INTRODUCTION

Drying Indonesian Low-Rank Coalat Electric Power Plants for INDIA.

Direct Coal Drying Of LRC atThe Head End Of Steam Generating Boilers

For Injection Directly Into Steam Generator

Direct Coal Drying Of LRC

at

The Head End Of SteamGenerating Boilers For Injection Directly Into

Steam Generator

PREFACEProject documentation underwrites the effective use of the following

Electric Power Generation

To introduce a prospective party to Develop and Finance a Head End DryingTechnology , with a super efficient power generation system utilizing the LowRank Coal situated directly on the coal concession.

The power produced to be sold to the power grid. Enter into PPA with the Indiannational power company to directly supply electricity to them. InvestmentApproximately 1.0 Billion USD.

As our ADVISOR and CONSULTANT to seek and collate information, documentand secure promote the above Proposed JV Investment Schemes to Investors,Technologies Provider and Funders. In connection with the Proposal Investmentinclude the sourcing of requisite professional eg, Lawyers and financial advisersto facilitate or assist in the Proposed Investment, if required.

Business Development

DirectorMr Robert Polce

GeoAsia LtdCEO - GeoMax LRC Processing System

DirectorMR Max Butt

Oriental Power Shenzhen Chang Sheng Investment Co. LtdBusiness Development and Consultant for GeoMax LRC ProcessingSystem.

DirectorMR Subhangshu DuttKrishnapatnam PortShipping and Handling - Annually 20 millions Coal.

DirectorMr Balathandautham TAM

Extreme Energy India Private LimitedBusiness Development for Coal Supply for India

Board of AdvisersTechnical AdvisoryPaul Muncy

Plasma Arc Technology. From humble beginnings in 1984 as a coal mining company, Allied investedin crude oil production and related technologies which include Secondary Oil Recovery and WellStimulation with Steam Technology. Given the philosophical shift to green technologies, the companydiversified to embrace the latest methods for energy independence and sustainable industries, Allied isheavily invested in Plasmafication and Hydro-Electric projects. Our goal is to provide Clean WorldSolutions in the reduction of the Carbon Footprint and help create a sustainable world. CTO fordevelopment of Iron Ore and Coal Properties in South East Asia. Muncy will retain his board position atAllied Energy. These changes in the corporate structures of the family of companies increases the worldwide position in developing "Syn Gas" uses and clean coal technology.

Technical AdvisoryDr K.Vijaykumar

Dr K.Vijaykumar is a Technocrat, B.Tech. Mechanical engineering with post graduate degree M.Tech.in Industrial management and systems from IIT ( Indian Institute of Technology) , Chennai. (One of thepremier technology institutes in India), Ph.D. in Energy Economics from Andhra University, India. Hehas over 30 years functional experience in engineering, design, Energy, Maintenance , projects and ITin one of the largest Public sector Companies in Petroleum Industry ( M/s Hindustan PetroleumCorporation Ltd.)

Technical AdvisoryDr PISHVA, Davar

Dr. Pishva is a professor at Ritsumeikan Asia Pacific University (APU) in Japan. Hehas an Electrical Engineering and Computer Science background and has obtained aPhD degree in System Engineering from Mie University, Japan. He has been active in

both academia and the industry. Throughout his career, he has been investigatingapplication of ICT in numerous fields and possesses many patents. One of his recentresearch interests is energy efficient environmental technologies and sustainable energyresources. He teaches environmental technology management at the graduate schooland supervises students research in the field.

THE PATH TO REFINED COALTHE MILESTONES OF INNOVATION

BY GEOASIA / APRM ALLIANCE

Since 1996, the Company has successively developed five generations of dilute phasedifferential pneumatic systems (DPT). The first application of Pneumatic Systems used toprocess Low Rank Lignitic Coal began in 1997 on a project with the electric utility, PacificCorp toupgrade high moisture lignite coals from Australias Hazlewood and Morwell seams. Later,PacificCorp successfully used the Pneumatic System to upgrade Wyoming Centralia lignite coal.Use of this Pneumatic Acceleration System removes moisture mechanically rather than usingsystems that require heat to evaporate moisture from the raw material. In production, thematerials are passed through the accelerator where carbon and water are separated by usinglow pressure high volume air exchange injected into the product which separates the twomaterials in structural form rather than using the eutectic phase change of water to steam toreduce moisture and increase calorific value. The end result is a dry coal product which issuitable for further processing. Product particle size is dependent on several interactive physicalprocesses but as a rule the particle size becomes smaller as more processing is used to removewater.

