v 2012/1.0

Sustainable Fuel Energy ecoPHASERSolid to Gas Phase Thermal Reactor

1987 2007

440Hz Pulsed Oxidizer

Solid to Gas PhaseSublimation Reactor

ecoTECH Energy Group, Inc. (the “Company”) acquired ecoPHASER Energy Corp in 2010. ecoPHASER was incorporated with the express purpose of developing

systems based on sublimation (gasification) for use in agriculture and industrial applications where waste products may be converted to energy rather than being discarded. ecoTECH Energy Group is a project developer that utilizes ecoPHASER technologies.

In municipal, commercial, institutional, agriculture, forestry and industry management, the waste and effluent streams have become the focus of intense concern. The sheer volume of effluent and waste materials requiring disposal solutions without adding to the long term effects of greenhouse gases, and the current waste contamination and pollutant problems are becoming an increasing socioeconomic drain. By recapturing the energy value of the waste, these concerns can be resolved at a substantial net gain - not only to the specific operator, but on a societal basis by helping to meet the increasing demand and cost for energy, whilst safeguarding health and environmental sustainability. This brochure describes the ecoPHASER technology.

The resulting systems are available for utilization in projects world wide and designed to generate carbon and greenhouse gas credits under green energy protocols that are scheduled to be introduced on in place many participating countries for carbon reduction

credits trading.

Head Office & LaboratoryUnit 101 - 26633 Gloucester Way,

Langley, British Columbia, Canada V4W 3S8

tel: +1 604 288 8263 e-mail: info@ecth.caproduct web site: www.ecophaser.ca

corporate web site: www.ecotechenergygroup.com

Multi-Fuel ecoPHASER:MANY FUELS FOR THE THERMAL OXIDATION PROCESS

CoalLignite

LeonarditePeat

Chipped TyresStraw

Wood wasteForestry Slash

CroppingsBarkCoke

SawdustPaper

Natural GasLandfill Gas

BagassePresorted Garbage*

Manure**Dried Sewage**

* = Segregated Combustible Components (Chopped to

< 75mm = < 3”)

** = With other open fibre materials

HistoryecoTECH formed 1980

federal incorporation 1990

public incorporation (RTO) 2010

Gasifiersfirst unit built 1983

first large commercial unit 1987

Canada demo unit 1990

ecoPHASERfirst unit built 1990

pulsed combustor 1997

pulse unit acquisition 2004

reactor + pulsed oxidizer 2007

ecoTECH & Power Stationsthermal combustion consultancy 1979

own projects started (BC Hydro) 2007

The ecoPHASER CHP* Generation System New Advances in Combined Heat & Power (*CHP) Thermal Technology

Sustainable Biomass Oxidation, or Co-fired Fossil Fuels and Biomass

Co-firing usually involves substituting biomass for a portion of coal, lignite or anthracite coke in an existing power plant furnace. It is the most economic near-term option for introducing new biomass power generation.

Because much of the existing power plant equipment can be used without major modifications, co-firing is far less expensive than building a new Bio-Power plant. Compared to the coal it replaces, biomass reduces sulphur dioxide (SO2), nitrogen oxides (NOx), and net greenhouse gas emissions. After “tuning” the furnace combustion process, there is little or no loss in efficiency from adding biomass. This allows the energy in biomass to be converted to electricity with the high efficiency (in the 33-37% range for single cycle operation) of a modern coal-fired power plant.

ecoTECH Energy Group, Inc.. has developed an environmentally superior system which allows the co-firing of biomass with natural gas. This is possible in areas with supplies of natural gas and a demand for power greater than that which can be derived from available local biomass sources.

A valuable extension of this system allows for the cleaning and co-firing of coal-bed methane gas, an especially clean form of natural gas. This form of fuel use for energy generation will be incorporated in the plant design.

Sublimation: Solids to gas phase conversion (gasification)

Biomass and coal gasifiers operate by heating the fuels in a reduced oxygen (sub-stoichiometric) environment where the solid matter breaks down (changes phase) to form an inflammable gas, known as “syn-gas” or “producer” gas. This offers several advantages over directly

burning the biomass. In some chemically toxic fuel applications, the syn-gas can be cleaned and filtered to remove problem chemical compounds before it is burned. Ordinarily, low pressure sublimation and pulse combustion eliminates this need in virtually all applications. This allows use of a wider range of biomass or coal derivative fuels, including coals, lignins, pulp liquors and sour gas emitting fuels that are marginal or impossible for standard combustion systems.

