Crystal Sea Crystal Sea Oil Oil Oily Oily-Water Separators W t - - PowerPoint PPT Presentation

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Crystal Sea Crystal Sea Oil Oil W t S t W t S t Oily Oily-Water Separators Water Separators

SLIDE 2

The instrumentation and controls are user The instrumentation and controls are user-

• friendly and include

friendly and include carefully selected components for exceptional reliability. carefully selected components for exceptional reliability. In custom In custom-built units Crystal Sea separators can be integrated built units Crystal Sea separators can be integrated In custom In custom built units Crystal Sea separators can be integrated built units Crystal Sea separators can be integrated into complex automation systems being operated and monitored from a central into complex automation systems being operated and monitored from a central location. location. Explosion Explosion-proof automation (Class I Div. I) for the oil industry is available upon proof automation (Class I Div. I) for the oil industry is available upon Explosion Explosion proof automation (Class I Div. I) for the oil industry is available upon proof automation (Class I Div. I) for the oil industry is available upon request. request. Crystal Sea separators typically achieve effluent purities of less than 5 mg/l for 0 Crystal Sea separators typically achieve effluent purities of less than 5 mg/l for 0-

• 100% oil in water mixtures and relative oil densities of up to 0.985. A specially

100% oil in water mixtures and relative oil densities of up to 0.985. A specially 100% oil in water mixtures and relative oil densities of up to 0.985. A specially 100% oil in water mixtures and relative oil densities of up to 0.985. A specially designed oil dome is also available to reduce the oil content to 5 mg/l at angles of designed oil dome is also available to reduce the oil content to 5 mg/l at angles of inclination of up to 22.5 inclination of up to 22.5O in stormy conditions. in stormy conditions.

SLIDE 3

Introduction Introduction

Genoil Crystal Sea oily Genoil Crystal Sea oily-

• water separators utilize a patented, unique process for multi

water separators utilize a patented, unique process for multi-

• stage separation of immiscible phases with different densities such as mineral oils and

stage separation of immiscible phases with different densities such as mineral oils and water An innovative separation process combines gravitational and centrifugal forces water An innovative separation process combines gravitational and centrifugal forces

• water. An innovative separation process combines gravitational and centrifugal forces
• water. An innovative separation process combines gravitational and centrifugal forces

with surface tension and vortex effect prior to the polishing stage. A highly effective with surface tension and vortex effect prior to the polishing stage. A highly effective polishing stage enhances performance and minimizes maintenance costs and downtime. polishing stage enhances performance and minimizes maintenance costs and downtime. Crystal Sea separators are designed for ships and have been certified by the US Coast Crystal Sea separators are designed for ships and have been certified by the US Coast G d i d ith IMO R l ti MEPC 107(49) G d i d ith IMO R l ti MEPC 107(49) Guard in accordance with IMO Resolution MEPC. 107(49). Guard in accordance with IMO Resolution MEPC. 107(49). The separator components meet or exceed the rigorous specifications of classification The separator components meet or exceed the rigorous specifications of classification societies and all Crystal Sea MU models are ABS certified. The units are precision built societies and all Crystal Sea MU models are ABS certified. The units are precision built by Donghwa Entec of Busan, Korea, a company specializing in marine equipment since by Donghwa Entec of Busan, Korea, a company specializing in marine equipment since 1980. 1980. Due to their high efficiency the separators are compact and need access only from the Due to their high efficiency the separators are compact and need access only from the front side. They can also be placed against the wall, even in corners and do not require front side. They can also be placed against the wall, even in corners and do not require any extra head room. any extra head room. The automation system ensures unattended operation and features PLC units, self The automation system ensures unattended operation and features PLC units, self-

• cleaning oil sensors and fail

cleaning oil sensors and fail-

• safe components.

safe components.

SLIDE 4

Process Flow Diagram Process Flow Diagram Description Description

The separation process occurs in six stages in fluid communication with each other as The separation process occurs in six stages in fluid communication with each other as shown below. Oil is gradually removed in each stage and collected in oil zones A, B and shown below. Oil is gradually removed in each stage and collected in oil zones A, B and C ti l h i Fi 1 C ti l h i Fi 1 C respectively, as shown in Fig.1. C respectively, as shown in Fig.1. Periodically, a preset amount of oil is detected by oil sensors, which initiate an oil Periodically, a preset amount of oil is detected by oil sensors, which initiate an oil discharge sequence. The liquid flow through the stages is reversed and oil accumulated discharge sequence. The liquid flow through the stages is reversed and oil accumulated in the collection ones is then discharged into a aste oil tank in the collection ones is then discharged into a aste oil tank in the collection zones is then discharged into a waste oil tank. in the collection zones is then discharged into a waste oil tank.