These companies believed that developing synthetic fuel from coal fines was its best bet forcommercializing this technology. One reason for this strategy was the fact that it enabled thecompany to take advantage of significant tax benefits. After two Arab oil embargos in a singledecade, The US Congress created a federal synthetic fuels tax credit (Section 29) in 1979 topromote alternative energy production within the United States.

For about 10 years, these Coal Processing Plants were installed and operated to removemoisture, ash and sulphur. These plants where constructed at mine sites and directly at powerplants to produce agglomerate coal briquettes for consumption by some of the largest electricpower producers in the United States . The companies involved in the development of theseplants, Covall, Headwaters and Terra Systems built over 30 coal drying plants and coalbriquettes plants for Power Plants . Headwaters' share price rose 383 percent during the 2001calendar year, reported the Salt Lake Tribune,making it the best-performing stock among Utah'spublicly held companies as a direct result of this programme .

The Synthetic Fuel Tax Credit Programme (known as Tax Credit Section 29) in US that began in1998 was discontinued in 2007, and all the plants were idled and subsequently dismantled asscrap steel salvage. Without the aid of the tax credit, it was no longer commercially viable to usean agglomerated coal product due to the fact that ROM (Run-Of-Mine) coal in the US is veryin-expensive. Economic pressure on coal is further exacerbated by increased production ofMarcellas and also because of the massive availability of natural gas , which is a cleanerburning fuel with a substantially lower price .

AGGLOMERATION

Our engineers have spent nearly a decade successfully developing our agglomeration processes,which recombines small particles of coal (coal fines) into briquette or pellet fuel which can beused in the same manner as the parent coal to power coal fired steam electric generationstations.

The refined fuel, GeoMax Coal is produced using carefully formulated binders that will notdamage the boiler or its coal handling equipment. The binders used in our agglomerationprocesses are the result of over a decade of experimentation and successful commercialapplication by 28 US power companies.

A NEW FUEL

It was quite difficult (in the beginning) to get the electrical power utilities comfortable with theidea of introducing a processed fuel that contained relatively unknown binders into commercialboilers. Sophisticated demonstration of the attributes of these finished fuels in a 5 megawattinstrumented test boiler showed that the processed fuel performed as well as the parent coal fromwhich it was made. In some cases the processed fuel proved to be a more stable fuel than theparent coal. In the end, millions of tons of agglomerated fuel were burned by US powercompanies over a 12 year period with no major issues reported.

During this development period, the engineering staff successfully managed to light a new way ofrelating to coal fuel production. Not only is it sufficient to dry mined coal, processing has to takeinto consideration each of the major attributes by which coal is graded. By comparing the rawcoal structure to the GeoMax Coal finished product specifications, sub-structures in the productunder manufacture can be manipulated to produce a consistent refined coal fuel which does notchange significantly from batch to batch. Additionally, a specific set of attributes may be specified(by the customer) before the GeoMax Coal is produced.

APPLICATION IN INDONESIA

In Indonesia, the Pneumatic Accelerator System, sub-structure formulation and agglomerationprocesses will be combined into a unique system that will produce GeoMax Coal. Starting withhigh moisture (35-50%), low calorific value coal, refined GeoMax Coal will be produced in modernfacilities in commercial quantities.In recent testing, an LRC with a moisture content of 52% and a calorific value of 3,056 KC/Kg wasused as a processing material to produce GeoMax Coal with a moisture content of 8.02% and acalorific value of 6,488 KC/Kg.

RECENT MILESTONES

1997-2007

Twenty-eight Syn-fuel plants are built using agglomeration technology developed by ourengineers. The fuel was used by power plants throughout the US to boost the quality of theirboiler feedstock.

1997-2011Two PAS separation systems where constructed, predecessors to our GeoMax system.

2009-2011

The GeoAsia Group of Companies is formed with seasoned industry professionals andspecializes in financing coal transactions with customers in India, China and SE Asia. Alsoinvolved in trading of iron ore and nickel from Indonesia

July 2012GeoAsia is granted exclusive rights to a patented coal drying/upgrading technology inIndonesia

August 2012GeoAsia signs an MOU with Oriental Power to supply coal to as many as 42 Chinese powerplants

September 2012GeoAsia signs joint venture agreement with an Indonesian mining company to develop a mineconcession with proven coal reserves of 130M metric tons and total in-ground assets worth$4.5 Billion

January 2013GeoAsia Ltd signs a JV agreement to joint venture with a second Indonesian mining companyto develop a 90,000 ha. (347 sq. mile) resource with proven coal reserves of 337M tons andtotal resources of over 2 Billion tons.

April 2013GeoAsia engineers design DPT system for compliance with Indonesia environmental andoperating conditions.

