder criterion
Some challenges of Petroleum Industry, connected with PDS exploitation, treatment, transport and refining




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Слайд 2Classification of disperse particles in ODS
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Слайд 314/09/16
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Слайд 4
What is NANO?
NANO
Media


particle
VB
VS
VB ~ VS
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Слайд 5Energy and power aspects of surface (interfacial)* tension
The compensate of intermolecular

interactions on the phase boundary leads to the fact that the phase boundary surface has an uncompensated excess energy (energy aspect), σ [erg/cm2, J/m2] and causes the appearance of a tangential force (power aspect), σ [din/cm, N/m]
* The term "interphase boundary" is usually attributed to the boundary between two immiscible phases, the term "surface" indicates that one of the phases is a gas, usually air

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Слайд 6Figure. The interface between a liquid and a gas

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Слайд 7Figure. The interface between two liquids (Rosen, 1989).

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Слайд 8Surface tension in some liquids

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Слайд 9Schematic illustration of a surfactant molecule

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Слайд 10Lyophilic and lyophobic ODS
ODS can be divided on lyophilic and

lyophobic due to value
of interfacial interactions at the interface

Shchukin-Rehbinder criterion 4πr2σ ~ γkT,where
r - particle size,
T-temperature,
K - Boltzmann constant,
 - dimensionless coefficient


Calculation shows, that at standart conditions
σcrit~ 0,01-0,1 mN/m

Lyophilic ODS σ < σcrit
Lyophobic ODS σ > σcrit


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Слайд 11Composite ODS
Five interfaces:

Solid body – gas (surface)
Solid body -

liquid (interphase boundary)
Solid body – solid body
liquid – gas (surface)
liquid-liquid (interphase boundary)

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Слайд 12 After-effect of asphaltens deposits in case of crude production
Deposits on

pipeline sides

Decrease of PTA penetration
Decreasing of flow area of wells elevator and oilfield pipeline;
Bottom deposits accumulation in reservoirs, separators and etc.

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Слайд 13Basic conditions, which determine risk of asphaltens setting out in PTA

(pig trap area)

Changing of thermobaricе conditions in PTA;
Рпл – Рн > 8 – 10 МPа;
Presence of contamination;
Formation of trolly-oil;
Practice of incongruent chemicals (isopropil alcohol, methanol, propanone, solvents);
Acid treatment and other chemical methods of intensification of oil inflow from the bench

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Слайд 14Deposition of asphaltenes in a pipeline wall

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Слайд 15Naphthenate deposition problems at the Heidrun platform

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Слайд 16Pigging operation to remove wax from the Norwegian shelf


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Слайд 17Production
Asphaltum-resins-paraffin deposit (ARPD)

Clogging of oil reservoir pores
(skin-effect)
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Слайд 18Recovery and transport
Water-oil emulsions
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Слайд 19Refining

Change of states in processing vessels and in coilers of pipe

heaters

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