SLIDE 5

A: Oil collection area (1st stage) A: Oil collection area (1st stage) B: Oil collection area (2nd stage) B: Oil collection area (2nd stage) C: Oil collection area (3rd stage) C: Oil collection area (3rd stage) V1: Oil outlet valve (1st stage) V1: Oil outlet valve (1st stage) V2: Oil outlet valve (2nd stage) V2: Oil outlet valve (2nd stage) V7: By V7: By-

• pass valve

pass valve P1, P2, P3: Pressure gauges P1, P2, P3: Pressure gauges HP: High oil probe HP: High oil probe LP: Low oil probe LP: Low oil probe RP: Reference probe RP: Reference probe V2: Oil outlet valve (2nd stage) V2: Oil outlet valve (2nd stage) dP: Oil outlet valve (3rd stage) dP: Oil outlet valve (3rd stage) V3: Inlet valve V3: Inlet valve V4: Effluent outlet valve V4: Effluent outlet valve V5: Air supply valve V5: Air supply valve V6: Water supply (back V6: Water supply (back-

• flushing) valve

flushing) valve RP: Reference probe RP: Reference probe VC1, VC2, VC3: Vent cocks VC1, VC2, VC3: Vent cocks FM: Flow meter FM: Flow meter ADP: Air diaphragm pump ADP: Air diaphragm pump PR1, PR2: Pressure reducers PR1, PR2: Pressure reducers PRV: Pressure relief valve PRV: Pressure relief valve

SLIDE 6

S ti P S ti P Separation Process Separation Process

The Crystal Sea oily The Crystal Sea oily-

• water treatment units are designed to separate the liquid phases

water treatment units are designed to separate the liquid phases in six stages located within a single vessel. Each stage is devised to remove oil particles in six stages located within a single vessel. Each stage is devised to remove oil particles

• f a certain size and renders the liquid cleaner for the next stage. This ensures greater
• f a certain size and renders the liquid cleaner for the next stage. This ensures greater

effectiveness and manageable loads for each stage. Furthermore, it also precludes effectiveness and manageable loads for each stage. Furthermore, it also precludes undue contamination and clogging of various stages by oil, resulting in trouble free undue contamination and clogging of various stages by oil, resulting in trouble free-

• peration.
• peration.

Minute gas bubbles resulting from controlled vacuum conditions enhance the removal Minute gas bubbles resulting from controlled vacuum conditions enhance the removal

• f oil droplets from the water stream. Vacuum is created in the stages operating prior
• f oil droplets from the water stream. Vacuum is created in the stages operating prior

to the circulation pump. Oil is retained at the upper portion of the stages and is to the circulation pump. Oil is retained at the upper portion of the stages and is gradually accumulated in collection zones. gradually accumulated in collection zones. Downstream from the pump the stages are slightly pressurized. Oil extracted in these Downstream from the pump the stages are slightly pressurized. Oil extracted in these stages is transferred continually into the collection zones through specially designed stages is transferred continually into the collection zones through specially designed

• conduits. The transfer of oil occurs due to the pressure differential existing between
• conduits. The transfer of oil occurs due to the pressure differential existing between

the stages located upstream and downstream from the pump respectively. Continual the stages located upstream and downstream from the pump respectively. Continual

• il extraction ensures outstanding cleanliness of the polishing stages and prevents
• il extraction ensures outstanding cleanliness of the polishing stages and prevents

accidental contamination of the effluent. accidental contamination of the effluent.

SLIDE 7

Oil accumulation in the collection zones is monitored by a probe that initiates Oil accumulation in the collection zones is monitored by a probe that initiates periodic oil discharge sequences. periodic oil discharge sequences. The separator is isolated from the effluent discharge line and connected to a The separator is isolated from the effluent discharge line and connected to a The separator is isolated from the effluent discharge line and connected to a The separator is isolated from the effluent discharge line and connected to a pressurized line. Clean water back pressurized line. Clean water back-

• flushes the stages and displaces the oil from the

flushes the stages and displaces the oil from the collection zones. The oil probe resumes the separation process after a preset amount collection zones. The oil probe resumes the separation process after a preset amount

• f oil is evacuated.
• f oil is evacuated.

