Coalescer Filter very vital for oil removal, for separation of immiscible liquids

A coalescer filter is used to separate immiscible liquids or remove liquid droplets from a gas or liquid stream. It works by:

• Capturing very fine dispersed droplets (often in the micron or sub-micron range).
• Merging ("coalescing") them into larger droplets.
• Allowing these larger droplets to separate under gravity or flow direction change.

Common Uses:

• Oil–water separation (oil removal from produced water, oily wastewater).
• Water removal from hydrocarbon fuels (diesel, kerosene, aviation fuel).
• Liquid removal from natural gas streams.
• Protection of downstream equipment (pumps, turbines, membranes).

Uses of Coalescer Filters in Oil–Water Separation

1. Produced Water Treatment in Oil & Gas

• Upstream Oil Production:
  In crude oil production, produced water often contains finely dispersed oil droplets (<10 microns). Gravity separators (API separators) can’t effectively remove these ultra-fine droplets.
  Coalescer filters:
  • Capture sub-micron to few-micron oil droplets.
  • Merge them into larger droplets (50–100+ microns) so they rise quickly in downstream separators.
  • Reduce oil content to <10 ppm before discharge or reinjection.
• Enhanced Oil Recovery (EOR) systems:
  Prevents oil carry-over into reinjection water, protecting reservoir formation from plugging.

2. Refinery Wastewater Treatment

• Desalter Effluent Treatment:
  Refinery crude desalters generate oily wastewater streams.
  Coalescers improve oil removal before API separators or DAF (Dissolved Air Flotation) units, reducing chemical usage.
• Cooling Water Blowdown:
  Removes oil films and sheens from cooling tower blowdown streams before discharge to meet environmental limits.

3. Petrochemical & Chemical Plants

• Process Water Cleanup:
  Many petrochemical processes generate oily condensate. Coalescers separate the hydrocarbon layer for recovery and reuse.
• Cooling and Boiler Feedwater Protection:
  Removes oil contamination from process leaks to prevent fouling in heat exchangers and boilers.

4. Power Plants

• Turbine Lube Oil Systems:
  Prevents water ingress into lube oil by removing water droplets, or conversely removes oil from water-cooled condenser drain water.

5. Marine Applications

• Bilge Water Treatment:
  Ship engine rooms collect bilge water contaminated with fuel oil, lubricating oil, and hydraulic fluids.
  Coalescer filters are used in marine Oily Water Separators (OWS) to meet IMO MEPC 107(49) discharge standards (<15 ppm oil overboard).
• Deck Drainage Systems:
  Prevents overboard discharge of oil during tank washing or fuel transfer.

6. Mining & Industrial Operations

• Heavy Equipment Wash Bays:
  Removes diesel and hydraulic oil from wash water before recycling or discharge.
• Ore Processing Plants:
  Separates flotation reagents and oils from process water streams.

7. Airports & Fuel Handling Facilities

• Stormwater Runoff Treatment:
  Removes jet fuel, de-icing fluids, and lubricants from apron and runway drainage water.
• Fuel Spill Cleanup:
  Emergency treatment of oily water after accidental spills.

Why Coalescer Filters Are Favoured in Oil–Water Separation

• High Efficiency: Can remove very fine droplets down to 0.3 microns.
• Compact Footprint: Requires less space than gravity separators or large settling tanks.
• Low Energy Use: Works on pressure differential; no heat or large pumps required.
• Scalable: Can be designed for small flows (bilge water) to large industrial flows (thousands of m³/hr).
• Compliance: Helps meet strict discharge standards (e.g., <10 ppm for onshore, <15 ppm IMO for ships).

Typical Process Position

Coalescer filters are often installed:

1. After primary separation (API separator, CPI separator, or skim tank) to polish the water.
2. Before reinjection pumps to protect downhole formations.
3. Before biological treatment to prevent oil overloading of microbes.
4. Before discharge to surface waters to ensure regulatory compliance.

