Petroleum disperse systems
Classification of disperse particles in ODS
Energy and power aspects of surface (interfacial)* tension
Figure. The interface between a liquid and a gas
Figure. The interface between two liquids (Rosen, 1989).
Surface tension in some liquids
Schematic illustration of a surfactant molecule
Lyophilic and lyophobic ODS
Composite ODS
After-effect of asphaltens deposits in case of crude production
Basic conditions, which determine risk of asphaltens setting out in PTA (pig trap area)
Deposition of asphaltenes in a pipeline wall
Naphthenate deposition problems at the Heidrun platform
Pigging operation to remove wax from the Norwegian shelf
Production
Recovery and transport
Refining
1.24M
Category: industryindustry

Petroleum disperse systems. (Lecture 3)

1. Petroleum 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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2. Classification of disperse particles in ODS

Characteristic of classification
The names of disperse particles
Size of particles:
1-100 nm
100 nm – 1 mkm
1-10 mkm
Ultradisperse (nanoparticles)
Finely dispersed powder
Сoarsely dispersed
Forms of particles:
The length, width and thickness of the particles are
approximately the same, ranging from 1 nm to 10
mkm
The thickness of the particles is about 1 nm-10
microns, the length and width is more than 100
microns
Cross-sectional diameter is about 1 nm -10 microns
Volume (3D)
Chemical composition of particles
Nonorganic(salts, mechanical impurities)
Organic(paraffins, fullerenes, adamantanes )
Superficial (2D): for example thin films and layers
Line (1D): thin fibres
Structure of particles
Hard particles, liquid drops and films, gas bubbles
Micelles from the molecules of surface-active
substances; clusters
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Phasic
Pseudophasic (colloid)
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3.

Примеры НДС по форме дисперсных частиц
Размерность
Форма
Примеры НДС
Трехмерный
Твердые частицы, капли,
Нефти, нефтяные остатки, эмульсии,
пузырьки
пены
Двухмерный
Пленки
Нефтяные пленки на воде, смазочные
материалы на металлической
поверхности
Одномерный
нити, волокна, поры,
Нефти в пористых средах, углеродные
капилляры
волокна, нефтеполимерные материалы,
анизотропные коксы
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4.

What is NANO?
powders
layers (films)
NANO
structures (pores, grain size…)
composites
VS
Media
VB
VB ~ VS
particle
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5. Energy 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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6. Figure. The interface between a liquid and a gas

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

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8. Surface tension in some liquids

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9. Schematic illustration of a surfactant molecule

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10. Lyophilic 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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11. Composite 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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12. After-effect of asphaltens deposits in case of crude production

Decrease of PTA penetration of well
Decrease of PTA penetration
Decreasing of flow area of wells
elevator and oilfield pipeline;
After 2-3 months
нефть
Bottom deposits accumulation in
reservoirs, separators and etc.
Асфальтены


Pпл
Deposits on pipeline sides
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13. Basic 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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14. Deposition of asphaltenes in a pipeline wall

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15. Naphthenate deposition problems at the Heidrun platform

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16. Pigging operation to remove wax from the Norwegian shelf

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17. Production

• Asphaltum-resinsparaffin deposit
(ARPD)
• Clogging of oil
reservoir pores
(skin-effect)
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18. Recovery and transport

Water-oil emulsions
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19. Refining

Change of states in
processing vessels and in
coilers of pipe heaters
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