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C O N S U LTA N C Y            TECHNOLOGY                 E N V I R O N M E N TA L


PROCESS STUDIES                PRODUCED WATER TREATMENT   MARINE ECOTOXICOLOGY
COMPUTATIONAL FLUID DYNAMICS   - CFU                      FRESHWATER ECOTOXICOLOGY
PHYSICAL MODELLING             - Mare’s Tail              WHOLE EFFLUENT ANALYSIS
SLOSHING ANALYSIS & DESIGN     - Hydrocyclones            BAT/BEP
FLUIDS CHARACTERISATION        PROCESS UPGRADE            ENVIRONMENTAL SERVICES
TEST FACILITIES                PROCESS NEW BUILD
OILFIELD CHEMISTRY SERVICES    PROCESS INTERNALS
BAT/BEP                        SAND MANAGEMENT
                               IMPLEMENTATION
                               RESEARCH & DEVELOPMENT



CASE STUDIES                   CASE STUDIES                CASE STUDIES




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RESOURCES




TECHNOLOGY – CASE STUDIES




  CFU - Triton
  CFU – Gorm Platform
  CFU – Heather Platform
  CFU – Peregrino FPSO
  CFU – Field Test Unit


  MARE’S TAIL - Video


  NEW BUILD Condensate Separator
  NEW BUILD Production Separator


  PROCESS UPGRADE – HP Separator
  PROCESS UPGRADE – Degasser
  PROCESS UPGRADE – HP Separator on FPSO
RESOURCES




C O N S U LTA N C Y – C A S E S T U D I E S




  Process Optimisation – Review and Upgrades. PM3 BRA/BRD
  Hydrocyclone Optimisation – BAT/BEP
RESOURCES




C O N S U LTA N C Y – C A S E S T U D I E S   Talisman Energy (Malaysia) Ltd – Bunga Raya Complex

                                              Scope of Work:
                                              >   Process Review, Offshore Fluids Characterisation,
                                              >   Hydrocyclone Trials
                                              >   Vessel Upgrades

                                              Method
                                              >   Comprehensive review of Produced Water Treatment and
                                                  Operating Philosophy
                                              >   Conduct Offshore Fluids Characterisation and evaluation of
                                                  two hydrocyclone vendors
                                              >   Identify Bottlenecks and Prioritise Improvements

                                              Upgrades
                                              >   Replacement hydrocyclone liners
                                              >   1st stage separator and degasser internals

                                              Result
                                              >    Capacity increased from 35,000 to 70,000 BWPD.
RESOURCES




C O N S U LTA N C Y – C A S E S T U D I E S   Shell (now Talisman) Auk – Hydrocyclone Optimisation

                                              Background:
                                              >   Not meeting discharge consent
                                              >   Hydrocyclones operating very inefficiently
                                              >   Multi-vendor trial to ascertain best option for upgrade

                                              Findings
                                              >    Platform HC’s operating at ~50% removal
                                              >    Identified best vendor liner
                                              >    Platform HC’s PDR set at 1.2 – 1.3 due to reject bottleneck
                                              >    With raised PDR, achieved improved efficiency

                                              Conclusion
                                              >   The existing platform hydrocyclones would be capable of
                                                  meeting the efficiency targets if operated at the correct PDR
                                              >   A reject piping cross-over was recommended to achieve PDR
                                              >   No need to upgrade the hydrocyclones
                                              >   Considerable CAPEX savings
RESOURCES



TECHNOLOGY – CASE STUDIES


                            BP Andrew Mare’s Tail®

                            Scope of supply
                            >   Mechanical and process
                                design, fabrication, testing, inspect
                                ion, certification and delivery ex-
                                works of an 18” Mare’s Tail
                            >   Design to pressure vessel
                                specification
                            >   Complete with spare media
                                cartridge and revised cartridge
                                handling systems (for aid in removal
                                and insertion of media cartridges)

                            Process Specifications
                            >    18” unit
                            >    Max design flow: 440m3/hr,
                            >    Normal flow: 191m3/hr
                            >    Predicted inlet process conditions;
                                 100-1000mg/l oil at 10-20 µm
RESOURCES