2. Key Requirements for a Coalescer Filter

A. Performance Requirements

1. Separation Efficiency
   • Oil–Water: Typically target <10 ppm oil in water at outlet (some designs achieve <1 ppm).
   • Gas–Liquid: Remove 99.9% of droplets ≥0.3 microns.
   • Fuel–Water: Outlet water content <5 ppm (aviation fuel standards per EI 1581 or API 1581).
2. Flow Capacity (Rated Flow)
   • Sized for maximum process flowrate without exceeding recommended face velocity.
   • Typical liquid–liquid coalescers: 0.1–0.3 m/s face velocity.
   • Gas–liquid coalescers: 0.05–0.15 m/s.
3. Micron Rating
   • Commonly 0.3 to 5 microns for liquid droplets.
   • Solid particulate removal capability may also be integrated (dual-stage designs).
4. Differential Pressure (ΔP)
   • Clean element ΔP: 0.05–0.2 bar.
   • Replace element at ΔP of 0.7–1.0 bar or per manufacturer guidance.

B. Construction Requirements

1. Housing Material
   • Carbon Steel: For non-corrosive hydrocarbon service.
   • Stainless Steel 304/316L: For corrosive environments, seawater, or aggressive chemicals.
   • Coatings: Epoxy-lined or phenolic-coated for seawater or wastewater.
2. Element Media
   • Fiberglass: High efficiency, chemical resistant.
   • Synthetic fibers: For compatibility with fuels and lubricants.
   • Polyester or Polypropylene: For general water/oil service.
   • Multi-layer gradient density media for improved droplet capture.
3. Sealing
   • Buna-N, Viton, EPDM, or fluoropolymer elastomers — chosen based on fluid chemistry and temperature.
4. Pressure Rating
   • Designed for process operating pressure (e.g., ANSI 150, 300, 600 flanges or equivalent).
   • Gas coalescers often rated for 10–150 bar service.
5. Temperature Rating
   • Select elastomers and media compatible with process temperature (often -20°C to +90°C standard, higher for special designs).

C. Design Features

1. Two-Stage Configuration
   • Stage 1: Coalescer media (merges fine droplets).
   • Stage 2: Separator media (repels coalesced phase and allows clean phase to pass).
2. Drainage Provisions
   • For separated liquid collection and removal.
   • Automatic or manual drains.
3. Flow Direction
   • Often inside-to-outside for solids removal in first stage, then outside-to-inside for coalescing.
4. Ease of Maintenance
   • Quick-opening closures (swing bolt, clamp ring) for element replacement.
   • Vertical or horizontal vessel orientation depending on site footprint.
5. Instrumentation
   • Inlet and outlet pressure gauges/transmitters to monitor ΔP.
   • Sight glass or level sensor in sump section.
   • Optional water-in-fuel detectors (for aviation fuel service).

D. Installation Requirements

• Upstream Filtration: Install particulate filters before coalescer to prevent plugging.
• Flow Conditioning: Avoid high turbulence — use straight pipe runs before unit.
• Drain Connection: For separated phase removal to prevent re-entrainment.
• Vent Connection: To remove trapped gas or air pockets

3. Relevant Standards

• API 12J – Oil–Water Separator Design
• API 1581 / EI 1581 – Aviation Fuel Filter/Separators
• ASME Section VIII – Pressure Vessel Design
• ISO 12500-3 – Compressed Air Filters (Liquid Removal)
• ASTM D3948 – Water Separation Test

4. Typical Specification Table for Procurement

Parameter	Requirement
Service Fluid	Produced water with dispersed oil
Inlet Oil Concentration	200 ppm
Outlet Oil Concentration	≤10 ppm
Flowrate	345 m³/hr
Micron Rating	≤0.3 μm droplets
Vessel Design Pressure	10 bar
Vessel Design Temperature	-20°C to +80°C
Material of Construction	SS316L
Coalescer Element Media	Fiberglass, multi-layer
Elastomers	Viton
End Connections	ANSI 150 RF
Housing Type	Horizontal, two-stage
Drain Type	Automatic + manual
ΔP Clean	≤0.15 bar
ΔP Dirty	≥0.7 bar (replacement)