May 2013

Site Licensing Agreements will be issued to Asia Pacific Resources & Mining Pte Ltd (APRM)our partner for Total Mine Development to build Coal Processing Plants in Asia.

To quickly develop market awareness of GeoMax Coal and GeoAsia, we will continue to usewell-connected third parties to facilitate meetings with top power, cement and steel companiesin all Asian markets. In our experience, such third parties are able to quickly arrange meetingswith key decision makers; they understand the corporate cultures and priorities of thecompanies we meet; they provide political support; and thereby save us time, effort andfrustration as we define our working relationship with these companies. So the decision wasmade to grant Site Licensing Agreements will be issued to Asia Pacific Resources & Mining(APRM) our partner for Total Mine Development to build Coal Processing Plants in Asia.

Existing Power Plant Modification

GeoAsia proposes to apply its proprietary GeoMax Kcal+ coal drying process, to arecently commissioned electric power generation station which is owned by PT PLN(Persero). The power station that is being investigated for suitability is the relativelynewly installed PTLU Tarahan facility. This station, commissioned in 2012, is situatednear Lampung South Sumatra Indonesia.

From an engineering perspective, our primary concern is to facilitate the installation ofour equipment, with minimal interruption to the current operations of the station. This willbe accomplished by locating our coal drying equipment in proximity to the CoalPulverizing Equipment.

As shown in the basic sketch below, GeoAsia will re-engineer the area between items#1 and #4. The ideal footprint addition is anticipated to be approximately 60 ft. (18.288meters) by 80 ft.(24.384 meters). This configuration may be compacted thru verticalstacking.

:Typical (Rankine Cycle) Thermal Coal Fired Power Station (Non-IGCC)

1. Coal conveyor 2. Stoker 3. Pulverizer 4. Boiler 5. Coal Ash 6. Air Preheater 7.Electrostatic Precipitator 8. Smoke Stack 9. Turbine 10. Condenser 11. Transformers 12.Cooling towers 13. Generator 14.High Voltage Power Transmission LinesGeoAsia will install its equipment between the Pulverizer and Boiler.Pulverizer : The coal is put in the boiler after pulverization. A pulverizer is a device forgrinding coal for combustion in a furnace in a power plant.

Types of Pulverizers

Ball and Tube Mill

Ball mill is a pulverizer that consists of a horizontal rotating cylinder, up to threediameters in length, containing a charge of tumbling or cascading steel balls, pebbles,or rods.Tube mill is a revolving cylinder of up to five diameters in length used for finepulverization of ore, rock, and other such materials; the material, mixed with water, isfed into the chamber from one end, and passes out the other end as slime.

Ring and Ball

This type consists of two rings separated by a series of large balls. The lower ringrotates, while the upper ring presses down on the balls via a set of spring and adjusterassemblies. Coal is introduced into the center or side of the pulverizer and is groundinto powder, as the lower ring rotates causing the balls to orbit between the upper andlower rings. The coal is carried out of the mill by the flow of air moving through it. Thesize of the coal particles released from the grinding section of the mill is determined bya classifier separator. These mills are typically produced by B&W (Babcock and Wilcox).

Boiler : Pulverized coal is drafted or injected into boiler where it is ignited. Thiscombustion process heats water or other is heated and circulated until the water isturned in to steam at the pressures required by the Steam Turbine Manufacturer.

Coal is burned inside the combustion chamber of boiler. The products of combustionare primarily Hydrogen and Carbon based coal gases and particulate of non-combustedelements. These gases which are at high temperature vaporize the water inside theboiler to steam. Some times this steam is further heated in a super-heater as the higherthe steam pressure and temperature the greater efficiency the steam turbine will have inconverting the heat in steam in to mechanical work. This steam at high pressure andtemperature is used directly as a heating medium, or as the working fluid in a primemover to convert thermal energy to mechanical work. This mechanical energy is thenconverted into mechanical energy (rotary motion) which is coupled to an electrical