Also, biomass derived bio-gas or coal syn-gas can be used in more efficient power generation systems called combined-cycles, which combine gas turbines and steam turbines, with sequential heat capture to power heat recovery steam generators, or our own high to low pressure steam to steam reheat cascade system, transferred to turbine-generators for energy conversion to electricity.

Whereas, the most modern single cycle power systems operate at up to 40% total efficiency, these newer systems can exceed 85% of fuel potential energy to electrical energy conversion.

The remaining heat drives the clean exhaust gases clear of the exhaust stack.

Actual through porthole view of ecoPHASER’s combustion system primary gasifying chamber.

PRE-HEAT PHASE

OPERATIONAL PHASE

BIOMASS or COALPHASE CONVERSION REACTOR

The Thermal System ExplainedPhasers, boilers & heat capture energy conversion system

The energy conversion system consists of a matched pair of solid to liquid-suspension (superheated steam) and solid to gas phase reactors, (syngas generation primary zone), mated to boiler steam generation systems, (2 ecoPHASER reactors and one boiler system per 12 mW module), which are placed in arrays. Each ecoPHASER sublimation reactor is fitted to a secondary stage cyclonic,

carburettor and a proprietary pulsed flame burner (“The Phaser System”). A Phaser embodies a primary stage coal or bio-gasification reactor/generator, a second stage carburettor and a super SSW high temperature burner, with superior environmental protection and heat radiance characteristics.

The waste is fed into this system and fuelled by a combination of the coal or biomass contained in the fuel and in co-fired systems, (where coal bed gas is available), 100% methane [CH4] natural gas. The gas or micronized particle coal emulsion (20-50 micron particle size) is injected into the second stage of the Phaser in steam cogeneration systems, or is filtered into the fuel injection systems of gas turbine cogeneration systems.

In the primary stage the solid fuel is burned under starved air (sub-stoichiometric) conditions, so that it releases a combustible gas mixture. Ash residue is minimal (circa 2%). The process is actually enhanced by the moisture content of the coal or woodwaste.

In the second stage, with a swirled vortex of pressurized air added, the resultant gas mixture ignites in the nozzle of the SSW Burner, generating high frequency waves of heat energy, ensuring complete burnout of particulate matter with temperatures sufficient to crack the hydrocarbons and break down gases to simple products of combustion.

The combustion gases that occur with entrained superheated steam plus released carbon are described in the following equation:

Csolid+H2O steam = CO + H2 *

* = per “Biomass Energy Systems & Technology (BEST) Project” research analysis by Winrock International Institute for Agricultural Development - 1998.

Introduced in the mk VII (2007) design, the new Sonic Standing Wave (SSW) combustion unit produces a high radiance, mushroom-head flame that pulses the combustion flame at 440 Hz. The high frequency flame oscillation disrupts the recombination of elements of combustion, giving a NEAR ZERO NOx emission profile!

This tertiary combustion unit is connected to a heat extraction system via a tertiary chamber (firebox) which acts as a thermal reservoir and stabilizer due to its high mass of super-insulated, reflective refractory. In most cases the sender (receptacle) radiator for the hot oil transmission system is sited within, servicing remote heat radiators for process heat via the high speed pumped oil circuit or boilers that generate steam for power turbines, which power electricity generators. Boilers may also be close coupled to the firebox, depending on the system purpose, and the power to process-heat ratio.

Temperature band control systems in the tertiary (firebox), and the following combustion and heat transfer chambers (boiler, superheater, re-heater, economizer) further prevent undesirable recombination of the simple products of combustion, (NOx & SOx). On-demand bubble or cloud scrubbers complete the throughput hot gas transfer and treatment system for exhausts with zero entrained particulate and near-zero nitrous oxide emissions.

Waste heat from the power generation process is fed through excess and residual energy recovery systems that feed industrial processes, provide district or local heating and preheat boiler influent water to prevent shocking of the boiler tubes or heat transfer vanes. The energy depleted exhaust is fed through a patented wet, enhanced surface recovery cloud or bubble scrubber arrays, depending on fuel.

This exclusive system is proprietary to ecoTECH and is licensed in each Company approved application only. This document provides general information only to preserve the technological innovation in the system, details of which are governed by trade secret criteria.

