Making CNG Cheaper and “Greener” Improving CNG Tank Filling Efficiency/Capacity & Eliminating Gas Preheating in the CNG Decompression Process …a Thermal Solution www.universal-vortex.com HQ: 410 Princeton Hightstown Rd. Princeton Junction NJ 08550 +1609-586-3702 Confidential and Proprietary
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Making CNG Cheaper and “Greener”Improving CNG Tank Filling Efficiency/Capacity &
Eliminating Gas Preheating in the CNG Decompression Process
…a Thermal Solution
www.universal-vortex.com
HQ: 410 Princeton Hightstown Rd.Princeton Junction NJ 08550+1609-586-3702
Confidential and Proprietary
We are “A Thermal Solution”
Eliminate gas preheat in pressure reduction◦ Non-freeze pressure reduction of non-preheated gas
◦ No moving parts
◦ No external energy
◦ No Magic, Only Physics– Vortex phenomenon “discovered/invented” in 1931 by Georges Ranque, improved in 1947 by Rudolf Hilsch in a two-way (hot/cold) vortex tube cyclone
But we are different.
Confidential and Proprietary
2-way Vortex Tube
Problem: Conventional VT freezes up with natural gas due to Joule-Thomson, so conventional VT not commercially applicable
Patented UVI VT overcomes the conventional VT flaw with a non-freeze provision.
Gas Compression/ Mother Station◦ Reduce the impact of the heat of compression
◦ Eliminate costly glycol chilling loops
◦ Decrease the impact of logistical costs facing CNG transport
◦ Improve reliability and consistency of compression/filling process
Gas Decompression/ Pressure Letdown/ Daughter Station ◦ Every m3 of Gas in the tanks should be delivered to the customer
◦ CNG decompression should be affordable from a CAPEX and OPEX perspective
◦ CNG should be the cleanest, most fuel efficient energy solution for off-grid consumers
◦ CNG decompression should be simple and require NO external man-made energy
◦ Enable CNG companies to capture small consumers of gas when OPEX of conventional methods of decompression make the model unviable
◦ Eliminate Carbon Emissions from the CNG decompression process
Confidential and Proprietary
Vortex Pressure Reduction Station
(VPRS-CNG)
Confidential and Proprietary
Vortex Cooling System (VCS-CNG)
Confidential and Proprietary
…and more!
VPRS-CNG does what no other decompression technology does:◦ Completely Eliminates Gas Preheat/Conditioning during the decompression process, while
overcoming the J/T effect
No Boiler
No Electric Heater
No Water Bath Heater
◦ Completely Eliminates CO2 Emissions
No consumption of gas product to feed a heater
No emissions from heater
No gas loss- closed loop decompression
◦ Reduces pressure from any inlet pressure to any outlet pressure
◦ No limitations on flow rate
◦ Modular PRS technology to increase operational flexibility
Fully Scalable-- Regardless of size of system, the design philosophy is the same
◦ Increased Reliability and Safety
No moving parts other than solenoid valves
Few wear items– all critical components static are Stainless Steel and Aluminum
No open flame, no electric heaters
No gas overheat possibility
Confidential and Proprietary
Patented Self-Heating Single-Flow Vortex Pressure Reducer (VPR)
◦ High Pressure gas expands at the tangential inlet nozzle down to the delivery pressure
◦ Rotating low pressure gas in the Vortex Tube undergoes energy division, splitting into cold and hot fractions (Vortex Phenomenon)
◦ Hottest portion provides efficient internal “spot heating” of the inlet nozzle to eliminate freeze-up
◦ Thermodynamically more efficient than two-way vortex◦ Cold and Hot flows are recombined prior at the pressure reducer
outlet, negating the temperature delta◦ Exit gas temperature is equal to the inlet temperature, less the
Joule-Thomson temperature drop
Vortex Pressure Reducer Array
Regulated/Warmed Low Pressure Gas
Confidential and Proprietary
VPRS-CNG Panel:Flow Rate: 2000 Nm3/hr (70,000 SCFH)Inlet Pressure: 250 Bar (3600 PSI)Outlet Pressure: 3 Bar (40 PSI)
Confidential and Proprietary
https://www.youtube.com/watch?v=75xoDTaUYac
Confidential and Proprietary
A minimum of 0.6% of CNG flow is used as a fuel to preheat gas upstream of pressure reduction. For a sample flow rate of 5000Nm3/hr, this translates into the elimination of 61.3 kg/hr, or 536 tons/year of CO2 emissions!