current generator. Although other fluids are sometimes used for these purposes,demineralized water is by far the most common, because of its economy and its suitablethermodynamic characteristics.In point instant, the TARAHAN system is manufactured by JINAN BOILER GROUP CO.,LTD. Shandong , China .http://www.jnboiler.com/en/index.aspx?lanmuid=71&sublanmuid=681Of particular interest to our engineers, is the configuration and specifications of thepulverized coal transportation system between the pulverizer and the combustion inletof the boiler train. As the Chief Technology Officer of GeoAsia, I would intend to workwith plant operations and engineering and purpose that positive positioning gatedampers be installed in the coal fines transport system, which would allow metering ofthe coal feed going into the steam generator. By design, the GeoAsia system requirescoal feedstock similar to the coal which is presently being fired at PTLU Tarahan. In anover simplified description of the GeoAsia system, our proprietary technology removesentrained water from a eutectic composite material by dilute phase differentialpneumatic system fed by low humidity air stream.In previous operations, we have been able to reduce moisture from Low Rank LigniticCoal in Indonesia from levels around 50%, down to a total moisture of 8%.Our operational goal is to design a parallel system where the dried coal can bemetered into the boiler along with your existing wet coal feed. At the same time, wewill proportionally reduce the existing wet coal so that the control room operators cankeep the flame path at its optimum efficiency without losing flame. Because the lowermoisture of the GeoMAX, we would anticipate that the fire-stream can be maintained atthe desired point of going over the crown into the economizer.In using the GeoMax dried coal product, we predict that the emissions will be reducedfrom the stack, the flow rate and efficiency will increase and the operating costs willdecrease.

Outside Technical Source: http://powerelectrical.blogspot.com/2007/03/thermal-power-plant-layout-and.html

GEOMax LRC PROCESSING SYSTEM

Detail System Information

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Table of Contents

Description pagesOverview 35LRCpictures 6TechnicalPaper 79SiteProcess 1012List 13

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Overview

The Proprietary LRC Processing System (GEOMAX LRC PROCESSING SYSTEM) Technology comprises a gas linear particle accelerator that transports and processes bulk material at high velocity in a particle isolated state, using air as the medium of movement.

The system is a unique gas linear particle accelerator, which permits a uniform dispersal of materials at a high degree of particle isolation. The dry process method utilizes air (or other gases) as the medium of movement, carrying bulk materials at high velocity but low pressure. The system can transport almost any particle, for any duration of time, at any temperature, and at any velocity/density ratio (a key principle in fluid dynamics). The combination of the system's ability to isolate particles and to transport them at high (and varying) velocities permits bulk materials to be accelerated, stratified, and electrified (the particles absorb electrical properties). As a result, the system can process industrial bulk materials in a variety of ways, including: separating, pulverizing, drying, classifying, mixing, forming, transporting and trans loading. These processes are seen as broadly applicable to handling coal, coal ash, rice, grains, precious metals and waste materials, to name just a few. The system has six basic components:

1. Pneumatic injector feed system 2. Motive force delivery package 3. Transmission lines to the exclusive accelerator assembly 4. Accelerator assembly 5. Product lines through which bulk materials are transported 6. Computer operated controls 7.

GeoAsia Proprietary system utilizes slow-moving laminar gas to transport bulk materials through a carrying duct. The gas flows at high velocity, but at low pressures and temperatures. Differential velocities create a "boundary" layer of air next to the outside wall of the conduit pipe and the center flow of the material much like "currents in a river". The main central current is faster than the outside current, thus protecting the bulk material from the walls of the pipe. When the gas in the pipe is accelerated, it creates an optimal differential environment, in which velocity controls density. The faster velocity in the center of the duct and the differential velocity with the boundary layer, puts the particles into a "high-spin state". This "spin state" provides a mechanism to dry the material while it is being transported as well as creating electro-magnetic, electro-static and electro-plasmatic properties if so desired.

In this accelerated state, the particles can be reduced in size by: 1.) colliding the particles with each other as they move irregularly through the duct at high velocity or

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2) directing

the particles to strike an ablative plate - the particle size determined by the impact velocity which can be finitely adjusted by the system's unique accelerator.

Functionally, GeoAsia unique system can perform a variety of physical procedures. These primarily include:

1. Isolating particles 2. Pulverizing (down to very fine pharmaceutical compound size) 3. Drying 4. Classifying/Sorting 5. Mixing 6. Forming (pelletizing, briquetting, etc.) 7. Transporting

8. Trans loading (transferring from one mode of transportation to another) Economic benefits from utilizing the system include:

1. Higher unit prices of end products through drying, classifying, upgrading, beneficiating, concentrating, etc.

2. Lower unit costs of production through greater efficiency, use of air as a medium of movement rather than water, systems ability to perform multiple task at the same time, no requirement for chemical additives and lower maintenance costs.

The GEOMAX LRC PROCESSING SYSTEM Technology is applicable to both organic and inorganic materials. Virtually all bulk materials used in basic industries can use the technology, such as:

Agriculture

Used in the drying of grains, sugar, etc. Soil reconditioning by restoring depleted trace elements.

