IRJET- A Research Paper on Design and Experimentation on Continuous Loop Demulsifier

International Research Journal of Engineering and Technology (IRJET) e-ISSN: 2395-0056
Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072
© 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 902
A RESEARCH PAPER ON DESIGN AND EXPERIMENTATION ON
CONTINUOUS LOOP DEMULSIFIER
Divij Gupta1, Ketan Singhvi2
1,2B.E. Mechanical
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Abstract - This paper explains the working of an Electrocoalescer used to separate water from crude oil. This separation is of
utmost importance and economic relevance affecting the quality of crude oil. The water present in crudeoilenhancescorrosion in
refineries, reduces quality of crude oil and its by-products, and catalysis occurs. Hence we have developed a practical andlowcost
model of an electrocoalescer that increases the demulsification rate and improves the oil quality.
Key Words: electrocoalescer, crude oil, demulsification, catalysis
1. INTRODUCTION
India imports more than 82% of its oil needs. Oil water separators or demulsifiers are hence of great importance today.Water
molecules induced during extraction of crude oil from 4000 m below sea level, form an emulsion with the oil thatcorrodesthe
process equipment, drastically reduces oil quality and may render it poisonous. Therefore it is necessary to keep the water
below 0.3% by volume and salt below 10 lbs PTB (per thousand barrels). Other separation processes like gravity separation,
chemical demulsification, centrifugal separation etc. used currently either have high maintenance and running costs or low
production rates.
Hence we are developing an electrostatic separator that is continuous. It will maintain theindustrystandardsofcrudeoil.Also
electrocoalescer will potentially reduce the cost of production of petroleum products. Highvoltageelectricityisusedtoinduce
opposite dipole charges in small water droplets and coalesce the water droplets so that they fall under the action of gravity
2. LITERATURE REVIEW
In [1], the researchers showed that the dependency of water drop in emulsion (waterandoil)inconductivityforspecificphase
of medium. The researchers used two method to do this experiment, one was cone-dimple method and other was cone-spray
method. In the experiment of cone-dimple method was performed under the silicon oil and this was done by increasing its
conductivity and inserting peperazine and D130. But the reason behind performing this experiment was difficulttoexplainas
per the researchers, but they assumed that this can be due to high conductivity of medium to form the jet, unlike the dielectric
medium. Thus, they concluded that this happen because the charge travel between the high conductivitymediumandbecause
of this it generates the tangential stress at the interface which results in formation of jet.
From this experiment that have observed that the coalescence of oil in a medium, cone dimple method is dielectric in medium
conductivity due to properties of crude oil, and concluded thathowelectricfielddependsoncoalescencemethodthataffect the
construction of parts like desalters and dehydrators and separation of water.
In [2], the authors shows that how the water drops id separated due to electrocoalescence process. This process can get more
efficient by different methods like applying gravity, improvement in Stokeslet interaction in hydrodynamics, applying high
electrostatics, electric field which is dependable that can be accomplished by high conductivity of drop. Hence, the authors
finally concluded that in electrocoalescer process separation of drop can be achieved by verified experimental data.
In [3], the researchers checked the coalescence of uniform and non-uniform electric field in two mixture(water-in-oil mixture
and oil-in-oil mixture). By the data the researchers observed that in water-in-oil mixture, the uniform and symmetric non-
uniform electric is less advantages than the asymmetric non-uniform electric field and in case of oil-in-oil mixture it was
completely opposite. Hence, the researchers concludedthatforoptimumresultstheelectrodeshouldbecoatedsothattheycan
produce more asymmetric electric field and dependency of efficient electrode is on properties of dispersed and continuous
phase.
In [4], the researchers shows that the angle between two drops should be less than 54.7˚ and 125.3˚ so that the electric fieldto
be largest. From the experimental data they observed that at 0˚ angle the surface of drops can go under deformation that are
facing each other. From this experiment researchers also understood that 2-D electrode can be designed by inducing electric
field that is perpendicular between the imaginary lines drawn from center of two drops. The experimental data showed the
researchers that the drop will vibrate when the electric field is same as the applied pulsed frequency. If the frequency is not

same that the drop will have small magnitude of vibration because this depends on continuous liquid phase. Hence, by these
experimental data researchers concludedthatelectricfieldisnecessaryforwaterdropletsseparationandalsoshowsthebetter
design of electrocoalescer that can be developed so that it becomes more efficient.
3. MATERIAL AND COMPONENTS
3.1 Distributor:
A hollow tube with holes in staggered position is used to properlydistributetheflowof emulsionintheElectrocoalescervessel.
This ensures that separation starts as soon as emulsion leaves the distributor, since due to a uniform flow across the vessel
length more emulsion is in contact with the electric field.
Material used: SS304
Dimensions: OD - 12 mm
ID - 7 mm
Orifice diameter - 1 mm
Length - 400 mm
Fig -1: Distributor
3.2 Collector:
A hollow tube with holes in staggered position with a pipe in the middle is used to collect pure oil after separation. Since oil is
less dense it enters the collector from underneath through the holes and exits through the pipe due to pressure exerted on it.
Dimensions: OD- 16 mm
ID- 10 mm
Orifice diameter- 6 mm
Pipe diameter: OD- 8 mm
ID- 6 mm