Sonic Standing Wave High RadianceCombustion Unit

The Thermal System Explained:Phasers, boilers & heat capture energy conversion system module, per 12 mW (2 x 85 GJ or 80 Mbtu) ecoPHASERs:

The Combined Heat & Power FireboxDue to the intense heat characteristics of the tertiary stage SSW (sonic standing wave) pulse combustion unit that follows the second stage vortex carburetion zone of the Phaser, an intermediary ceramic lined firebox is used to absorb and radiate the heat into the boiler complex. The firebox diffuses the pulsed energy in the flames from the SSW burner of the phase conversion reactor, sometimes including a Thermax® hot oil circuit depending on the specified CHP heat usage allocation format (power or circuit heat emphasis).

A unique burner, the SSW oxidizer generates its own sonic standing wave to give a pulse burn, (without mechanical frequency modulation) producing a high radiation 440 Hz staccato sequence of thermal pulses. The high emissivity shield refractory of the firebox flows heat onto all of the boiler, superheater, reheater and economizer zones without the high velocity jet action usually associated with vortex ram-jet combustion systems, deflecting and blending hot spots to achieve a homogenized, long residence radiance, which heats the boiler tubes without zone shock.

The boiler of each 12 megaWatt energy module is of the Benson type and is of a pyramid design, with the firebox forming the lower zone. All of the boiler heat zones are walled with highly reflective olivine/dunite and heavy foamed ceramic insulation.

The Modified Once-through Boiler of the ecoTECHPower Generation & Industrial Process Heat System: The principles of the “Once-through” boiler are not new or untried. A once-through boiler was constructed in England under the direction of Mark Benson as far back as 1923. Some years later their development was taken over by Siemens of Germany. No steam drum is used in the once-through principle. The feed water is forced through the tubes in a true forced-circulation manner.

The auxiliary heating tube by-passed around the throttling device is used to thermally indicate a change in rate of firing before steam pressure or temperature is affected. Pure feed water (from treated condensate) should be used with boilers of this type. Accordingly, we use closed loop water systems, with excess steam and water recovery via combustion inlet air preheat through the system’s condensers.

Make-up feed is derived from an evaporator so that distilled water is produced for feed. Any salts formed on internal surfaces of the tubes are dissolved and removed when the unit is started up or shut down, operating as a flooded system. Due to its sensitivity of response to changes in combustion rates the once-through boiler is well adapted to the principle of variable-pressure operation in conjunction with specially designed cascade (high pressure then low pressure) turbines.

All types of fuel have been used with success (including mechanical stoker coal, gas and pulverized fuel, or the MSW or forestry derived biomass described for our sustainable energy system).

Advantages of the ecoTECH derivative of the once-through style of boiler are:

√ Lower cost and weight due to elimination of drums. √ Elimination of trouble due to natural circulation. √ Extreme flexibility in respect to pressure, temperature and overloads.

The Company has researched many ways to inhibit the corrosion usually associated with steam production. With new advances in understanding high temperature microbial action on boiler tubes, recent development of biofilm colony disruption additives will ensure a trouble-free extended life for our project. New understanding of the signal mechanisms that allow biofilms to form has brought about a remarkable additive that disrupts

Phaser Mk II hearth photographed during bi-annual servicing & refractory inspection (1990) showing vertical auger feeder unit and

removable-for-servicing airway wedges

The Mark V Phaser’s Primary Zone chamber

sublimation (gasifying) hearth, showing the vertical fuel feeder screw and starved-air feeder ports (airways).

The author examines a Mk II gasifier in April 1990, after 3 years in operation.

The unit continues to heat an 800,000 sq. ft. factory in Wisconsin USA.

The author examines a Mk II gasifier in April 1990, after 3 years in operation.

The unit continues to heat an 800,000 sq. ft. factory in Wisconsin USA.

New power plants are currently built for a service life of 30 to 40 years. They must therefore continue cost-effective electric power generation through the year 2050. High efficiency contributes significantly to the cost-effectiveness of steam power plants. Biomass (or fossil fuel) sublimation and SSW oxidation virtually eliminates particulate travel abrasion and the usual wear in the boiler and ancillary areas of the system, resulting in a clean, environmentally benign, zero particulate exhaust and the use of a spectrographically triggered on-demand scrubber, that is deployed only if undesirables are found in the gas stream from problem fuels.