The first stage achieves oil The first stage achieves oil-water separation through gravity enhanced through a water separation through gravity enhanced through a The first stage achieves oil The first stage achieves oil-water separation through gravity, enhanced through a water separation through gravity, enhanced through a flotation effect by minute gas bubbles. A specially designed device imparts a rapid flotation effect by minute gas bubbles. A specially designed device imparts a rapid circular motion to the liquid. Oil migrates to the centre of the device and then circular motion to the liquid. Oil migrates to the centre of the device and then ascends, accumulating progressively in a collection zone (A). Solids and sludge are ascends, accumulating progressively in a collection zone (A). Solids and sludge are deposited at the bottom of the stage for removal Most of the oil droplets are removed deposited at the bottom of the stage for removal Most of the oil droplets are removed deposited at the bottom of the stage for removal. Most of the oil droplets are removed deposited at the bottom of the stage for removal. Most of the oil droplets are removed in this stage. in this stage. The flow is reversed prior to the liquid entering the second stage which contains The flow is reversed prior to the liquid entering the second stage which contains

• leophilic material. Small particles of oil adhere to the surface of the oleophilic beads
• leophilic material. Small particles of oil adhere to the surface of the oleophilic beads

and are attracted to them by a surface tension effect As they get together the oil and are attracted to them by a surface tension effect As they get together the oil and are attracted to them by a surface tension effect. As they get together, the oil and are attracted to them by a surface tension effect. As they get together, the oil droplets form larger globules whose enhanced buoyancy overcomes the force of droplets form larger globules whose enhanced buoyancy overcomes the force of attraction exerted by the beads. The oil globules then detach themselves from the attraction exerted by the beads. The oil globules then detach themselves from the beads, move upwardly with the liquid and remain in the secondary collection zone (B) beads, move upwardly with the liquid and remain in the secondary collection zone (B) for removal for removal for removal. for removal.

SLIDE 8

This stage is designed to allow continual agitation of the beads in order to accelerate This stage is designed to allow continual agitation of the beads in order to accelerate g g g g g g the coalescing process and facilitate the self the coalescing process and facilitate the self-

• cleaning of the beads. The flow is

cleaning of the beads. The flow is reversed through a circular motion at the upper part of the second stage and oil reversed through a circular motion at the upper part of the second stage and oil remains in the secondary collection zone (B). remains in the secondary collection zone (B). The liquid is further processed in the third stage entering the core of a circular basket The liquid is further processed in the third stage entering the core of a circular basket and moving radially outwards through the coalescing material. Liquid velocity and moving radially outwards through the coalescing material. Liquid velocity decreases towards the periphery of the basket thus allowing minute oil particles to decreases towards the periphery of the basket thus allowing minute oil particles to coalesce effectively. The resulting oil globules are retained in a collection zone (C) as coalesce effectively. The resulting oil globules are retained in a collection zone (C) as the liquid reverses its motion and descends towards the fourth stage. the liquid reverses its motion and descends towards the fourth stage. A positive displacement pump delivers the liquid to the fourth stage for further A positive displacement pump delivers the liquid to the fourth stage for further separation by means of a vortex separation by means of a vortex-

• generating device. Centripetal forces within the

generating device. Centripetal forces within the vortex agglomerate the oil particles and force them to coalesce in order to form larger vortex agglomerate the oil particles and force them to coalesce in order to form larger

• globules. Furthermore, an effect similar to one created by a cyclone also agglomerates
• globules. Furthermore, an effect similar to one created by a cyclone also agglomerates

the oil particles thus enhancing the coalescing process. A perforated conduit retrieves the oil particles thus enhancing the coalescing process. A perforated conduit retrieves the globules from the eye of the vortex and directs them to a dispersion plate placed the globules from the eye of the vortex and directs them to a dispersion plate placed above the vortex generator. above the vortex generator.

SLIDE 9

Oil particles then travel through suitably sized perforations in the dispersion plate, Oil particles then travel through suitably sized perforations in the dispersion plate, gather around a funnel and migrate toward the oil collector of the first stage. gather around a funnel and migrate toward the oil collector of the first stage. Spinning liquid rapidly exits the vortex generator being deflected downwards by the Spinning liquid rapidly exits the vortex generator being deflected downwards by the dispersion plate. dispersion plate. Further separation of minute oil particles occurs in the fifth stage by means of surface Further separation of minute oil particles occurs in the fifth stage by means of surface tension within a specially designed device. The liquid flows radially though the device tension within a specially designed device. The liquid flows radially though the device and the oil particles are forced to form clusters of larger globules. The liquid is then and the oil particles are forced to form clusters of larger globules. The liquid is then directed around a circular baffle devised to create a quiet zone above the device. Oil is directed around a circular baffle devised to create a quiet zone above the device. Oil is readily left behind and then drawn into the first stage as the flow is reversed and cleaner readily left behind and then drawn into the first stage as the flow is reversed and cleaner liquid is transferred to the final filtration stage. liquid is transferred to the final filtration stage. In most cases the separation is completed prior to this stage. However, for oils of In most cases the separation is completed prior to this stage. However, for oils of unusually high density, the sixth stage retains the remaining particles by means of unusually high density, the sixth stage retains the remaining particles by means of