TECHNOLOGY – CASE STUDIES

                     Mare’s Tail® Demonstration Video
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Hess / Wood Group: Triton FPSO

                            >   Design PW flowrate per CFU train – 430
                                m3/hr
                            >   Oil inlet concentration 100 ppm with 10 –
                                15 ppm at the outlet
                            >   Package comprises 2 x trains of 2 CFU’s
                            >   with interstage Mares Tail®
                            >   Approx package dimensions 5m x 6m x
                                6.5m high – dry weight 30.0 te
                            >   Vessels, pipework and valves in Duplex
                                31803
                            >   Structural steel etc carbon steel
                            >   Instrumentation – impulse tubing all wiring
                                terminated at skid edge JB’s
                            >   Package successfully commissioned
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Lundin / Petrofac: Heather Platform

                            >   PW flow rate – 331 m3/hr
                            >   Oil inlet concentration 1500 ppm with 10 ppm
                                at the outlet
                            >   Package comprises 1 x train of 2 CFU’s with
                                Mares Tail and Reject package added to take
                                reject stream
                            >   Approximate dimensions 11m x 8m x 7m high –
                                dry weight 50.0 te
                            >   Vessels, pipework and valves in lined / painted
                                carbon steel
                            >   Structures - carbon steel
                            >   Instrumentation – impulse tubing all wiring
                                terminated at skid edge JB’s
                            >   Package being installed and being
                                commissioned
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Maersk Olie og Gas, Esbjerg: Gorm Platform

                            >   Design PW flow rate– 400 - 500 m3/hr
                            >   Oil inlet concentration 500 ppm with < 15
                                ppm at the outlet
                            >   Package comprises 1 x train of 2 CFU’s.
                            >   Approx package dimensions 5m x 5.5m x
                                6m high – dry weight 20.0 te.
                            >   Vessels, pipework and valves in Super
                                Duplex 32760.
                            >   Structure carbon steel
                            >   Instrumentation – capillary’s with all
                                wiring terminated at skid edge JB’s
                            >   Package commissioning completed Nov
                                2008
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Maersk / McDermott: Peregrino FPSO

                            >   PW flowrate– 357 m3/hr Heavy Crude
                            >   Oil inlet concentration 100 ppm with 29 ppm at
                                the outlet
                            >   Package comprises 1 x train of 1 CFU
                            >   Approximate dimensions 2.5m x 4.3m x 6.5m
                                high – dry weight 11.5 te
                            >   Vessels, pipework & valves in Duplex 31803
                            >   Structural steel etc carbon steel
                            >   Commissioned
                            >   Exceeding contractual performance with higher
                                inlet oil loading and transient conditions
                            >   Client is very pleased with robust operation
                                and reliable operation
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Compact Flotation Test Rig

                            >   Design Basis:
                            >   Suitable for side stream flowrates between 5.0
                                – 15 m3/hr
                            >   Vessel designed to PD5500 in SS316L.
                            >   Unit provided with all
                                piping, instrumentation, motive water pump
                                etc
                            >   Tie-in points 1.5 – 2” NB
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Rambol Denmark, South Arne Degasser
                            >   Vessel process / mechanical design and supply of internals.
                            >   Opus also took responsibility for the supply, installation
                                and commissioning including nucleonic instrumentation.

                            Process specifications
                            >    PW Flowrate 100,000 bpd
                            >    6.8m T/T
                            >    2.8m ID
                            >    Inlet 400ppm OIW
                            >    Outlet 20ppm OIW
RESOURCES



TECHNOLOGY – CASE STUDIES
                            BP Andrew Kinnoull Separator


                            Scope of supply

                            >   Process design and supply of process internals, including
                                VIEC (electrostatic coalescer).

                            >   CFD modelling analysis includes: multiple flow
                                cases, slugging behaviour.

