Making CNG Cheaper and “Greener” - Gastech Barcelona Gale - Lev... · Making CNG Cheaper and...

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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

Transcript of Making CNG Cheaper and “Greener” - Gastech Barcelona Gale - Lev... · Making CNG Cheaper and...

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.

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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.

…more on this later

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

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Vortex Pressure Reduction Station

(VPRS-CNG)

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Vortex Cooling System (VCS-CNG)

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…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

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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

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VPRS-CNG Panel:Flow Rate: 2000 Nm3/hr (70,000 SCFH)Inlet Pressure: 250 Bar (3600 PSI)Outlet Pressure: 3 Bar (40 PSI)

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https://www.youtube.com/watch?v=75xoDTaUYac

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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

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250Nm3/hr @ 250 Bar to 1 Bar, South Africa

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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

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…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

[email protected]

+1(609) 586-3702

+1(609) 516-9129

Ross Gale

Director of Sales & Marketing

[email protected]

+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