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Coal

1. Moisture Reduction 2. Ash Removal 3. Micro-pulverization (to 80% less than 325 mesh) 4. Bulk Transportation 5. Reclamation of gob (waste) piles

Mining

Precious metal classification and concentration

Environmental

Dry/Extract/Remove of Waste from:

Industrial Process Streams Animal Agriculture Food Processing Human Waste

Construction By-product beneficiation (i.e. Fly Ash)

Ronald L. Frank, Executive Vice President of Ecology and Environment states: "We are impressed with the potential applicability of GeoAsia LRC system to a wide variety of environmental issues. In particular, we believe the ability of GeoAsia system to operate without water will become an increasingly attractive attribute in the worldwide marketplace. GeoAsia anticipates it will share in the economic returns from the use of its technology through fees, royalties and/or profit sharing.

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LRC Processing System GEOMAX LRC PROCESSING SYSTEM Configurations:

Installation in US

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FIG.1isaviewinelevationofarepresentationofthepneumaticmaterialsconveyorofthepresentinvention

Fig15ViewofVesselandseparator

TechnicalInformationGeoAsiaLtdhasdevelopedauniqueandforwardmethodwhichisdesignedtoeliminatemoisturefromLignite,SubBituminousandotherLowRankBituminousCoals,typicallyfoundinabundantsupplyinIndonesia.Thissystemcanbeinstalledattheminesitewhereitdriesthecoalandconvertsthelowgradematerialintoahighlydesiredbriquette.ThebriquettingprocessproducesaproductknownonthemarketasGEOMaxKcal+COALPRODUCT(RegisteredTrademark).ThesignificanceofthisproductisthatthepurchasingpowerplantgetsaconsistentproductwiththesamekCal,Moisture,Ash,Volatile,Hardgroveandothercontractedspecificationsoneveryorder,everyshipmentreceived

ABSTRACTA dilute phase pneumatic materialsconveyanceapparatusisdisclosedhavingapneumaticacceleratorwhich iscapableofconveyingmaterials throughagasstreamwhich is selectively patterned. Theconveyance apparatus also includes asourcegasmanifoldandcontrolapparatuswhich enable selective control of theapparatuson a real timebasis to achievedesired gas pattern flows through theapparatus to achieve selected particledispersion, isolation, stratification,electrification, classification andentrainment of material and to convey itthrough a processing conduit. Theconfigurationoftheconveyanceapparatusalso enables further processing, includingdrying, sorting, pulverization andclassification of the materials. Theconveyance apparatus also enables classification of materials based on theaerodynamic diameter of the particlesbeing conveyed because of the ability toachieve particleisolation.

SUMMARYOFTHEINVENTIONIn accordance with the present invention, a pneumatic materialsaccelerator and conveyance apparatus is configured to produce aselected gas flow pattern at high volume, low pressure to providecontrolled conveyance of multi 60 phase materials, to selectivelydisperse, isolate, stratify, electrify and classify the particles beingconveyed and to enable further processing of such multiphasematerials, includingdrying,pulverizing, stratifying, sortingand clas

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Fig3isaplanviewofthepneumaticacceleratorofFIG.1