Calculation: The chemical equation for burning methane: CH4 +2*O2 = CO2 +2* H2O. Therefore 1 kg-mole of CH4 corresponds to 1 kg-mole of CO2 Since 1 kg-mole of CH4 = 16kg and 1 kg-mole of CO2 = 44kg, then 1kg of burned CH4.generates 2.75 kg. of CO2
“Turn Key” Engineering/Procurement Solution◦ UVI to design and build entire bespoke decompression skid, including all accessories
◦ Deliver on on a FOB assembly shop basis
◦ Shipping/Installation by others with UVI instruction and support
◦ Delivery Timeframe: 16-24 weeks
Engineering Package & Core Technology & Equipment◦ UVI to design bespoke decompression skid for manufacture/construction/installation
by others
◦ UVI to provide drawing package, technology/IP license to build skid, and Vortex Pressure Reducers
◦ Start up support
◦ Delivery Timeframe: 8-10 weeks
Core Technology & Equipment◦ UVI to provide conceptual design and operating philosophy,
Vortex Pressure Reducers
◦ Drawing review and acceptance
◦ Start up support
◦ Delivery Timeframe: 0-10 weeks
Confidential and Proprietary
Confidential and Proprietary
250Nm3/hr @ 250 Bar to 1 Bar, South Africa
Confidential and Proprietary
1000Nm3/hr @ 250 Bar to 5 Bar, Thailand
Gas @ VPR Outlet @ -90ºC to AAHE
https://www.youtube.com/watch?v=UauUgPZN2UM
Minimize compressor outlet/tank inlet gas temperature
Eliminate the need for glycol chillers
Maximize tank filling
Graphics Source: US Dept. of Energy, Alternative Fuels Data Center
Patented Self Heating Vortex Pressure Reducer (VPR)
◦ High Pressure gas expands at the tangential inlet nozzle down to the delivery pressure
◦ Rotating low pressure gas in the Vortex Tube undergoes energy division, splitting into cold and hot fractions (Vortex Phenomenon)
◦ Hottest portion provides efficient internal “spot heating” of the inlet nozzle to eliminate freeze-up at the pressure drop point
◦ Cold and Hot flows are recombined prior at the pressure reducer outlet, negating the temperature delta
◦ Exit gas temperature is equal to the inlet temperature, less the Joule-Thomson temperature drop– very cold!
Compressor Outlet Pressure: 250bar (3600psi)
Compressor Flow: 6000Nm3/h (3600scfm)
Ambient Temperature: 21.1°C (70°F)
Gas Outlet Temperature: Ambient +20°F
CNG Tank Pressure Range VPR Outlet Gas Temperatures0– 1,000psi(69bar) -53°F (-47.2°C) to -17°F (-27.2°C)1,000psi(69bar) - 2,000(138bar) -17°F (-27.2°C) to 19°F (-7.2°C)2,000(138bar) – 3,000(207bar) 19°F (-7.2°C) to 55°F (12.8°C)
Most effective with composite (better insulated) storage vessels
Hexagon Lincoln Titan Tube Trailer
Confidential and Proprietary
…and more!
Gas Gathering- Wellhead Thermal Conditioning
Gas Processing- NGL/Liquid Hydrocarbon Recovery
Transmission/Pipeline- Gas Regulation & Pilot Heating
CNG- Compression Cooling & Decompression (Mother/Daughter)
Pressurized LNG
LPG
Fuel Gas Conditioning (turbines & others)
Turbo-Expansion/ Pressure-to-Power
Dr. Lev Tunkel
Technical Director
+1(609) 586-3702
+1(609) 516-9129
Ross Gale
Director of Sales & Marketing
+1(609) 589-0627
+1(732) 616-4009
410 Princeton Hightstown Rd· Princeton Junction NJ 08550+1609-586-3702www.universal-vortex.com
…a Thermal Solution
© Universal Vortex Inc. 2017
Confidential and Proprietary
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