CR0SS-RBPBR« C8S TO RELATED APRUCATIOWS

STATBMBNT REGAR ING FEDERALLY SPONSORED RESEARCH OR .DEVELOP ENT

Not Applicable

10 !MCO PO.RA110N-BY- REf iR£NCB Of- MATERIAL SUBMITTED ON A COMPACT DISC

Not Ap licable

The Inveriiive System disclosed herein relates to an improved system fo extracting

I S metals from ore.

Ore ss defined as a mineral or an aggregate of minerals from which a valuable constituent and more specifically, at least one metal can be extract d. Om mmt he processed to separate unwanted organic? and minerals, or other inorganic materials, front metal. Onee ore is processed, it may be refined to separate metals. For example, Cupel Islion is a refining method used to separate silver from lead. Complex res, as used herein, means aft ore in which the ratio of metal to aggregate. organic and inorganic .raatoriai is low or ore in which metal is difficult to separate from ag regate organic a»d inorganic material.

Known methods for processing "include exposing lime and/or cyanide to ore slurry or other similar leaching processes. These methods a e inefficient and costly when dealing with complex ores. Consequently, metals in complex ores may not ie extracted. Even If known me hods; for processing o e were efficient and inex ensive, they arc toxic t the. environment. These methods release toxic gases and chemicals and unprocessed water into the environment, Known methods may also require large energy input.

The inventive System, described herein, provides methods and apparatus that is used to process complex ores efficiently and Inexpensively. The Inventive System is also "green": ( f ) The air emissions meet or are significantly below current county-, state, and federal regulatory limits ;

(2) l*rpeess water is treated and disposed of using Best Available Control Technology (BACT)j to allow release ks to the losai sewer sys em.

(3) Power supply is regulated so that it is more efficiently used.

A _* DESCRI ^P TION OF PEIOi¾ ART

The ⁽ hernial fcreatmeat of minerals and metallurgical ores and concentrates to bring about physical and chemical transforations in the materi ls to en&hfe recovery of metals is known in the art. Such treatment may ro uce saleable products such as

Compoun s m alloys suitable as feed for further refinement, it is known that plasma environments can ^' provide high temperatures t fuel thermal treatment to refine metal. For example, plasma environment have been used to convert Iron sla to u e Iron, ore

Specifically, low temperature plasma torches have been used to bring about, thermal and physical changes in processed o e. Processed ore is. generally placed in a crucible and heated; tills type of s stem can be thougla o f as a furnace,

in a furnace environment aggregate organic and inorganic materials cannot be removed with just the addition of heat. Usually, en ironmemaiiy toxic chemicals ust be added to create art environment in which ore can be processed.

In order to process ore using a plasma reactor several issues must be considered, First, it is critical that, feed ore is exposed to the high heat produced by the plasma torch for a period of time su eieni to cause melting -or other reactions, Second, torch-eonsumab!e c mponen s show high failure rates and great inefficiencies. Third, it is known that high hea creates failure i prior art reactor walls. Fourth, prior art reactors cannot run at industrial efficiency. Processing ore at industrial efficiency requires: (a) a reactor that can process hundreds of pounds of ore within a short period of time; (b) constant reactor temperatures; (c) low failure rates and low material bre kdown of the plasma torch ami other reactor compone ts; and (d) reacto parts that arc «as.Uy accessible for service. Fifth, the ability to efficiently collect processed ore is vital. Finally, known reactors are not energy efficient.

li INVEN IVE SYSTE

The Inventive System provides a unique configuration that combines a plasma torch in conjunction with induction heat to roem .comple ores in order to remove unwanted organic and inorganic mater als, leaving only metals at industrial efficiencies with no release of toxic chemicals or gases into the environment The Inve tive System is shown, generally, in figs, t - 2, It should be note that the Inventi e System may, however, he embodied in m y different forms and should not be construed as limited to the embodiments set forth herein,