Fig -2: Collector
3.3 Bigrid Electrodes:
Two Grid shaped Electrodes are used to create a uniformly distributed electrostatic field in the entire vessel. This grid or
antenna shape allows for a much strong and uniform electrostatic field. The voltage applied depends on the distance between
the surfaces of these electrodes, which is to be roughly 1 kV/cm or more.
Dimensions: Main Rod Diameter- 10 mm
Length- 340 mm
Grid Rod Diameter- 6 mm
Length- 120 mm
Pitch of Grid Rods- 20 mm
Fig -3: Bigrid Electrodes
3.4 Pump:
A reciprocating plunger pump (dosing) is used to pump the emulsion in the vessel via the distributor.
Specifications:
Company- Positive Metering Pumps Pvt. Ltd.
Capacity- 5-30 lph (variable flow rate)

Pressure- 5 kg/cm2
Fig -4: Pump
3.5 Electrocoalescer Vessel:
An acrylic vessel is used to mount all the components of the demulsifier and inspect the separation of the two liquids.
Components are mounted in the following order from top to bottom- Collector, Electrode, Distributor, Electrode.In thisvessel
the actual coalescence and separation occurs.
Material used: Acrylic
Dimensions: Outer Diameter- 190 mm
Thickness- 5 mm
PCD for fasteners- 250 mm
Fig -5: Electrocoalescer Vessel
3.6 High Voltage Amplifier:
A High Voltage Amplifier is used to achieve desired voltage at the desired frequency. The voltage gain in the amplifier used is
2000.

Fig -6: High Voltage Amplifier
4. WORKING PRINCIPLE
A Demulsifier/Electrocoalescer works on the principle of electrophoresis. Due to the uniform electrostatic field between two
electrodes, an electric dipole charge is induced in the micro droplets present in the crude oil resulting in a charge density. The
polarity of the dipole charge developed in any droplet depends on the proximity of that droplet to the electrode. The droplets
near the positive electrode develop a positive dipole and droplets near the negative electrode develop a negative dipole. The
opposite dipole charges and charge density between carrying fluid and micro-droplets act on droplets causing them to move
and coalesce to form large drops of water sedimenting quickly under theduetogravity. Thiswateristhendrainedviathedrain
valve. The separation percentage of water and its residence time depends upon various factors like intensity of electric field,
flow rate of emulsion, electronic configuration etc.
Fig -7: Diagrammatic Representation of Continuous Loop Demulsifier
5. WORKING OF CONTINUOUS LOOP DEMULSIFIER
In this project we have built a model of Continuous Loop Demulsifier for experimentation and simulation purposes. The oil-
water emulsion is prepared by mixing both liquids in an emulsion tank andcontinuous stirring.Thisemulsionispumpedusing
a metered dosing pump in the electrocoalescer vessel via the distributor. The two phase emulsion getsseparatedin thisvessel
due to the electrostatic field. The higher density water is drained through the drain valve in a water collector. While the lower
density oil is collected in a separate tank via the collector.

6. EXPERIMENT SPECIFICATIONS
1) Emulsion contents: 9000 mL oil (Sunflower Oil)
1160 mL water (Milli-Q Water)
2) Minimum Water level: 160 mL
3) This water is grounded for better electric field in the lower half of the vessel.
4) Electric Configuration- Alternate electrodes live ground and vessel floating.
5) Position of components- Distributor is up with holes in horizontal plane.
6) Pump used- Reciprocating Pump: Capacity - 0-25 Lph
Pressure- 5 kg/cm2
7) Setting of Amplifier: Voltage- 5000 V AC
Frequency- 50 Hz
7. METHODOLOGY OF EXPERIMENTATION
1) Preparation of Emulsion:
An oil-in-water emulsion is prepared by mixing 90% oil and10%water. Thismixtureishomogenizedusinga highspeedstirrer
for 3 minutes. A white homogenous emulsion is formed.
Emulsion contents: 9000 mL oil
1000 mL water
Fig -8: Homogenization of emulsion
2) Assembly and Preparation of Setup:
The Electrocoalescer setup is assembled according to the required electric configuration to be used. We have used Alternate
Live Ground Vessel Ground configuration for maximum separation and lowest residence time.
Voltage Applied- 5000 V AC