                            >   Project management of design, new build vessel interfaces
                                and internals installation

                            >   Overall process responsibility for the separator
RESOURCES



TECHNOLOGY – CASE STUDIES
                            BP Andrew Kinnoull Separator
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Mærsk Gorm HP Separator

                            Original Design & Performance


                            >   Vessel Internals Comprised of:-
                                 > Basic deflector plates Inlet
                                 > Perforated Plate Distribution Baffles
                                 > Two Vane Packs
                                 > Gas Outlet Droplet Separator
                                 > Adjustable Weir
                                 > Sand Jetting System
                            >   Oil in Water Performance ~1000 mg/l for
                                an inlet flowrate of 600 – 700 m3/hr
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Mærsk Gorm HP Separator

                            Review Phase

                            The requirement was to identify the operational
                            limitations of throughput through the HP Separator.

                            Methods Adopted:-
                                  > Theoretical Process Review
                                  > Physical Modelling
                                  > Finite Element Analysis of Existing Supports
                            Findings:-
                                  > The inlet device created significant turbulence
                                  > Flow is seen to exit the inlet zone over the first
                                       distribution baffle
                                  > Low open area baffle design is very restrictive
                                  > The water outlet nozzle was found to be
                                       undersized
                                  > Sand system, Droplet Separator & Weir height
                                       acceptable
RESOURCES



TECHNOLOGY – CASE STUDIES


                                        Mærsk Gorm HP Separator

                                        Upgrade Modifications


                                        >   Removal of Existing Inlet, Perforated Baffles
                                            and Vane Packs
                                        >   Internals Supplied for Upgrade:-
                                              >   Inlet Vane Device with Diffuser Baffle
                                              >   Horizontal Gate Baffle with Top Gas
             Confirmed results                    Baffle (Inlet Zone)
         Outlet           Outlet Post         >   Horizontal Gate Baffle (Distribution
      Pre-upgrade          Upgrade                Baffle)
       ~1000ppm           50 - 90ppm          >   Vertical Gate Baffle (Calming Baffle)
                                              >   Vortex Breaker (New Water Outlet)
                                        >   The water outlet nozzle was replaced for a
                                            larger nozzle
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Mærsk Halfdan Degasser

                            Original Design & Performance

                            >   Vessel Internals Comprised of:-
                                 > Open Pipe Inlet
                                 > Perforated Plate
                                 > Longitudinal Notched Weirs

                            Oil in Water Performance – 15-30ppm for an inlet
                            concentration of 50-200ppm.
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Mærsk Halfdan Degasser

                            Review Phase


                            >   Perforated plates fouled
                                   > Solids
                                   > Scale
                                   > Behaving more like weirs
                            >   Notched weirs not effective
                            >   Vessel levels difficult to control
                            >   Lack of inlet device causing poor flow
                                distribution
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Mærsk Halfdan Degasser

                            Upgrade Modifications

                            >   Remove all existing internals
                            >   Internals supplied for upgrade:-
                                  > ZSQ inlet device
                                  > Slotted baffles
                                  > Conventional notched weir
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Mærsk Halfdan Degasser

                            Upgrade Modifications

                            >   Remove all existing internals
                            >   Internals supplied for upgrade:-
                                  > ZSQ inlet device
                                  > Slotted baffles
                                  > Conventional notched weir
RESOURCES



TECHNOLOGY – CASE STUDIES


Mærsk Halfdan Degasser

The Achievements


>   New internals fabricated and supplied on schedule
>   Opus supervised installation
>   Client confirmed performance:-



                       Original Internals                   Revamped Internals

                   Inlet               Outlet             Inlet            Outlet

               50-200ppm             15-30ppm           50-200ppm         5-10ppm
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Hess Triton HP Separator

                            Original Design & Performance

                            >   Split Flow Vessel Situated on FPSO
                            >   Vessel Internals Comprised of:-
                                 > Inlet Diverter Assembly
                                 > Perforated Plate Baffles
                                 > Perforated Plate Over Weirs
                            >   Oil in Water Performance – 300-1500ppm
                            >   Objective was to increase throughput by
                                ~70% whilst maintaining performance
RESOURCES



TECHNOLOGY – CASE STUDIES


                            Hess Triton HP Separator

                            Review Phase

                            >   Process review carried out
                            >   Physical Modelling undertaken with some CFD
                            >   Comparative analysis performed
                            >   Improved internals arrangement determined
RESOURCES