Coalescer Filter – Engineering Procurement Datasheet

 

1. General Information

Item	Specification
Type	Horizontal, two-stage coalescer-separator vessel
Application	Removal of dispersed oil from produced water / wastewater
Standard	API 12J, ASME Section VIII Div. 1
Design Life	20 years minimum
Performance Guarantee	Outlet oil concentration ≤ 10 ppm at design flow

2. Process Data

Parameter	Design	Normal	Maximum
Flowrate	345 m³/hr	___	___
Inlet Oil Concentration	200 ppm	___	___
Outlet Oil Concentration	≤ 10 ppm	___	___
Fluid Viscosity	___ cP	___	___
Fluid Temperature	30°C	___	80°C
Fluid Density	Water: 1000 kg/m³, Oil: 850 kg/m³
Operating Pressure	6 bar(g)	___	___
Design Pressure	10 bar(g)
Design Temperature	-20°C		+80°C
pH Range	6.5 – 8.5

3. Mechanical Design

Item	Specification
Vessel Orientation	Horizontal
Shell Material	SS316L (ASTM A240)
Nozzle Flanges	ANSI B16.5, 150# RF
Corrosion Allowance	3 mm
Internal Coating	Epoxy phenolic (minimum 300 μm DFT)
Closure	Quick-opening, swing bolt type
Drain Connection	2” NPT (Automatic & Manual)
Vent Connection	2” NPT
Instrument Connections	ΔP transmitter, level gauge, sight glass
Support Type	Saddle support
Lifting Lugs	Yes

4. Coalescer Elements

Item	Specification
Quantity	As per vendor sizing (minimum redundancy: N+1 elements)
Flow Direction	Inside-to-outside (coalescing stage), then separator stage
Micron Rating	≤ 0.3 μm droplet capture
Media	Multi-layer fiberglass
Separator Stage	Teflon-coated hydrophobic mesh
Element Outer Shell	Perforated stainless steel
Element Length	Standard 40" or 60" (vendor to confirm)
Seals	Viton (compatible with hydrocarbons)
Replacement ΔP	0.7 bar(g)

5. Instrumentation & Controls

Item	Specification
Pressure Gauges	Inlet & Outlet, stainless steel, glycerin-filled
Differential Pressure Transmitter	4–20 mA output, HART protocol
Level Indicator	Magnetic level gauge + sight glass
Automatic Drain	Pneumatic/solenoid actuated
Manual Drain	Ball valve, SS316

6. Utilities

Item	Specification
Instrument Air	6–8 bar(g), clean & dry
Power Supply	230 VAC / 50 Hz for solenoid valves
Earthing	Vessel & instrumentation earthed per IEC standards

7. Vendor to Supply

1. Vessel with all internals installed.
2. Coalescer and separator elements.
3. Instrumentation (gauges, transmitters, level indicators).
4. Spare element set (for 1 year operation).
5. Foundation loading data.
6. Installation & O&M manual.
7. Performance test certificates.

8. Drawing Requirements

• General arrangement drawing (GA)
• Piping & nozzle orientation drawing
• Internal element layout
• Foundation loading diagram
• Instrument location diagram

9. Testing & Inspection

Item	Requirement
Hydrotest	1.5 × design pressure per ASME VIII
NDE	100% radiography on longitudinal & circumferential welds
Coating Inspection	Holiday test, DFT measurement
Performance Test	Witnessed by client at vendor works

10. Reference Standards

• ASME Section VIII Div. 1 – Pressure Vessel Code
• API 12J – Oil–Water Separator
• ASTM D4286 – Droplet size measurement
• ISO 9001 – QA/QC System
• ISO 12500-3 – Liquid removal from compressed air (relevant testing)