sifying. Because the configuration of the present invention 65 enables a selected andcontrolledgasflowpatternforentrainmentofparticulatematerials,theconveyanceofsuchparticulate matter is also selectively controllable to reduce wear in the apparatus and toreducetheoccurrenceofundesirableprocessingconditions,suchasblowback.The pneumatic materials accelerator and conveyance apparatus of the present inventiongenerallycomprisesaplenumhousing inwhich ispositionedanozzle,afeedmechanismforintroducing a material, such as a particulate material, into the selected gas flow patternproducedinthenozzle,gas inletspositioned intheplenumhousingfordeliveringgastothenozzleinaselectedmannertoproduceaselectedandcontrolledgasflowpatterntherein,andaprocessingconduitforconveyingthemultiphasematerialtoanendpoint.Asusedherein,"multiphase"referstoconveyablematterwhichiscomprisedofasolid,liquidorgas,oranycombinationthereof.Asourceofgasisassociatedwiththeplenumhousingtoprovidegastothegasinletsinaselectivelycontrolledmanner.Controlapparatusmayalsobeassociatedwiththegasinlets,plenumhousingandsourceofgastoprovidesuchcontrol.Theconfigurationofthepneumaticmaterialsconveyanceapparatusofthepresent inventionenables the establishment of a selectively controlled gas flow pattern,which is initiated atintroduction of gas through the gas inlets into the plenum housing, and is substantiallyestablished at the point where the nozzle, in proximity to the end point of the feedmechanism,directsthematerialsentrainedgasflowtotheprocessingconduit.Theestablishedgas flowpatternmaybeeitheran irrotational (i.e., linear) flowpatternor a rotational flowpattern(i.e.onehavingavortex),butineithercase,theabilitytocontrolthegasflowpatternenables the material to be conveyed at low to negligible static pressures in a distinct,threeregion flow pattern comprised of a turbulent core, a laminar boundary layer and anintermediatetransitionregion.Thecontrolledflowpatternreducestheincidenceofparticulatematerialcontactingorstrikingtheinnerwalloftheprocessingconduit,therebyreducingwearontheapparatus.The present inventionmore specifically comprises a pneumatic accelerator ofwhich a feedmechanism,includingafeedconduit,theplenumhousing,nozzleandprocessingconduitareapart. The feed mechanism of the present invention includes the feed conduit, which isattachedtotheplenumhousing,andmay includeastructuredfeed inletforreceivingabulkmaterialpriorto entry into thefeed conduit. The feedconduit may either bestationary relative to theplenumhousing or may beaxially adjustablerelative thereto for providingmore finite control of theintroduction of particulatematerialstothe gas flow. Insome embodiments,the feed mechanism may further include an auger orextruder located inornear the feed conduit to direct particulate materials toward the nozzlewithintheplenum.Theplenumhousingincludesoneormoregasinletsthroughwhichgasisintroducedfromthemanifold.Asusedherein,theterm"gas"ismeanttorefertoandincludebothasinglegasoramixtureofgases,asdescribedmorefullybelow.Theplenumhousingisconfiguredtoreceiveanddirectthegas inamannerwhichachievesahighvolume, lowpressureflowofgas intowhich the particulatematerialsbecomes entrained.More importantly, the plenum housingandnozzleare configured toachieveandmaintainahighvelocity/lowpressure irrotational(linear) or rotational (nonlinear), three region flow into which the particulate material isintroduced and conveyed in dilute phase to the endof the system. The nozzlewithin theplenum housing is positioned about one end of the feed conduit and is axially alignedtherewith.An annular space isprovidedbetween thenozzle and the feed conduit throughwhich gas flows. The annular space between the feed conduit and the nozzle may beselectivelyalteredtocontrolthegasflowpattern.Further,theinnerwallofthenozzlemaybepreferablycurved,ormaybe linear,and theconfigurationof thenozzlemaybeparticularlyselected toachieveadesired flowpattern in the5conveyanceof thematerials.Thenozzleconfiguration also enables controlled acceleration, dispersion, electrification, isolation andstratification of the particulate materials prior to the point of entry into the processing

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conduit. The gas and entrained materials are then conveyed at high velocity and 10lowpressurethroughtheprocessingconduittotheendofthesystem.Theconveyedmaterialsmaybefurtherprocessed,suchasbyphaseseparation,pulverization,classification and drying. Additional structures may be associated with the pneumaticmaterials conveyor to enable further processing, such as one or more capture vesselsarranged in seriesorparallel,oracombinationof seriesandparallel.Capturevesselsmayinclude a cyclone, bag house, mixing bin, pulverization chamber, classification chamber,productbinoranyother20typeofdevice.The pneumatic materials conveyor of the present invention is principally structured toachieve high volume, low pressure gas flows to achieve the described principles ofmaterialsconveyance,butalsomimicstheabilitiesofdeviceswhichproducehighpressure,low volume gas flows to achieve a vacuum pressure for conveyance ofmaterials in thatmaterials can be conveyedmore efficiently and over longer distanceswith the presentinvention. The ability to achieve and control vacuumpressures in thepresent inventionenables it tooperatewithoutblowback.Also, the inventioncanprovideawide rangeofgasflowvelocities,foraccommodatingthehandlingrequirementsofvariousmaterials,bythe axial adjustment of the materials feed conduit in relation to the nozzle, while notmodifyingthevolumeflowratefromthegassource.Thepneumaticmaterialsconveyorofthepresentinventionhasfewmovingparts(i.e.,thefeedconduit,nozzleandauger,whenused),andisconfiguredtoreducecontactbetweentheparticulatematterandtheapparatus,therebyeffectivelydecreasingthepotentialformechanical failureand increasingsystemproductivity.Because the inventionusesso fewmovingparts,itcanbesetupinanydesireddirection(e.g.verticalorhorizontal),therebyaccommodatingawidevarietyofapplications.