Frequency- 50 Hz
Fig -9: Schematic Diagram of Alternate Bigrid Live Ground and Vessel Ground
3) The emulsion is pumped into the coalescer vessel at a rate of 0.3 lph and the stopwatch is started. The experiments is
conducted for about 30 minutes.
4) The Grid Electrodes are supplied with 5000 V of electricity using a high voltage amplifier.
5) During the experiment as separation occurs, the oil is collected in an oil tank. Within regular intervals of 3 minutes
samples are collected in numbered sampling tubes.
6) The collected samples are then tested for water percent by volume using Karl Fischer’s titration.
7) Karl Fischer’s Titration:
Toluene, Dried Methanol, Chloroform and Karl Fischer’s Solution are poured in required quantitiesintheapparatus’ flask.The
setup and stirrer is started and approximately 30 drops of sample oil is poured in the flask using a syringe.
Fig -10: Karl Fischer’s Titration Apparatus and Solutions
8) The percentages of water in the oil samples are noted and plotted against time.

Fig -11: Experimental Setup of Continuous flow Electrocoalescer
8. RESULTS
8.1 Observations:
1) The water droplets start to coalesce as soon as the emulsion enters the electric field.
2) The droplets coalesced and form bigger drops.
3) These drops fall under the action of gravity and water gets collected in the lower part of the vessel due to higher
density.
4) Pure unadulterated oil is collected through the collector in a separate tank.
5) Total water used-1160 mL
Total water separated-1100 mL
Percentage of water separated~95%

Figure 12: Water drops coalescing and Figure 13: Water after separation
Falling under gravity
8.2 Results of Karl Fischer’s Titration:
Table 1: Karl Fischer’s Titration Result
Sample Number Weight (mg) Volume Displaced (mL) % Moisture by weight in
collected oil
1 127.07 0.294 1.1744
2 129.60 0.289 1.1358
3 121.69 0.287 1.2013
4 132.46 0.261 1.0039
5 121.54 0.457 1.9128
6 131.19 0.180 0.6964
7 144.10 0.284 1.0003
8 136.78 0.010 0.0371
9 167.61 0.294 0.8903
10 130.95 0.292 1.1318
1) Maximum percentage of moisture- 1.9128%
2) Minimum percentage of moisture- 0.0371%
3) Average percentage of moisture- 1.0184%

Chart -1: Sample number v/s percentage separation of water
9. CONCLUSIONS
1) The experimental setup successfully demulsifies the water-in-oil emulsion in a continuous loop.
2) Since there was no sparking in the setup, the electric field of 1 kV/cm is apt for electrocoalescence.
3) Satisfactory percentages of separation were achieved during the experimentation.
10. FUTURE SCOPE
1) Further experiments are to be conducted to find:
a) Variation of percentage of coalescence with change in frequency.
b) Dependence of separation and quality of oil on the flow rate of emulsion.
c) Residence time, position of distributor, electric field dependency on percentage water cut in emulsion.
2) Further analysis on optimum size of water droplets for coalescence to occur.
3) Designing of experiments to reduce sparking in coalesce due to water chain formation.
4) Design and development of systems with higher flow rate and lower residence time for faster production rate.
11. REFERENCES
1) “Modes of coalescences of aqueous anchored drops in insulating oil under electric field.” Prof. Vikky Anand, Vinay
Juvekar, Rochish Thaokar Date of Publication: 03 February 2019, Volume 568
https://www.sciencedirect.com/science/article/abs/pii/S0927775719300822
2) “Modelling and particle simulation of electrocoalescence of a water in oil emulsion.” Prof. Vikky Anand,RoshanPatil,
Vijay M. Naik, Vinay A. Juvekar, Rochish M. Thaokar Date of Publications: 04 December 2018, Volume 121
https://www.sciencedirect.com/science/article/pii/S0098135418312754
3) “Electro-coalescence in non-uniform electric field.” Prof. Sameer Mhatre, Rochish M. Thaokar DateofPublications:25
July 2015, Volume 96 https://www.sciencedirect.com/science/article/abs/pii/S0255270115300763
4) “Drop-drop coalescence in an electric field: the effect of applied electric field and electrode geometry.” Prof. John S.
Eow, Mojtaba Ghadiri Date of Publications: 23 January 2003, Volume 219,
https://www.sciencedirect.com/science/article/abs/pii/S0927775703000517
5) https://en.m.wikipedia.org/wiki/Oil_and_gas_industry_in_India

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