• filters. The filters are designed to retain temporarily minute particles of oil on their
• filters. The filters are designed to retain temporarily minute particles of oil on their
• surface. The particles coalesce and detach themselves from the filter media through
• surface. The particles coalesce and detach themselves from the filter media through

their enhanced buoyancy and the sweeping effect of the liquid. their enhanced buoyancy and the sweeping effect of the liquid. Thus filter media lifespan can be prolonged to significant periods of time. This is due to Thus filter media lifespan can be prolonged to significant periods of time. This is due to minimizing the amount of oil particles reaching the filter media and effective oil minimizing the amount of oil particles reaching the filter media and effective oil removal from the surface of the media. removal from the surface of the media.

SLIDE 10

Main Features

Out 1/4"

• OK

+ DEKMA HAMBURG DH 75450 Clean water 1/4" ON ALARM 1 ALARM 2 SYSTEM

H

Figure 2 Figure 2

D L

• 1. Oily
• 1. Oily-
• water inlet

water inlet

• 2. Oil outlet
• 2. Oil outlet
• 3. High Probe
• 3. High Probe
• 4. Low Probe
• 4. Low Probe
• 6. Oil outlet 2nd stage
• 6. Oil outlet 2nd stage

14 . By 14 . By-

• pass valve

pass valve 15a, 15b, 15c. Vent cocks 15a, 15b, 15c. Vent cocks 16 Rotameter 16 Rotameter

• 18. Back
• 18. Back-
• flush valve

flush valve

• 19. Pressure gauge P2
• 19. Pressure gauge P2

g

• 7. Reference probe
• 7. Reference probe
• 8. Oil outlet 3
• 8. Oil outlet 3rd

rd stage

stage

• 12. Pump
• 12. Pump
• 20. Pressure reducer PR2
• 20. Pressure reducer PR2
• 21. Effluent outlet valve
• 21. Effluent outlet valve
• 22. Diverter valve
• 22. Diverter valve

SLIDE 11

Specifications Specifications Specifications Specifications

Model Max. Capacity H Height L Length D Depth Inlet line Effluent Line Oil Outlet inch Power KW Weight kg Capacity l/h Height mm Length mm Depth mm line inch Line inch inch KW kg MU 2 250 550 600 230 3/8 3/8 3/8 0.5 150 MU 5 500 945 1215 485 3/4 3/4 1 0.75 365 MU 10 1000 1200 1500 660 1 3/4 3/4 1 450 MU 15 2000 1415 1700 780 1 3/4 1 1.5 900 MU 20 3000 1730 2200 955 1 1 1 2.5 1250 MU30 5000 1730 2200 955 1 1/4 1 1 3 5 1350 MU30 5000 1730 2200 955 1 1/4 1 1 3.5 1350 MU40 10000 2200 2800 1200 2 1 1/2 1 1/2 5 2200

SLIDE 12

Advantages: Advantages:

• Unique six

Unique six-

• stage design for high

stage design for high-

• efficiency and performance

efficiency and performance

• Low downtime, maintenance and operating costs

Low downtime, maintenance and operating costs

• Outstanding reliability

Outstanding reliability

• Very compact units for applications where space is at a premium

Very compact units for applications where space is at a premium

• Simple, unattended operation

Simple, unattended operation

• Versatility for a wide range of applications

Versatility for a wide range of applications

SLIDE 13

Applications: Applications: Applications: Applications:

• Bilge water separation for sea

Bilge water separation for sea-

• going vessels

going vessels

• Off

Off-

• shore oil platforms

shore oil platforms

• Wastewater treatment plants

Wastewater treatment plants

• Refineries

Refineries

• Gasoline/Diesel service stations

Gasoline/Diesel service stations Crystal Sea MU 20 Unit Crystal Sea MU 20 Unit

SLIDE 14

Testimonials Testimonials

The C.E.O of Enviremedial Services Inc. (E.S.I.), Mr. Chris Keogh of Vista, The C.E.O of Enviremedial Services Inc. (E.S.I.), Mr. Chris Keogh of Vista, California: California: “Our company was interested in operating mobile water treatment systems and “Our company was interested in operating mobile water treatment systems and an intricate part of that was the removal of oil from water down to very low an intricate part of that was the removal of oil from water down to very low parts per million in the effluent. Crystal was the only system we found that parts per million in the effluent. Crystal was the only system we found that could give us the desired results and be suitable to be moved about in a could give us the desired results and be suitable to be moved about in a could give us the desired results and be suitable to be moved about in a could give us the desired results and be suitable to be moved about in a

• vehicle. We first used this system in two plants, sold to the Royal Thai
• vehicle. We first used this system in two plants, sold to the Royal Thai
• Government. We have since purchased other units and have been very satisfied
• Government. We have since purchased other units and have been very satisfied

ever since. Our satisfaction not only came from the quality of the product but ever since. Our satisfaction not only came from the quality of the product but the level of service and commitment from Mr Costinel His first thought was the level of service and commitment from Mr Costinel His first thought was the level of service and commitment from Mr. Costinel. His first thought was the level of service and commitment from Mr. Costinel. His first thought was always the satisfaction of the customer and how well his separators service the always the satisfaction of the customer and how well his separators service the customer needs.” customer needs.” The President of Boyd T Keogh and Associates Mr Boyd Keogh of Manly The President of Boyd T Keogh and Associates Mr Boyd Keogh of Manly The President of Boyd T. Keogh and Associates, Mr. Boyd Keogh of Manly, The President of Boyd T. Keogh and Associates, Mr. Boyd Keogh of Manly, Australia: Australia: “Mr. Costinel’s unique invention is complementary to my company’s patented “Mr. Costinel’s unique invention is complementary to my company’s patented equipment and we have imported his Crystal Oil/Water Separator as an integral equipment and we have imported his Crystal Oil/Water Separator as an integral equipment, and we have imported his Crystal Oil/Water Separator as an integral equipment, and we have imported his Crystal Oil/Water Separator as an integral part of our plants, for use both in Australia and overseas. part of our plants, for use both in Australia and overseas.

SLIDE 15

• Mr. Costinel’s attention to detail and insistence on a high and reliable
• Mr. Costinel’s attention to detail and insistence on a high and reliable

level of service plus the quality of his product make it a pleasure to deal level of service plus the quality of his product make it a pleasure to deal with him.” with him.”

List of References List of References

Enviremedial Services Inc., Vista, U.S.A. Enviremedial Services Inc., Vista, U.S.A. Fort Bliss Army Base, Fort Bliss, U.S.A. Fort Bliss Army Base, Fort Bliss, U.S.A. Fort Bliss Army Base, Fort Bliss, U.S.A. Fort Bliss Army Base, Fort Bliss, U.S.A. Camp Pendleton Army Base, Camp Pendleton, U.S.A. Camp Pendleton Army Base, Camp Pendleton, U.S.A. Coronado Navy Base, San Diego, U.S.A. Coronado Navy Base, San Diego, U.S.A. Boyd T. Keogh and Associates, Manly, Australia Boyd T. Keogh and Associates, Manly, Australia Royal Thai Government, Bangkok, Thailand Royal Thai Government, Bangkok, Thailand Royal Thai Government, Bangkok, Thailand Royal Thai Government, Bangkok, Thailand Oil Terminal S.A., Constanta, Romania Oil Terminal S.A., Constanta, Romania A.C.N. srl. Constanta, Romania A.C.N. srl. Constanta, Romania CET Progresul S.A., Bucharest, Romania CET Progresul S.A., Bucharest, Romania CET Iasi S.A., Iasi, Romania CET Iasi S.A., Iasi, Romania CET Iasi S.A., Iasi, Romania CET Iasi S.A., Iasi, Romania Mittal Sidex S.A., Galati, Romania Mittal Sidex S.A., Galati, Romania Santierul Naval Oltenita S.A., Oltenita, Romania Santierul Naval Oltenita S.A., Oltenita, Romania CE3 Technologies, Edmonton, AB, Canada CE3 Technologies, Edmonton, AB, Canada Terra Mannix, Calgary, AB, Canada Terra Mannix, Calgary, AB, Canada Terra Mannix, Calgary, AB, Canada Terra Mannix, Calgary, AB, Canada Hydroxyl Inc. Sidney, BC, Canada Hydroxyl Inc. Sidney, BC, Canada

SLIDE 16

YO YO THANK YOU THANK YOU

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