Referring to Fig. 1 , in a first mbodiment, the inventive System comprises an AMT Reactor™ (10), a bag house (700), and an oi¾as system (800).· Ore enters the Inventive System at (3 ) and is processed by the AMT Reactor™ (10). in the simplest scenario, processed ore is removed from the Inventive System at (2),

As ore is processed through the AMT Reactor™ (10) it releases gases such as carbon, sulphur, oxygen, and various combinations thereof As gases leave the AMT Reaotor ^iM (10) as (3) ore pastieuiaies, having lowe densities, ma be p« into the high te p mture bag house (hereinafter "bag house") (700). The bag house (700) comprises a plurality of filters to capture ore particulates. Because some of the ore particulates entering the bag house (700) contain metal, the recovered ore particulates ma be chemically treated (50) to remo e unwanted material, in a preferred embodiment the chemical treatment (50) may be an mid or base

Oases continue to move from the ba boose (700) to the ot ^' f*gs$ s stem SOU), i¾e off- as system (BOO) chutes and cleans process gases from the AMT R actor™ (10). T e off-gas system (800) runs at a vacuum or below airni?s heric p essure so that process gases move from the AMT Reactor™ (10) toward the off-gas system {80O}.

Referring to Fig. m a second embodiment, the Inventive System anther comprises a secondary melt s stem (900). At times metals are so ensconced in unwanted organic and inorganic materials that they cannot be completely processed in the AMT Reactor™ (10), in such Ά ease the ors Is also processed through s secondary me system (900). Hie $¾:0{idat melt system can be a second AMT Reactor™ ( f 0) ov conductive, coils, for ex m le. Even if a secondary melt system (900) is used, desired metal may still be shrouded in unwanted organic and inorganic materia! as it leaves the seconda y meit system (900) at {?), To remove the remaining unwanted rgan c aid i organic materials the ore may he further processed in chemical treatment (50).

in each of the above described embodiments, and any embodiments which are obvious variations thereof, the components of the inventive System are attached to each other with high temperature ducting. Hie Inventive System, regardless of embodiment, uses a proprietary I/O system io control everything from ore feed rate ^' s to the t pe of gases released throug the off-gas system (800). The I/O control system eonteinpOfMeonsi measu es flew rates into die AMT Reactor™ (S 0), through the bag house (700), and the off-gas system (800), It msa&aneoosi adjusts run en i nment so that gases and other toxins are appropriately treated hefoft release into the environment Conse uently* the amount of toxic gas and material released is closely monitored md. all released, gases add malerials are appropriately iteate d meet or are below all local, state, or federal regulatory fe uiremeuts.

. «¾Ef :mS€ P lO .0F THE SE¥IRAj, VIEWS OF. H DRAWI GS

Other features and advantages of the present iavgndont will become apparent in the following detailed descriptions of t e preferred embodiment with referenc to the accompanying drawings, of which:

Fig. 1 is a flow chart s owing one preferred embodiment of the inventive s stem;

Fig. 2 is a flow chart showing a second preferred embodiment of the inventive system;

Pig. 3 Is a cui-avvay view of the AMI Reactor™;

f ig, 4 is a detail, cut-swa view of the A T Reaet r™;

fig, 5 is a schematic of the Inventive System;

Fig. 6 is schematic of the torch, isolation valve;

Fig. 7A shows a -cut-awa view of an embodiment of the of© feed gysta;

Pig, IB shows a cut-away view of ^" another -embodiment of the ore feed system;

Fig, 8 is schematic of the fourth-chamber isolation valve;

Pig, 9 is a cut-sway view of a generic plasm torch.

The present invention is described more fully hereinafter with reference to the accompa in drawings, in which preferred embodiments of the invention are shown. This invention may, however, may be embodied in many different forms and should not be construed a limited, to the.embodtmems set i¾r herein; rather, these emhod »et>¾s are provided mat this disclosure ^' wOi e thorough and complete will full conve the scope of the m «atjo{s TO those skilled in the art.