One of the most effective measures for achieving high power plant efficiency is selecting a high design steam pressure. Efficiency increases by roughly 3% on making the transition from 167 bar ,or 2422 p.s.i.g. (e. g. drum boiler) to 250 bar, (3625 p.s.i.g.) without significant increases in investment costs. The increased costs for the greater wall thicknesses of the pressure section are largely compensated by the lower costs of the smaller fuel/air/flue-gas path.

The once-through type boiler can be built with essentially the same design for sub-critical and super-critical pressures. Only the dimensions, materials specifications and wall thicknesses of the tubes and headers change with increasing pressure.

Main steam properties are selected based only on aspects of cost-effectiveness. Once-through boilers have been built to date for pressures from 40 to 310 bar (580 to 4500 p.s.i.g.). Increasing steam pressure is the most effective way to increase the efficiency and hence the cost-effectiveness of a power plant.

With the complete ecoPHASER system, you will note that all aspects and opportunities of heat capture in flue gases have been addressed, including gleaning all but the necessary stack lift energy from the fluid and gas exhausts via sophisticated heat exchangers, to recycle into the input fluid and inlet air.

This includes heat recovery from the fluid (bubble) exhaust scrubber, from the economizer heat transfer and the sinusoidal, through-stack exhaust-heated inlet air warmer (air-to-air heat exchanger). The scrubber and the steam make-up water filtration units (hour glass filters) are insulated to conserve and retain heat in the fluids. The design is crafted to achieve evenly-balanced warming curves throughout the circuit, thereby preventing thermal shock to the hot vessels and heat transfer tubes, in all ambients, arctic to tropic.

Main steam temperatures in the ecoPHASER once-through boiler are independent of load. This results in a higher process efficiency for the power plant over a wide load range. The fuel to feed-water flow ratio is controlled in the ecoPHASER boiler system such that the desired steam temperature is always established at the main steam outlet. This is made possible by the variable evaporation end-point. The evaporation and superheating surfaces automatically adjust to operating conditions. In dynamic processes, the superheaters support maintenance of constant main steam temperature.

Minimum output in once-through operation at high main steam temperatures is 35 to 40% for furnace walls with smooth tubes and is as low as 20% if rifled tubes are used. The outstanding heat transfer characteristics of rifled tubes enable simplification of the design of the boiler and further improvement in its operating behaviour. The Company is continuing to research the potential application of Free Energy Inc.’s super conductivity elements for next generation steam generation and for hybrid enhanced geothermally heated feed water plus sustainably fuelled, ‘Phaser-powered thermal systems. These systems will sometimes using Rankine-cycle turbo generators for smaller or remote and off-grid stand-alone, or distributed CHP energy installations.

Of the more than 1,000 once-through boilers constructed to date, roughly 600 have a vertically tubed furnace, most of these with several trains connected in series. Implementation of optimized rifled tubes with enhanced heat transfer characteristics now enable parallel configuration of all furnace tubes even in vertically tubed boilers.

British Columbia Construction 1995

We are often asked why the ecoPHASER system uses less fuel than conventional grate and/or fired boiler systems.

There are several reasons why this is so:»] the ecoPHASER System was originally designed to conserve fuel, whereas most other solid fuel systems, especially biomass and garbage fuel systems, are designed to incinerate (reduce) fuels with the emphasis on volume reduction over economical energy production.

»] the ecoPHASER is not a one combustion chamber design. In conventional solid fuel systems, all of the combustion, even in one-chamber “zoned” so-called gasification combustion units, occurs in a thermal firebox with hot spots and erratic, uneven fuel oxidation resulting in Nitrous Oxide creation, once the simple elements of combustion are liberated from the fuel. The erratic hot spots that occur with conventional burners give rise to silicon (ash) fusing (clinker creation) and dioxin/furan molecular combinations with some fuels.

»] In contrast, the ecoPHASER system consist of three separated chambers for sublimation, air/gas mixing and combustion, that gives full reduction of fuel in the sublimation reactor, full gas/air mixture in the carburettor and a high frequency, staccato short flame front from the Sonic Standing Wave oxidation unit.

The SSW oxidation unit delivers clean radiant energy in the firebox, which has its own particulate burn out and ash removal section. Massive refractory linings constructed from the most avant garde insulation components, stabilize and isolate the chambers, which are devoid of hot spots or chill zones. Sublimation is effected above the creosote potential heat threshold and below the ash fusion temperature, whilst the unique character of the pulsed burn enables heat to radiate without high gas velocity, having an element recombination disruption frequency calculated to eliminate the formation of NOx and other noxious greenhouse gases.