TECHNOLOGY – CASE STUDIES


                            HP SEPARATOR ON FPSO
                            Upgrade Modifications


                            >   Remove all existing internals
                            >   Internals supplied for upgrade:-
                                  > Vane type inlet device with distribution
                                      baffle
                                  > Slotted baffles
                                  > Plate pack coalescer
RESOURCES



TECHNOLOGY – CASE STUDIES


Hess Triton HP Separator

The Achievements


>   New internals fabricated and supplied on schedule
>   Opus supervised installation
>   Tie-in fluids added shortly after start-up
>   Client confirmed performance:-



                     Original Internals                  Revamped Internals
                                                        (with 70% additional flowrate)

                       300 - 1,500ppm                         100 - 600ppm

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Opus case studies - March2012

  • 1. RESOURCES C O N S U LTA N C Y TECHNOLOGY E N V I R O N M E N TA L PROCESS STUDIES PRODUCED WATER TREATMENT MARINE ECOTOXICOLOGY COMPUTATIONAL FLUID DYNAMICS - CFU FRESHWATER ECOTOXICOLOGY PHYSICAL MODELLING - Mare’s Tail WHOLE EFFLUENT ANALYSIS SLOSHING ANALYSIS & DESIGN - Hydrocyclones BAT/BEP FLUIDS CHARACTERISATION PROCESS UPGRADE ENVIRONMENTAL SERVICES TEST FACILITIES PROCESS NEW BUILD OILFIELD CHEMISTRY SERVICES PROCESS INTERNALS BAT/BEP SAND MANAGEMENT IMPLEMENTATION RESEARCH & DEVELOPMENT CASE STUDIES CASE STUDIES CASE STUDIES NOTE: PLEASE CLICK ON THE GREY TAB BELOW ON ANY SLIDE TO RETURN TO THIS MENU
  • 2. RESOURCES TECHNOLOGY – CASE STUDIES CFU - Triton CFU – Gorm Platform CFU – Heather Platform CFU – Peregrino FPSO CFU – Field Test Unit MARE’S TAIL - Video NEW BUILD Condensate Separator NEW BUILD Production Separator PROCESS UPGRADE – HP Separator PROCESS UPGRADE – Degasser PROCESS UPGRADE – HP Separator on FPSO
  • 3. RESOURCES C O N S U LTA N C Y – C A S E S T U D I E S Process Optimisation – Review and Upgrades. PM3 BRA/BRD Hydrocyclone Optimisation – BAT/BEP
  • 4. RESOURCES C O N S U LTA N C Y – C A S E S T U D I E S Talisman Energy (Malaysia) Ltd – Bunga Raya Complex Scope of Work: > Process Review, Offshore Fluids Characterisation, > Hydrocyclone Trials > Vessel Upgrades Method > Comprehensive review of Produced Water Treatment and Operating Philosophy > Conduct Offshore Fluids Characterisation and evaluation of two hydrocyclone vendors > Identify Bottlenecks and Prioritise Improvements Upgrades > Replacement hydrocyclone liners > 1st stage separator and degasser internals Result > Capacity increased from 35,000 to 70,000 BWPD.
  • 5. RESOURCES C O N S U LTA N C Y – C A S E S T U D I E S Shell (now Talisman) Auk – Hydrocyclone Optimisation Background: > Not meeting discharge consent > Hydrocyclones operating very inefficiently > Multi-vendor trial to ascertain best option for upgrade Findings > Platform HC’s operating at ~50% removal > Identified best vendor liner > Platform HC’s PDR set at 1.2 – 1.3 due to reject bottleneck > With raised PDR, achieved improved efficiency Conclusion > The existing platform hydrocyclones would be capable of meeting the efficiency targets if operated at the correct PDR > A reject piping cross-over was recommended to achieve PDR > No need to upgrade the hydrocyclones > Considerable CAPEX savings
  • 6. RESOURCES TECHNOLOGY – CASE STUDIES BP Andrew Mare’s Tail® Scope of supply > Mechanical and process design, fabrication, testing, inspect ion, certification and delivery ex- works of an 18” Mare’s Tail > Design to pressure vessel specification > Complete with spare media cartridge and revised cartridge handling systems (for aid in removal and insertion of media cartridges) Process Specifications > 18” unit > Max design flow: 440m3/hr, > Normal flow: 191m3/hr > Predicted inlet process conditions; 100-1000mg/l oil at 10-20 µm