Ift a preferred em o iment, the inventive System comprises tm AMT Reactor* ¹ * (10), a hag house (TOO), .and off-gas s stem (800). Jo another em diment, the in entive S stem comprises an AMT Reactor™ (10), a bag house (700), an off-gas system (800) and a -secondary melt s stem (900) .

AM .E ff¾ Referring to Figs, 3. - S, the AMI™ Reactor. ( 10) comprising a first cham er or feed chamber ( 100), a second chamber -or reaction chamber (200), -aad a plasma torch ( 00), The plasma torch (300) enters the reaction chamber (200) through the feed chamber (100), The plasms torch (300) has an active end ami m inactive end where the active end is the anode end (refer to fig, 9), The active end is placed into he reaction chamber (200), The depth of insertion is variable aad is de endent upon factors including but not limited to torch sate and AMT Reactor™ ( 1 ) size,

fCn wn methods ai¾ used to cool, each component of the A MT Reactor™ (10); more specifically, AMT Reactor™ (1.0) eomjKments ^' te cooled by circulating water and c olant through a coolajjj.manifold. The manifold is controlled by the proprietary Ϊ/Ο system mentioned above. Known methods are used to provide electrical power to the AMT Reactor™ (10),

Plasms torches are known in the art. A generic plasms torch is shown in Fig, 9, Burn as enters the torch at a cathode and tra els toward an electrical arc, becoming plasma, and e its through, to anode throat. The cathode in this instance Is positively charged and the anode is negatively charged, The two are electrically isolated from one another. The conducti ve as that becomes plasma is htitodiiced at a velocity that stretches the plasma arc beyond the anodes throat to thermally fe&et the ore being fed before the are returns and tennirta es OH the face of the _. anode. Many different types of bum gases have been used with plasma torches including air, oxygen, nitrogen, hydrogen, a gon, C¾ _s C2H4 arid G _$ ¾.

In a preferred embodiment, the plasma torch (300) is of the type where burn gas is fed into the p\ torch- (300) tangent to the anode and electrode. The plasma torch polarity is set to run in non-transfer m de, In a transfer plasma torch the are is looped from the torch ^e s anode to a ^* Vork piece" that has a negati e polarity., lite sixe of t e arc is limited in s ze by the distance between the anode arid the "work piece". A non-transfer plasma torch has both negative and positive polarity. In the Afvi ^' T Reactor the arc k looped from the electrode to the torch aozzle and does not have a size ilmitatton consequently, ore -can be continuously p ocessed through the AMI Reactor.

In a preferred embodiment, the feed chamber (1.00) is eonica!ly s aped having an input end (110) and an output end (120) where the input end (110) has a larger diameter thai} the output end ( 20), The input end (1 10) has a diameter sufficient m size to accept lasma torch (300) whore the plasm torch is of sufficient sixe to create the necessar temperature to create reaction In the ore. A person having ordinary skill in the art will kmrn that the. voltage of the plasma torch (300) will vary depending on various factors including bot not limited to the type of ore that is processed and the stee of the MT™ Reactor (10), amon other factors.

In a preferred embodiment _* the walls of the feed chamber (100) are angled, The angled feed chamber (100) walls allow more control over the feed rate of the ore into the AMI eac r™ ( 10), For example, ore having a smaller density may not properl enter into the reaction chamber (200) if the feed chamber (100) walls were notangled. The walls of the feed chamber (100) are angled at approximately 60°. H wever; depending on AMI Rencter™ (10) size and other factors including ho not limited to torch s ze and ore type, this angle may change, ϊη a preferred emlw imeoi _> she ias torch (300) is activated using helium. Because helium is costly, once the lasma torch (300) has been, established, it runs on -ar on. However, it should be noted that apart from cost, and temperature eettsidera ons, _. any known o unknown bum as raay be used to operate the .plasma torc (300),