The performance of the Mark VII ecoPHASER producing heat values of 52 Mega British Thermal Units (Mbtu), or 55 GigaJoules (GJ) per hour is compared in the tables on this page with the actual results in 7 years of reports of a 35 Mbtu/hour unit that operated in McBride BC at a veneer plant, recorded independently by inspectors and analysts during emissions testing for air-shed clean exhaust compliance. In each test run, the Mark III clone consumed 2 tonnes of 35-50% total moisture content forestry residue wood, (unwashed bark and trimmings) per hour. This unit was fitted with our earlier, less efficient, Vortex Ramjet Burner, with no exhaust scrubber.

Why the ecoPHASER Energy System is so efficient.

A. Lanfranco & Associates

Analysis of performance by extrapolation from the report.

3 35(MMBTU) Mbtu/hr

37GJ per hour

Fuel used in metric tonnes (forestry residues) per 1 hour test

2.00 35.8 inches 909 mm

Heat Energy creation 17.5 18.5

Sublimation Reactor (primary chamber) temperature deg F.

1,375 746 oC 2,150 1,177 oCelcius

ecoPHASER performance per module (170 GJ/hr 12 MW)

Fuel use in metric tonnes (forestry residues) per 1 hour

9.18 39.37 inches 1000 mm

Heat Energy creation 160.65 169.34Rated Nameplate 80.25 55 50.05%Sublimation Reactor (primary chamber) temperature deg F.

1,100 593 oC 2,255 1,235 oCelcius

Conversion Rates per ecoPHASER 1 of 3Raw Energy equivalents - nameplate 82 84.67 12.27 mWe

Raw Energy equivalents - actual 160.65 169.34 24.03 mWe 16.5038 MWe meanRaw Energy equivalents - nameplate 48.96% 24.26% 12.5 mWe Rating @ 12 MW/hr

Conversion Rates per CHP Module 2 of 3Raw Energy equivalents - nameplate 164 169.34 24.53 mWe

Raw Energy equivalents - actual 321.3 338.68 48.06 mWe 36.4007 MWe meanRaw Energy equivalents - nameplate 48.96% 24.26% 25 mWe Rating @ 12 MW/hr

at Boiler Efficiency of 50% 169.34 12.5 mWeGJ Boiler losses rating per module

Mbtu per hour GJ per hourEnergy margin MWe contingency

ecoPHASERS firing per firebox/boiler - HEAT generation only

ecoPHASERS firing individual ratings

Although similar in design to the unit above (derived from ecoTECH originals) the following improvements and differences are in the 2007 ecoPHASER Mk 7 fired 12 MW unit. 3 ecoPHASER

reactors are used per firebox - 2 active & 1 standby for 24/7 100 % uptime

Mbtu per hour GJ per hour

Tertiary Chamber (boiler) Temperature Fahrenheit

Tertiary Chamber (boiler) Temperature Fahrenheit

tonnes per hour Stack Diameter

Mbtu per hour GJ per hour

Energy margin MWe contingency

McBride Forest Industries: Gasifier Air Emissions Report - 29th September 2006 test date.

Mbtu per tonne GJ per tonne

Mbtu per hour GJ per hourMbtu per hour GJ per hour

1 hour tests

tonnes per hour

Rated nameplate

Stack Diameter

Mbtu per hour GJ per hour contingency margin

Carbon Dioxide emission analysis: ecoPHASER Thermal Energy System

ecoPHASER exhaust delivery rate (total gases) 100.00% 1.6 m3 /second

Thermal output rating 55 gJ/hour 52 Mbtu/hour (raw heat energy)

Carbon Dioxide content volume/time per reactor 12.80% 0.2048 m3 /second s.m3 (standard cubic metre)

Density of CO2 at standard ambient 1.98 grams/litre

Stack Temperature 111 oC 232 oFMass Flow: total gases relative density (ambient)* 81.07% 3.17 kg/second 2.57 actual kg/sec: adjusted (at stack temperature)

Actual CO2 mass delivery per net 12 mW train 81.07% 111 oC 17 mW equivalent raw heat energy

0.328742 kg/second flowrate corrected to standard ambient

Therefore: mass of Carbon Dioxide emitted mW per hour per day per year12 1.18 tonnes 28.32 tonnes 10,336.80 tonnes