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GeoMaxLRCProcess

SITECUSTOMIZEDEQUIPMENTStep1DumpSiteSelection:ConsiderationmustbegiventoIncomingRawCoalregardingingressandegressoftrucks.Furtherconsiderationisnecessarywheretherawfeedstockiswaterladen.Constructionofthedumpsiteonaphysicalelevationwhichallowsfornaturaldrainagefromthematerialisofconcern.Furtherconsiderationshouldbegiventoweatherpatterns.Thefeedstockshouldnotbestoredwhereitcanbecomefloodedduringmonsoonorotherweatherevents.Ifyouhaveahillsidearea,alargeconcretepadcanbeinstalledwhichallowstruckstobackupanddumpattheedge,whereitwillgravityintoaconcretebin(orSilo).Thefloorareaisdesignedwithaheavysteelgratecapableofsupportingthetrucks.TheopeningsinthisgratebecometheFirstLineseparationoftrampmaterialsIE:LargeRocks,TreeLimbsandRootsandothertrampmaterial.Thesizingoftherawfeedstockoccurswhenlargelumpsofcoalarebrokenupsothatitfallsthruthegrate.Thedumpattendantwilleitherbreaklargelumpswithamanualprocessorsmashitthruthegratewiththebucketofanendloader.Dependingontrucklogisticsandfeedrates,trucksmayberequiredtodumponthepadandformastoragepile.ThispileofmaterialcanthenbescoopedintothehopperbyamachineoperatorandendloaderorDozier.Ascalehousemayberequiredifcoalisbeingcomingledfrommorethanoneconcessionowner.Otherwise,thescalesystemattheplantwillbethecontrollingstandard.2)FeederBreakerCoal DragChainFeederBreakerisSecondSteptoresizethefeedstockintoauniformmediumwhichinapproximately2.5X0.Thebreakerconsistsofarotatingdrumwhichhashardenedbitprotrusions.Byadjustingthedrumclosetothechainconveyor,thefeedmaterialischoppedintosmallpieces.Thechainconveyor,(DragLine)pullstherawcoalpastthedrumandfeedsitontoabeltwherethematerialisweighedbyadigitalscale.Thematerialcanbebufferedintoastoragehopper,orfeddirectlytothedryer.DependingontheHardgroveGrindofthecoal,theengineeringdepartmentwillmakeadeterminationwithregardtodivertthematerialtoaballmillforfurthergrinding,ifrequired.3)DigitalControlSystemUtilizationofastateoftheartcomputerizedcontrolsystemwithfullintegration,willcontrolallvalves,softstartmotorcontrolsystems,gates,liquidspumpsandIOInterfacewithdownstreamcomponents.

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SITECUSTOMIZEDEQUIPMENTa)StackerConveyorisrequiredtoliftthefeedstockfromitsinitialdumpingpoint,intoaStorageSiloorBin.Ifused,thismachineislocatedbetweentheFeederBreakerandtheBufferStorageb)BucketLiftDependentonsiteconfiguration,abucketliftmaybesubstitutedfortheStackerConveyor.ThephysicaltradeoffisthefactthataBucketLiftrequiresasmallfootprint.NotethatBucketliftsaremoreexpensivetopurchaseandmaintainthanastackerConveyor.c)HopperConstructedfromPlateSteelandbeams,theStorageHopperissizedtoofferasystemruntimebufferof12Hrs.Thispreventsthenecessityofthesystemfrombeingrequiredtoberecalibratedasacoldstart.d)BeltScalestwo(2)independentbeltscaleswillbeinstalledtoweighthecoalinthefly.TheseDigitalScalesareintegratedintothemastercontrolsystem.Changesinweightsandvolumesaffectthethruputofthedryingsystemandarecontinuouslyadjustedbyacomputerizedcontrolsystem,inordertoobtainthedesiredmoisturelevelintheoutputproduct.Note:Variousmaterialshandlingsystemsincludingscrews,belts,chainconveyorsandpneumaticsystemsareutilizedtomovematerials. e)BallMill(AlternateRequirement)Ballmillwithapproximately2m3volumemayberequiredtopulverizethefeedstock.Thisistobedeterminedinengineeringphase.IntheStandardConfiguration,aballmillisnotrequired f)Baghouse(maybenotneeded)StandarddesignconfigurationutilizesaBagHouseforthepurposeofcapturingfineairbornefloatmaterial.Ifthefinaldesignfeedsanelectricalgeneratingpowerstation,thereisnorequirementforabaghouse,becausethesefinesarereconstitutedintotheinjectionstreamfortheCoalFiredSteamGenerator.InastandardSystem,thesefinesmaterialsarereconstitutedintothefeedstreamforthePugMill.4)ScrewConveyors,SolidsPumpsInadirectfeedsystem,therawcoalispickedupbyanArchimedesScrewConveyorandinjectedintotheDryingValveSystem.IfaBallMillisused,thefeedstockisconveyedinanairstreamdirectlytothedryer.5)JetSteamCompressorsfromBallmillMaterialisintroducedtoJetStreamofcompressedair.(HighvolumeAirStream)Thematerialisconveyedthruaspeciallydesignedtubewhichcreatesalaminarflowduetoitsaerodynamicdesign.6)DryerIneitherconfiguration(3or4)thematerialenterstheproprietaryDryerviaaJetStreamofAir.Dryerisfurtherdefinedinattachmentsherewithandmadeparthereof.Thecovalentbondsbetweenthewaterandthesolidsmaterialarebrokeninacoldprocess. 7)Cyclone/Separatorthefinalseparationofthemoistureandthesolidsisachievedinanofftheshelf,lowpressurecyclone.ThesolidsmaterialdroppingoutofthecycloneisreadyforfurtherprocessingintobriquettesordirectinjectionintoaSteamGenerator.

