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Organic and Mineral Recovery Boilers
Reference: Direct Contact Steam Generation
Gas Technology Institute
OMR Boilers
Proforma
Produced
Water- A1
Produced
Water- A2
Produced
Water- A3
Palm Oil
Work
Camp
Treated water M3/yr 699339 699339 699339 174835 1748
M3/Hr 80 80 80 20 0.2
BBL/Day 12071 12071 12071 3018 30
Power revenue $0.12/kwh $18.84 $18.64 $18.48 $4.64 $0.04
Capex USD Million$ $40.40 $41.00 $41.10 $13.70 $1.28
Capital Charge/yr Million$ $4.63 $4.70 $4.71 $1.57 $0.15
Opex/yr Millons$ 5.00% $2.02 $2.05 $2.06 $0.69 $0.06
Net Revenue/yr Million$ ($10.71) ($11.77) ($12.50) ($3.61) ($0.22)
Water Specific Cost $/M3 $15.31 $16.83 $17.87 $20.64 $123.66
Water Specific Cost $/bbl $2.43 $2.67 $2.84 $3.28 $19.63
Evaporator Blowdown - Assumes 10% of Feed Water
Evaporator Cost not included
Proforma
Produced
Water- A1
Produced
Water- A2
Produced
Water- A3
Palm Oil
Work
Camp
Treated water M3/yr 699339 699339 699339 174835 1748
M3/Hr 80 80 80 20 0.2
BBL/Day 12071 12071 12071 3018 30
Power revenue $0.12/kwh $18.84 $18.64 $18.48 $4.64 $0.04
Capex USD Million$ $40.40 $41.00 $41.10 $13.70 $1.28
Capital Charge/yr Million$ $4.63 $4.70 $4.71 $1.57 $0.15
Opex/yr Millons$ 5.00% $2.02 $2.05 $2.06 $0.69 $0.06
Net Revenue/yr Million$ ($10.71) ($11.77) ($12.50) ($3.61) ($0.22)
Water Specific Cost $/M3 $15.31 $16.83 $17.87 $20.64 $123.66
Water Specific Cost $/bbl $2.43 $2.67 $2.84 $3.28 $19.63
37.21 37.56 37.87 9.45 0.37
17.92 17.73 17.59 4.42 0.18
18.7 19.5 20.1 19.8 18.5
Evaporator Blowdown - Assumes 10% of Feed Water
Evaporator Cost not included
Gross MW
Net MW
GJ/ Net mwh
OMR Boilers-The Problem
Conventional Membranes
Generation 1- Dynamic or Filter-cake
membranes
Generation 2- Fabricated and attached
skin layer membranes-Most common
Attached Skin Layer with pore size
0.01 to 0.1micron
The 3rd Generation-RSL Membranes
Patent protected
Membranes hang onto a
manifold and slide in and out of
the housing
Add a powder slurry of highly Ionic media to create
the Membrane skin layer
Skin layer on the tubes is approximately 50
microns- the thickness of hair
RSL Membranes
The Replaceable skin layer
Three Easy Operating Steps
1. Add the RSL Powder to the surface of the membrane
– 5 minutes
2. Filter the water to be treated-4 to 30 Hrs
3. When the pressure across the membrane reaches 10
psi (70kpa), the membrane tube is backwashed, the
powder is removed, and we start over with step 1- 2
minutes
The Highly Ionic Powder skin layer
simulates the DLVO Theory- What??
• River going into the
ocean full of suspended
solids.
• When river enters the
ocean, the solids
separate from the water
WHY? Because the high ionic environment in the
ocean (Na+ and Cl+) causes the electric double layer
around the solids to collapse.
Generation 1 –
Filtercake
(Dynamic
Membranes)
Generation 2 -
Conventional
and most
common
Membranes
(e.g.
Ultrafiltration
Membranes)
Phase 1 Filtration Cycle
Colloids repulsed from membrane surface
Pressure across the membrane is close to zero
Phase 2 Filtration Cycle
Colloids start to penetrate ionic powder skin layer
Pressure across the membrane rises to 70 kpa
Generation 3 –RSL Membranes
Phase 1
Phase 2
Phase 2
RSL Membranes selected as lead technology to treat Evaporator blow
down water and produced water from Canada’s oil sand operations
Completed fully commercialized RSL Membrane Project with
PetroChina– 25 m3/hr (3600 bbl/day)- operating 7days per week
and 24 hrs per day.
Proved RSL Membranes can separate oil and TSS simultaneously
from water.
Now in design for two more Produced Water Projects.
Commercialized Technology
“Petro China rates RSL Membranes as the
best technology in the world to treat
Produced Water”
60000 bbl/day Produced Water-Permian Basin Case
RSL Membranes
Inside Trailer – RSL
Membranes™
Product 1- Treated water
ready for resale to Frac
operations, EOR, feed
water for irrigation
treatment
Product 2- Recovered oil
from the treated Produced
water
Produced Water Treatment
PWS Standards
Notes
1- Prime technology competitor to RSL Membranes is the DAF (Air flotation) Technology.
2- RSL Membranes provide very high quality treated water at 50% of DAF costs.
BROKER-DEALER/RIA USE ONLY
Conclusion-The 3rd Generation-
RSL Membranes
Patent protected
Provides 10 times the capacity and 90% less
energy.
Separates solids and oil simultaneously.