Referring to Figs, 4 »» Sj the feed chamber (100) further com r ses ars ore feed s stem (550). he ore feed system com rises at feast one feed hopper 0$$) and a screw feeder sysism (580), The screw feeder s stem comprises a screw conveyor (556) and feed chamber valve (557) (shown in fig, 7). Optimally, the ore feed system ($50) has at least two feed hoppers (555) so that one feed hopper (555) can be loaded while the other is discharged inf the AM ™ Reactor To deliver ore to the feed chamber (100) oxygen is aspirated from the at least ne feed hopper (555). The a least one eed hopper (SS5) is back .filled with s carrier as. When the feed chamber valve (SS7) and the screw conveyor (556) are in the open position, feed ore and gas are delivered to the AMI ^' Reactor*** (1 ) through the feed chamber (100) through at least one teed tob ( 10 \) into the reaction chamber -(200). The ore feed system (530) deli ers feed ore and carrier _. gas alon the- same xis at whic the plasma torch (300) is inserted into the A T

eactor™(i0), In a preferred embodiments nitrogen is used as the carrier gas.

Referring to Pigs. 4™ 6, the reaction chamber (200) is, generally., tubular in shape- and comprises an input end (210) and an Output end (220). The length. of reaction chamber (200) is depende t on various factors including hot not limited to the AMT Reactor ^' *** (10) SIKS, plasma torch (300) size, and ore feed rates, amongst others.

The output end (120) of the feed chamber (100) mates with, input end. (210) of the reaction ch mber (200) using a flange (130), The reaction chamber (200) is radially surrounded by graphite (230), The graphite {230} is insulated and i ej! radially surrounded by heatin coils (240), in a preferred embodiment, the heating soils (240) are induction coils (240), The graphite (230) is radially insulated by a graphite insula ion blanket (231) id then a refractory lining (not ¾how»). The purpose of t e isductiert coils (240) is t o-fbid: (a) to keep the re ctor temperature at a relatively eonstaot level; ami (b) to create an electmroagaettc field which stirs ore as it passes throug the .reactor. In this c nfiguration graphite is allowed to expand or contrast w necessary,

The area between the reaction -chamber (200) and. die graphite (230) must be sealed to keep notorial from migrating outside ^' the AMT Reastor™ (10) md to protect iiiduelioii coils (240) from direct plasms arcing which would bu.ro the coils.

The output end {220} of the rection chamber (200) projects through the refractory base plate (233), The induction coil (240) is supported by the m& iw y base plate (233); the refectory base plate (233) sits on a water cooled base plate (234), This configuration allows the expansion of the reaction chamber (200) as necessary.

The plasma torch (300) enters the reaction chamber (200) through the torch seal housing (310) which mates with a torch Isolation valve (320) (See lso Fig, 6), The torch isolation val ve (320) creates a vacuum seal between i tself and the reaction chamber (200) and between it self and the torch seal housing (310). The torch seal housing (310) is made of rjon-conduetive material.

This eo figuration electrically Isolates the plasma torch (300) from the rest of the AMT Reactor™ (10). To perform ma ntenance on the plasma torch (300), the torch isolation valve (320) is sealed to maintain, the atmosphere to the rcaetkm c amber (200) _» and the plasma torch (300) is lifted out of the AMT e c r^ (10); The feed chamber (100) and th reaction chamber (200) re encompassed by the tertiary chamber (5(50). The tertiary chamber (500) allows paniculate and gas exhaust into- a hag house (700), in a preferred emb d ment, the tertiary chamber (300) comprises at least one chamber door (S30). The chamber door (530) allows access for maintenance. The tertiary chamber (500) is tubular in shape and comprises an Input end (510) and an output end £520),

To operate the AMT Reactor™ (10) air is aspirated, to create a low oxygen environment, from the feactiao. chamber (200) tsstng a- acuum pump. The syste then isolates the vacuum pump with a valve. The AMT Reac or™ (10) is then backfilled with inert g&s to near

atomospherie prssure. Then the plasma torch (300) is-igaited, and a mixtee of feed ore and gas are backfilled into the AMT Reactor™ (10), The at least one- feed hopper (555) is aspirated to remove oxygen. The at least one feed hoppe (555) is then backfilled with a gas, preferably the same as the buna gas, poshing ore into -the AMT Re ctor^ (10) through feed tubes (101).