  • 7. RESOURCES TECHNOLOGY – CASE STUDIES Mare’s Tail® Demonstration Video
  • 8. RESOURCES TECHNOLOGY – CASE STUDIES Hess / Wood Group: Triton FPSO > Design PW flowrate per CFU train – 430 m3/hr > Oil inlet concentration 100 ppm with 10 – 15 ppm at the outlet > Package comprises 2 x trains of 2 CFU’s > with interstage Mares Tail® > Approx package dimensions 5m x 6m x 6.5m high – dry weight 30.0 te > Vessels, pipework and valves in Duplex 31803 > Structural steel etc carbon steel > Instrumentation – impulse tubing all wiring terminated at skid edge JB’s > Package successfully commissioned
  • 9. RESOURCES TECHNOLOGY – CASE STUDIES Lundin / Petrofac: Heather Platform > PW flow rate – 331 m3/hr > Oil inlet concentration 1500 ppm with 10 ppm at the outlet > Package comprises 1 x train of 2 CFU’s with Mares Tail and Reject package added to take reject stream > Approximate dimensions 11m x 8m x 7m high – dry weight 50.0 te > Vessels, pipework and valves in lined / painted carbon steel > Structures - carbon steel > Instrumentation – impulse tubing all wiring terminated at skid edge JB’s > Package being installed and being commissioned
  • 10. RESOURCES TECHNOLOGY – CASE STUDIES Maersk Olie og Gas, Esbjerg: Gorm Platform > Design PW flow rate– 400 - 500 m3/hr > Oil inlet concentration 500 ppm with < 15 ppm at the outlet > Package comprises 1 x train of 2 CFU’s. > Approx package dimensions 5m x 5.5m x 6m high – dry weight 20.0 te. > Vessels, pipework and valves in Super Duplex 32760. > Structure carbon steel > Instrumentation – capillary’s with all wiring terminated at skid edge JB’s > Package commissioning completed Nov 2008
  • 11. RESOURCES TECHNOLOGY – CASE STUDIES Maersk / McDermott: Peregrino FPSO > PW flowrate– 357 m3/hr Heavy Crude > Oil inlet concentration 100 ppm with 29 ppm at the outlet > Package comprises 1 x train of 1 CFU > Approximate dimensions 2.5m x 4.3m x 6.5m high – dry weight 11.5 te > Vessels, pipework & valves in Duplex 31803 > Structural steel etc carbon steel > Commissioned > Exceeding contractual performance with higher inlet oil loading and transient conditions > Client is very pleased with robust operation and reliable operation
  • 12. RESOURCES TECHNOLOGY – CASE STUDIES Compact Flotation Test Rig > Design Basis: > Suitable for side stream flowrates between 5.0 – 15 m3/hr > Vessel designed to PD5500 in SS316L. > Unit provided with all piping, instrumentation, motive water pump etc > Tie-in points 1.5 – 2” NB
  • 13. RESOURCES TECHNOLOGY – CASE STUDIES Rambol Denmark, South Arne Degasser > Vessel process / mechanical design and supply of internals. > Opus also took responsibility for the supply, installation and commissioning including nucleonic instrumentation. Process specifications > PW Flowrate 100,000 bpd > 6.8m T/T > 2.8m ID > Inlet 400ppm OIW > Outlet 20ppm OIW
  • 14. RESOURCES TECHNOLOGY – CASE STUDIES BP Andrew Kinnoull Separator Scope of supply > Process design and supply of process internals, including VIEC (electrostatic coalescer). > CFD modelling analysis includes: multiple flow cases, slugging behaviour. > Project management of design, new build vessel interfaces and internals installation > Overall process responsibility for the separator
  • 15. RESOURCES TECHNOLOGY – CASE STUDIES BP Andrew Kinnoull Separator
  • 16. RESOURCES TECHNOLOGY – CASE STUDIES Mærsk Gorm HP Separator Original Design & Performance > Vessel Internals Comprised of:- > Basic deflector plates Inlet > Perforated Plate Distribution Baffles > Two Vane Packs > Gas Outlet Droplet Separator > Adjustable Weir > Sand Jetting System > Oil in Water Performance ~1000 mg/l for an inlet flowrate of 600 – 700 m3/hr
  • 17. RESOURCES TECHNOLOGY – CASE STUDIES Mærsk Gorm HP Separator Review Phase The requirement was to identify the operational limitations of throughput through the HP Separator. Methods Adopted:- > Theoretical Process Review > Physical Modelling > Finite Element Analysis of Existing Supports Findings:- > The inlet device created significant turbulence > Flow is seen to exit the inlet zone over the first distribution baffle > Low open area baffle design is very restrictive > The water outlet nozzle was found to be undersized > Sand system, Droplet Separator & Weir height acceptable
  • 18. RESOURCES TECHNOLOGY – CASE STUDIES Mærsk Gorm HP Separator Upgrade Modifications > Removal of Existing Inlet, Perforated Baffles and Vane Packs > Internals Supplied for Upgrade:- > Inlet Vane Device with Diffuser Baffle > Horizontal Gate Baffle with Top Gas Confirmed results Baffle (Inlet Zone) Outlet Outlet Post > Horizontal Gate Baffle (Distribution Pre-upgrade Upgrade Baffle) ~1000ppm 50 - 90ppm > Vertical Gate Baffle (Calming Baffle) > Vortex Breaker (New Water Outlet) > The water outlet nozzle was replaced for a larger nozzle
  • 19. RESOURCES TECHNOLOGY – CASE STUDIES Mærsk Halfdan Degasser Original Design & Performance > Vessel Internals Comprised of:- > Open Pipe Inlet > Perforated Plate > Longitudinal Notched Weirs Oil in Water Performance – 15-30ppm for an inlet concentration of 50-200ppm.
  • 20. RESOURCES TECHNOLOGY – CASE STUDIES Mærsk Halfdan Degasser Review Phase > Perforated plates fouled > Solids > Scale > Behaving more like weirs > Notched weirs not effective > Vessel levels difficult to control > Lack of inlet device causing poor flow distribution
  • 21. RESOURCES TECHNOLOGY – CASE STUDIES Mærsk Halfdan Degasser Upgrade Modifications > Remove all existing internals > Internals supplied for upgrade:- > ZSQ inlet device > Slotted baffles > Conventional notched weir
  • 22. RESOURCES TECHNOLOGY – CASE STUDIES Mærsk Halfdan Degasser Upgrade Modifications > Remove all existing internals > Internals supplied for upgrade:- > ZSQ inlet device > Slotted baffles > Conventional notched weir
  • 23. RESOURCES TECHNOLOGY – CASE STUDIES Mærsk Halfdan Degasser The Achievements > New internals fabricated and supplied on schedule > Opus supervised installation > Client confirmed performance:- Original Internals Revamped Internals Inlet Outlet Inlet Outlet 50-200ppm 15-30ppm 50-200ppm 5-10ppm
  • 24. RESOURCES TECHNOLOGY – CASE STUDIES Hess Triton HP Separator Original Design & Performance > Split Flow Vessel Situated on FPSO > Vessel Internals Comprised of:- > Inlet Diverter Assembly > Perforated Plate Baffles > Perforated Plate Over Weirs > Oil in Water Performance – 300-1500ppm > Objective was to increase throughput by ~70% whilst maintaining performance
  • 25. RESOURCES TECHNOLOGY – CASE STUDIES Hess Triton HP Separator Review Phase > Process review carried out > Physical Modelling undertaken with some CFD > Comparative analysis performed > Improved internals arrangement determined
  • 26. RESOURCES TECHNOLOGY – CASE STUDIES HP SEPARATOR ON FPSO Upgrade Modifications > Remove all existing internals > Internals supplied for upgrade:- > Vane type inlet device with distribution baffle > Slotted baffles > Plate pack coalescer
  • 27. RESOURCES TECHNOLOGY – CASE STUDIES Hess Triton HP Separator The Achievements > New internals fabricated and supplied on schedule > Opus supervised installation > Tie-in fluids added shortly after start-up > Client confirmed performance:- Original Internals Revamped Internals (with 70% additional flowrate) 300 - 1,500ppm 100 - 600ppm