Replaces all existing processes that separate
solids (DAF’s, clarifiers, oil water separators,
sand filters & all low pressure membranes)
Very small footprint- easy mobility
T H A N K Y O U
www.dbe-rsl.com

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RSL MEMBRANE: PRODUCED WATER TREATMENT & ELECTRICITY GENERATION

  • 1. Organic and Mineral Recovery Boilers Reference: Direct Contact Steam Generation Gas Technology Institute
  • 2.
  • 3. OMR Boilers Proforma Produced Water- A1 Produced Water- A2 Produced Water- A3 Palm Oil Work Camp Treated water M3/yr 699339 699339 699339 174835 1748 M3/Hr 80 80 80 20 0.2 BBL/Day 12071 12071 12071 3018 30 Power revenue $0.12/kwh $18.84 $18.64 $18.48 $4.64 $0.04 Capex USD Million$ $40.40 $41.00 $41.10 $13.70 $1.28 Capital Charge/yr Million$ $4.63 $4.70 $4.71 $1.57 $0.15 Opex/yr Millons$ 5.00% $2.02 $2.05 $2.06 $0.69 $0.06 Net Revenue/yr Million$ ($10.71) ($11.77) ($12.50) ($3.61) ($0.22) Water Specific Cost $/M3 $15.31 $16.83 $17.87 $20.64 $123.66 Water Specific Cost $/bbl $2.43 $2.67 $2.84 $3.28 $19.63 Evaporator Blowdown - Assumes 10% of Feed Water Evaporator Cost not included
  • 4. Proforma Produced Water- A1 Produced Water- A2 Produced Water- A3 Palm Oil Work Camp Treated water M3/yr 699339 699339 699339 174835 1748 M3/Hr 80 80 80 20 0.2 BBL/Day 12071 12071 12071 3018 30 Power revenue $0.12/kwh $18.84 $18.64 $18.48 $4.64 $0.04 Capex USD Million$ $40.40 $41.00 $41.10 $13.70 $1.28 Capital Charge/yr Million$ $4.63 $4.70 $4.71 $1.57 $0.15 Opex/yr Millons$ 5.00% $2.02 $2.05 $2.06 $0.69 $0.06 Net Revenue/yr Million$ ($10.71) ($11.77) ($12.50) ($3.61) ($0.22) Water Specific Cost $/M3 $15.31 $16.83 $17.87 $20.64 $123.66 Water Specific Cost $/bbl $2.43 $2.67 $2.84 $3.28 $19.63 37.21 37.56 37.87 9.45 0.37 17.92 17.73 17.59 4.42 0.18 18.7 19.5 20.1 19.8 18.5 Evaporator Blowdown - Assumes 10% of Feed Water Evaporator Cost not included Gross MW Net MW GJ/ Net mwh OMR Boilers-The Problem
  • 5.
  • 6. Conventional Membranes Generation 1- Dynamic or Filter-cake membranes Generation 2- Fabricated and attached skin layer membranes-Most common Attached Skin Layer with pore size 0.01 to 0.1micron
  • 7. The 3rd Generation-RSL Membranes Patent protected Membranes hang onto a manifold and slide in and out of the housing
  • 8. Add a powder slurry of highly Ionic media to create the Membrane skin layer Skin layer on the tubes is approximately 50 microns- the thickness of hair RSL Membranes The Replaceable skin layer
  • 9. Three Easy Operating Steps 1. Add the RSL Powder to the surface of the membrane – 5 minutes 2. Filter the water to be treated-4 to 30 Hrs 3. When the pressure across the membrane reaches 10 psi (70kpa), the membrane tube is backwashed, the powder is removed, and we start over with step 1- 2 minutes
  • 10. The Highly Ionic Powder skin layer simulates the DLVO Theory- What?? • River going into the ocean full of suspended solids. • When river enters the ocean, the solids separate from the water WHY? Because the high ionic environment in the ocean (Na+ and Cl+) causes the electric double layer around the solids to collapse.
  • 12. Generation 2 - Conventional and most common Membranes (e.g. Ultrafiltration Membranes)
  • 13. Phase 1 Filtration Cycle Colloids repulsed from membrane surface Pressure across the membrane is close to zero Phase 2 Filtration Cycle Colloids start to penetrate ionic powder skin layer Pressure across the membrane rises to 70 kpa
  • 14. Generation 3 –RSL Membranes Phase 1 Phase 2 Phase 2
  • 15. RSL Membranes selected as lead technology to treat Evaporator blow down water and produced water from Canada’s oil sand operations Completed fully commercialized RSL Membrane Project with PetroChina– 25 m3/hr (3600 bbl/day)- operating 7days per week and 24 hrs per day. Proved RSL Membranes can separate oil and TSS simultaneously from water. Now in design for two more Produced Water Projects. Commercialized Technology “Petro China rates RSL Membranes as the best technology in the world to treat Produced Water”
  • 16. 60000 bbl/day Produced Water-Permian Basin Case RSL Membranes Inside Trailer – RSL Membranes™ Product 1- Treated water ready for resale to Frac operations, EOR, feed water for irrigation treatment Product 2- Recovered oil from the treated Produced water
  • 17. Produced Water Treatment PWS Standards Notes 1- Prime technology competitor to RSL Membranes is the DAF (Air flotation) Technology. 2- RSL Membranes provide very high quality treated water at 50% of DAF costs. BROKER-DEALER/RIA USE ONLY
  • 18. Conclusion-The 3rd Generation- RSL Membranes Patent protected Provides 10 times the capacity and 90% less energy. Separates solids and oil simultaneously. Replaces all existing processes that separate solids (DAF’s, clarifiers, oil water separators, sand filters & all low pressure membranes) Very small footprint- easy mobility
  • 19. T H A N K Y O U www.dbe-rsl.com