Referring to Fig. 7, in one preferred embodiment, the at least one feed tube (101) simply releases ore into the reaction chamber (200), Referring to Fig. 78 _» in a second preferred embodiment, the at least one feed tube (101 ) is of an extended length, so that- it delivers ore closer to the plasma torch (300), The e tende feed tube (101) is adjustable and is angled. The angle is similar to that of die feed chamber (200) wall; die angle and length are dependent upon the type of ore that is being processed.

The output, end (520) of the tertiary chamber (500) comprises at least one quench ring (550). The, at least one quench ring (550) comprises a plurality of multiple gas npaades. As ^' processed ore fails through the reaction chamber (200), it passes through the quench rings (550) where it is sprayed by gas. Preferably, the quench gas is a noble gas. The purpose of the spray is twofold; (a) to atomize processed ore; and (b) to cool processed ore. Preferably, the gas nozzles are pointed toward die center of the a least one. quench ring (SSO) aud down toward the output end (620) of a fourth clssm her (600) ( im d below).

The fourth chamb r {600) comprises input end (630) and an output end (620), s a preferred embodiment., the fourth chamber is conieaHy s ipped where the input end (610) has a diameter larger han the output end (620), The output end (520) of the tertiary chamber (500) mates with the input ead (61 Q) of the fourth c amber. Th output end (6.20) of the fourth chamber (600) comprises a lower m isolation valve (540) (See also Fig. 8), The lower cone isolation alve (540) al ows the ap aratus to riiahttain a l w oxygen environment while allowing processed ore to be; removed md collected into ^' -a ooUec oa oaa or hopper.

Bag jlojj , As disc ssed above, particulates from AMT Reactor™ (10) may flow to a bag house (700). The bag house (70.0) is attached to tertiary chamber (500), As discussed above, there Is a n ati e pressure thai allows particulate matter to How front the AMT Reacto™ (10) to tile hag house (700), The bag house (700) c mpris s at least Ot e filter that &m filter out ore particulates before gases enter the off-gas system (800).

Off-Pas ^' ^vstem. As discussed above, the ofT-gss system (800) runs at & vacu m or below atmospheric pressure. This causes ases to flow from the bag house (700) to t off-gas system (800), The off- as system (800) uses known methods to filter sulphur and ether harmful gases that are received f o the AMT Reac o™ (10) before release of neutral gases feto the atmosphere.

$kMadam.$$$t Svsteay I» some eases, even after proeessmg ore through the AMT Reactor™ (10) _s valuable metal &y remain difficult to extract, in this case, the ore is processed through a Secondary Melt System (900), This system can he an inductive heat system or a smelter, for example. jf|¾jjj¾ jjff¾ For the Inventi e System to work optimally, the feed ore is delivered .into the feed chamber (100) as a fine mesh size and at a moisture level between 0 - 20%, Ore tot has high moisture content will dump together,. Clumped ore is heavier ar¾d falls; through the reaction chamber (200) t o quickly and, consequently, ore hang time is decreased. Hsgh moistTO e ftteaf also causes AMT i¾s¾ctor™(10) consumables, such as the torch head, to bum out mora quickly.

The reaction chamber (200) Is prepared for processing ore by removing oxygen from th reaction chamber (200). This ½ done by using a vacuum pumping system, in a preferred embodiment, o ce the pressure in the ie&ct n chamber (200) eaches close to 0 ps , the reaction chamber (200) is backfilled with burn gm< Optimally,, the AMT Reactor™ ( ! 0) runs at approximately 0-2 pst». So a preferred embodiment, the reaction chamber (200) is maintained at. about 3000 ° here the plasma torch mm ai approximate! y 23,000 "F. These parameters may vary depending on AMT e¾ctor™(10) size, type of Ore, and feed rate.