24 mW Power Station 24 2.36 tonnes 56.64 tonnes 20,673.60 tonnes

36 mW Power Station 36 7.08 tonnes 169.92 tonnes 62,020.80 tonnes

48 mW Power Station 48 28.32 tonnes 679.68 tonnes 248,083.20 tonnes

60 mW Power Station 60 141.6 tonnes 3398.4 tonnes 1,240,416.00 tonnes

72 mW Power Station 72 849.6 tonnes 20390.4 tonnes 7,442,496.00 tonnes

Control equivalent: Hazlewood Power Station, Victoria, Australia 1 1.55 tonnes/mW

12 18.6 tonnes 15.763

Comparative efficiency of CO 2 emissions 6.34% of control (Hazlewood) CO2 emissions

to 1 emission ratio

ecoPHASER is

Lignite fuel is equivalent to wood in ecoPHASER 2 phase combustion**

n.b. these are old figures based on previous vortex burner: SSW burner (with near zero Nox) expected @ <80% of vortex CO2 emissions values.

* @ 70oF & 14.696 psia, dry air has a density of 0.002120564 lb/cubic foot* @ 21.1oC & 0.101325353 MPa, (1 atm), dry air has a density of 0.033968172 kg/cubic metre

Standard ecoPHASER Power Train Module

Lignite fueled combustion**

ecoPHASER Energy Corp 03/01/2012

(Lb./Hour) (Tons/year)

2.11304348 9.25513043 68o F @ 101.3 kPa

0 0 0 0

0 0 0 0

2.8173913 12.3401739 4 to 6 p.p.m.

0 0 0 00 0 0 0

*****

ecoPHASER CLEAN ENERGY - Near ZERO pollutant emissions

Emission Rates

(Alternate averaging periods)

Model type and specification to be advised

Model type and specification to be advised

WE ACHIEVE NEAR ZERO OF THE ABOVE EMISSIONS WITH A CHARGED PARTICLE (Cloud) SCRUBBER ON EACH MODULE Most potential pollutants are completely oxidized with the pulse burn.

Per Caterpillar published figures (insignificant)

**Emergency Blackstart Standby Diesel Generator Per Caterpillar published figures

SO2

Pb

NOx

VOCCO*** Wood Fuel (Chip & Hog Fuel) Loader #1

Regulated Air Pollutant

PM10

36MW EXAMPLE STACK EMISSIONS: UNIT SPECIFIC AND PLANT-WIDE EMISSIONS SUMMARYEmissions Unit Specific EmissionecoPHASER 36mW Station fires 3 Thermal units simultaneously. The results shown are totals Emissions Unit Identification All Power Trains Identical

Phasers, boilers & heat capture energy conversion system module, per 12 mW

(2 x 85 GJ or 80 Mbtu) ecoPHASERs:

ecoTECH Power Station Module: Schematic DiagramecoTECH power stations are built in a series of 12 MW -24 MW modules for maximum flexibility of load demand response and off-line maintenance cycling, so that modules can overlap for full 100% coverage.

See Also:ecoTECH Power shaping technology

for green energy grid balancing:h t tp : / /www.ecophase r.ca /pd f /Green_Power_

Stabilization_eT_VIEWresolution.pdf

© Copyright C. Victor Hall & ecoTECH Energy Group, Inc. 2007/2012

www.ecotechenergygroup.com www.ecophaser.ca

www.etwm.ca

Mk V ecoPHASER Reactor Cutaway View (looking head-on to the flame).

Secondary VortexCombustion Zonewith slurry, emulsion,

+ syn-gasinjectors.

Primary Gasifying Zone

Technology advantages of the breakthrough ecoPHASER SSW BURNER• Near ZERO NOx !

• Radiant, even burn• Burns any combustible gas

•Continuous development of this technology.

• Long Hot Zone residence times•Maximum thermal oxidation of contaminants• Exclusive to the ecoPHASER

SOLID FUEL SUBLIMATION

(PRODUCER) SYN-GAS PULSED BURN

Head Office & Main Laboratory:Building #1 - 26633 Gloucester Way,Langley, British Columbia, V4W 3S8

CANADA

www.ecotechenergygroup.comwww.ecophaser.cawww.etwm.ca

tel: +1 604 755 9363e-mail: info@ecth.ca