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SITECUSTOMIZEDEQUIPMENTPROCESSNOTE:Thematerialdryingphaseiscompletedatthispointintheprocess.ThematerialcanbeinjecteddirectlyintoaSteamGeneratoratanonsitepowergenerationstation.Thedriedmaterialissubjecttoreabsorptionofmoisture.8)FireSuppressionThedriedmaterialleavingtheDryingValveandCycloneisbelowitsInherentMoisture.InstallationofaCO2(CARDOX)andNitrogenInjectionSystemisREQUIRED.TherecanbenoresidencytimeinopenatmospherebetweentheSeparatorandtheendprocess,albeitdirectinjectionatanelectricpowergenerationstationorsenttothePugMillforprocessingintoGeoMaxBriquettes.9)PugMillMixerwillcomplywithfeedrateandresidencyrequirementsforinjectionofliquidsintoadrysolidsmaterial.ItisrecommendedthattheMixerbepurchasedwithsteamtrace.Theminimumrequirementisbasedona100tonperhourthruput.10)MixingTanks/BatchTanks/FuelStoragethestorageandmixingofBinders,basechemicalsandsolventswillbeperformedonsite.Variousformulasofbinderswillbeadjustedontheflyinordertoproduceaconsistentproductfortheconsumer.Cuttingagentsandsolventsarestoredinseparatetanksandaddedtotheproductasformulachangesrequire.OnSiteLabEquipmentandProcessSystemfeedbackwilladjusttherawmaterialsaccordingly.FuelStoragePrimaryandBackUptanksareincludedwiththeliquidscontainmentare.11)Extruder/BriquettePillowBriquettesarethelikelychoiceofourengineersbecausethehighlycompressedmaterialwithstandsthestressesofshippingandhandlingbetterthananextrudedproduct.However,thefinalproductwillbedeterminedduringprojectengineering,withtheinputofthecustomer.12)StackerConveyor/Stockpile/SalesYardConsiderationforingress,egressandloadingofthefinishedproductwillbecompliantwiththecustomersrequirement,duringtheengineeringphase.AnarticulatedStackerConveyorwiththeabilitytostackthebriquetteswillbedesignedtooperateonaconcretepadandtravelonarailsysteminaradiusofatleast180degrees.TheStockpilewillbemaintainedbyarubbertireendloader.Itisrecommendedthatthestockpileareabecapableofholding70,000metrictonsofmaterialwhichisprocessedandreadyforshipmenttotheenduser/customer.

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SITECUSTOMIZEDEQUIPMENTLISTActual Equipment list may vary

No. Machinery Description Notes 1 Feeder breaker Drag chain Jaw crusher 2 Stacker Conveyor 3 Bucket Lift Vertical Approx. 20M 4 Hopper vibrator Approx. 600 MT 5 Short Belt Scales Motor control 6 Ball mill to 7 Jet Steam Fan Cowling Motors 8 Dryer Vessel 9 Cyclone Separator 10 Pug mill 11 Mixing tanks Binder 12 Extruder 13 Stacker Conveyor To Stock pile 14 Controllers Motor controls 15 Strobes QC 16 CCTV QC 17 Automatic Oilers maintenance 18 Gen sets TBD 350-500KVA

THEPATHTOREFINEDCOALTHEMILESTONESOFINNOVATIONBYGEOASIA/APRMALLIANCEANEWFUELAPPLICATIONININDONESIARECENTMILESTONESCoal Drying Direct Injection for PLN - 2014.pdfTHEPATHTOREFINEDCOALTHEMILESTONESOFINNOVATIONBYGEOASIA/TERRA/APRMALLIANCEANEWFUELAPPLICATIONININDONESIARECENTMILESTONES

Proposed PLN Power Plant Modification Brief Jan 2 2014.pdfGeoAsiaproposestoapplyitsproprietaryGeoMaxKFromanengineeringperspective,ourprimaryconceAsshowninthebasicsketchbelow,GeoAsiawillrOutsideTechnicalSource: