US20090200248A1 - Belt Filter Apparatus - Google Patents

Belt Filter Apparatus Download PDF

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Publication number
US20090200248A1
US20090200248A1 US12/299,386 US29938607A US2009200248A1 US 20090200248 A1 US20090200248 A1 US 20090200248A1 US 29938607 A US29938607 A US 29938607A US 2009200248 A1 US2009200248 A1 US 2009200248A1
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US
United States
Prior art keywords
belt filter
fine material
filter section
liquid
partially dry
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US12/299,386
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English (en)
Inventor
Kenneth Carl Van Rooyen
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Cabanga Innovations Pty Ltd
Original Assignee
Cabanga Innovations Pty Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Cabanga Innovations Pty Ltd filed Critical Cabanga Innovations Pty Ltd
Assigned to CABANGA INNOVATIONS (PTY) LTD reassignment CABANGA INNOVATIONS (PTY) LTD ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: VAN ROOYEN, KENNETH CARL
Publication of US20090200248A1 publication Critical patent/US20090200248A1/en
Abandoned legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/04—Filters with filtering elements which move during the filtering operation with filtering bands or the like supported on cylinders which are impervious for filtering
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/35—Filters with filtering elements which move during the filtering operation with multiple filtering elements characterised by their mutual disposition
    • B01D33/37—Filters with filtering elements which move during the filtering operation with multiple filtering elements characterised by their mutual disposition in parallel connection
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/44—Regenerating the filter material in the filter
    • B01D33/48—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
    • B01D33/50—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps with backwash arms, shoes or nozzles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/58—Handling the filter cake in the filter for purposes other than for regenerating the filter cake remaining on the filtering element

Definitions

  • THIS invention relates to a belt filter apparatus.
  • the invention concerns a belt filter apparatus for use in drying fine material, typically fine coal.
  • the invention also extends to a method of drying fine material.
  • Coal which is mined from the ground often contains unwanted impurities such as carbonaceous and non-carbonaceous material which are reduced to various different sized fragments. Users of coal, however, normally require coal of consistent quality. For this reason mined coal should undergo a process referred to as beneficiation, also known as coal preparation or coal washing. Coal beneficiation refers to the treatment of coal to ensure consistent quality and to enhance its suitability for specific end-users.
  • the treatment of coal will be dependent upon the physical properties of the coal and its intended purpose. For certain applications the treatment may simply require crushing while in other instances it may be necessary for the coal to undergo a complex process for reducing impurities.
  • coal In order to remove impurities, coal is crushed and thereafter separated into various coal fractions, whereafter the fractions typically undergo a further treatment referred to as dense medium separation.
  • dense medium separation In this process, the coal is separated from impurities by being floated in a tank containing a liquid of specific gravity, usually water holding finely ground magnetite in suspension. Due to the fact that the coal is less dense than the liquid, it will float and can be separated off while heavier rock and other impurities sink and can be removed as waste.
  • the process of beneficiation typically generates a fine fraction referred to as slurry, a slightly coarser fraction which is known as duff and an even coarser fraction known as discard.
  • a fine fraction referred to as slurry
  • slightly coarser fraction which is known as duff
  • an even coarser fraction known as discard.
  • the moisture would need to be removed from the fine fractions.
  • a South African context water is a scarce commodity and the use thereof consequently strictly controlled by the South African Department of Water Affairs and Forestry. It will, therefore, be appreciated that coal should be separated from the water in the slurry and duff in such a manner that the water can be re-used in future beneficiation processes.
  • the mining industry has for this reason developed various methods for drying fine and ultra fine materials. These methods typically utilise drying beds, belt filter presses and hydraulic filter presses. A brief description of the mentioned methods is provided below together with advantages and drawbacks associated with the methods.
  • Drying beds are normally provided by constructing lined, large surface area dams into which slurry can be placed.
  • the water can hereafter be removed from the drying beds with the use of, for example, penstock systems. Water is decanted from the surface of the slurry, the so-called supernatant water, and once the drying beds are dry the fine material is mechanically excavated and sold. Making use of drying beds has the advantage that once the drying beds are in place, drying costs are minimal while the drying beds can handle large volumes of slurry.
  • the drawbacks of making use of drying beds include a substantial capital outlay for constructing such drying beds, loss of water due to evaporation, loss of income due to delays during the period of drying, a potential for environmental spills due to over-topping and chemical breakdown of coal due to prolonged exposure to oxidation.
  • a belt filter press typically comprises two belts between which slurry can be placed and thereafter pressed.
  • a belt filter also makes use of a vacuum for sucking water from the filter.
  • the advantages of using a belt filter press includes that continued drying can take place, a relative small operating area is required and water that is removed from slurry can be recovered immediately. Further advantages include that the dried product can be added to the product line and a relatively quick turnaround of revenue is possible.
  • the drawbacks of using belt filter presses include high installation costs, high material and maintenance costs and consequential high running costs.
  • a very important drawback of making use of a belt filter press is that by compressing hydraulically placed material, the permeability of such material is reduced with a consequential reduction in the ability of extracting all free water. Compressing the water containing material only serves to increase the pore pressure of the material with the consequential result that the largest volume of water is extracted prior to compaction. Energy which is therefore used with a view of removing free water is in fact wasted.
  • a hydraulic filter press comprises a bag in which fine material can be placed whereafter the material in the bag can be compressed hydraulically.
  • the hydraulic filter press also makes use of a vacuum for sucking water from the bag. Upon completion of a drying cycle, batch material is blown from the bag into a bin and the cycle repeated.
  • Advantages of making use of a hydraulic filter press include fast recovery of water, a minimal potential for detrimental environmental impact and fast realisation of a saleable product.
  • the drawbacks of hydraulic filter presses include high installation costs, high running and maintenance costs as well as batch processing, i.e. there is no continuous flow of material and consequently large volumes of liquid should be stored.
  • Making use of hydraulic filter presses also results in compressed materials with increased pore pressure and reduced permeabilities similar to the situation with belt filter presses.
  • a belt filter apparatus comprising:
  • the permeable fabric of the first and second belt filter sections is a non-woven fabric or a micro-pore fabric.
  • the permeable fabric of the first and second belt filter sections includes reinforcing.
  • the permeable fabric of the first and second belt filter sections has a permeability of not less than 10 ⁇ 3 cm/s.
  • the permeable fabric of the first and second belt filter sections is a geo-fabric which is reinforced with nylon netting.
  • first and second belt filter sections are formed by providing a first set of pulleys and a second set of pulleys about which a single belt filter can be moved.
  • the means for mechanically placing the partially dry fine material comprises an impulse blower which is located proximate a drop-off point between the first belt filter section and the second belt filter section, in use the impulse blower serving to impart jets of air onto the first belt filter section such that the partially dry fine material on the belt filter can be forced therefrom to fall onto the second belt filter section.
  • the means for mechanically placing the partially dry fine material comprises a cam which is located proximate a drop-off point between the first belt filter section and the second belt filter section, in use the cam serving to impact on the first belt filter section thereby forcing the partially dry fine material to fall onto the second belt filter section.
  • the belt filter apparatus includes an agitator formation for redistributing partially dry fine material on the first belt filter section and/or the second belt filter section.
  • the agitator formation is provided in the form of at least one blower and/or at least one rotatable cam.
  • the liquid collection arrangement includes liquid collectors which are locatable below the first and second belt filter sections for collecting liquid which is removed from the fine material during the first and second drying cycles.
  • the liquid collection arrangement also includes ducting for providing fluid communication between the liquid collectors and a liquid storage container.
  • the method of drying fine material includes the step of providing a vacuum which is in fluid communication with the first and the second belt filter sections.
  • the mixture of liquid and fine material is coal slurry.
  • a belt filter apparatus comprising:
  • a belt filter apparatus comprising:
  • FIG. 1 shows a front view of a belt filter apparatus in accordance with a first embodiment of the present invention
  • FIG. 2 shows a side view of the belt filter apparatus
  • FIG. 3 shows a perspective view of a liquid collector for use in the belt filter apparatus of the invention.
  • FIG. 4 provides a diagrammatic representation of a belt filter apparatus in accordance with a second embodiment of the invention.
  • FIG. 1 and FIG. 2 show a belt filter apparatus in accordance with a first embodiment of the invention, generally indicated with the reference numeral 10 .
  • the belt filter apparatus 10 includes a support structure 12 comprising a number of support pillars 14 . 1 , 14 . 2 , . . . , 14 .n and support struts 16 . 1 , 16 . 2 , . . . , 16 .n which are configured as shown.
  • the support structure 12 carries a number of pulleys which are arranged to form a first set of pulleys 18 and a second set of pulleys 20 .
  • a single belt filter 22 is wrapped about the first and second set of pulleys 18 and 20 respectively to provide a first and second belt filter section 24 and 26 .
  • the belt filter 22 is produced from a non-woven fabric having a permeability of at least 10 ⁇ 3 cm/s.
  • the fabric is a geo-fabric produced by Kaytech and sold under the trade name BiddumTM.
  • the fabric of the belt filter 22 is reinforced with nylon netting.
  • a number of liquid collectors 28 . 1 , 28 . 2 , . . . , 28 .n are provided under the belt filter 22 in each of the first and second belt filter sections 24 and 26 .
  • each liquid collector 28 . 1 , 28 . 2 , . . . , 28 .n comprises a collector body 30 which is covered with a perforated deck plate 32 .
  • the liquid collectors 28 . 1 , 28 . 2 , . . . , 28 .n are connected in fluid communication with a liquid storage container, not shown in the drawings, via a network of ducting 34 .
  • the liquid collectors 28 . 1 , 28 . 2 , . . . , 28 .n and ducting 34 provide a liquid collection arrangement which is generally indicated with the reference numeral 29 .
  • the means for mechanically placing 36 is formed by firstly providing that the first belt filter section 24 includes a drop-off point 37 located between the first belt filter section 24 and the second belt filter section 26 and secondly by providing at least one impulse blower 38 which is placed adjacent the drop-off point 37 .
  • the impulse blower 38 imparting bursts of air onto the belt filter 22 at the drop-off point, all partially dry material on the belt filter 22 will be dislodged such that it can fall onto the second belt filter section 26 thereby being mechanically placed. The reason for placing partially dry fine material mechanically unto the second belt filter section 26 will be discussed below.
  • the belt filter apparatus 10 further includes an agitator formation, indicated with the reference numeral 40 , for redistributing the fine material which is transported by the belt filter 22 in the second belt filter section 26 . By redistributing the partially dry material the permeability thereof is enhanced.
  • the agitator formation 40 is provided in the form of a cam which can rotate to impart blows on the belt filter 22 , thereby enhancing the permeability of the partially dry fine material on the second belt filter section 26 .
  • the functionality of the cam 40 will become apparent from the description that follows below.
  • coal slurry which is a mixture of fine coal material and water
  • a conduit 42 from a dense medium separator, not shown in the drawings, and be placed hydraulically on the belt filter 22 at one end of the first belt filter section 24 .
  • a cyclone Simultaneous to, or just prior to the slurry being placed on the belt filter 22 , a cyclone, not shown in the drawings, will create a vacuum in the ducting 34 and consequently in the liquid collectors 28 . 1 , 28 . 2 ., . . . , 28 .n located underneath the belt filter 22 in the first and second belt filter sections 24 and 26 .
  • the fine coal material will become liberated from the water and the water will be drawn through the belt filter 22 under the influence of the vacuum to collect in the liquid collectors 28 . 1 , 28 . 2 , . . . , 28 .n. From the liquid collectors 28 . 1 , 28 . 2 , . . . 28 .n the collected water will be drawn via the ducting 34 to a liquid storage container, not shown in the drawings, for future re-use.
  • the slurry will have undergone a first drying cycle and partially dry fine coal material will have been formed.
  • the fine coal material will be aligned in such a manner that the optimum amount of fine coal material can be transported in a specific volume.
  • the result of this is a high bulk density with a very low degree of permeability such that once the slurry has undergone the first drying cycle, water may still be trapped between the particles of the fine coal material. It would, therefore, be appreciated that if the permeability of the fine coal material could be increased, trapped water could be released and removed from the fine coal material.
  • the fine coal material will have undergone a second drying cycle and will be dried to the satisfaction of an end user and ready for consumption by end-users.
  • the dry fine material is tipped unto a conveyor belt 44 to be transported to a storing facility.
  • FIG. 4 shows a second embodiment of a belt filter apparatus in accordance with the present invention, generally indicated with the reference numeral 110 .
  • the belt filter apparatus 110 operates on the same principles as the belt filter apparatus 10 and no further description is consequently necessary.
  • the belt filter apparatus 110 does, however, differ from the belt filter apparatus 10 in that both the first and second belt filter sections 112 and 114 are provided with an agitator formation 116 .
  • the agitator formation 116 in this embodiment of the invention comprises a plurality of blowers 118 . 1 , 118 . 2 , . . . , 118 .n which serve to redistribute partially dry fine material on the first and the second belt filter sections 112 and 114 , such that the amount of trapped water being released from between the particles constituting the partially dry fine material can be increased, consequently enhancing the effectiveness of the belt filter apparatus 110 .
  • the agitator formation 116 serves to create mechanical lift of the solids constituting the fine material, so that the trapped liquid may fall past the solids and drain from the coal slurry. This mechanical lift is created in that the agitator formation 116 causes the fine material solids to bounce on the belt filter sections 112 and 114 .
  • the belt filter apparatus 110 further differs from the belt filter apparatus 10 in that it includes means for mechanically placing the partially dry fine material which is provided in the form of a rotatable cam 115 which is placed proximate a drop-off point 117 located between the first belt filter section and the second belt filter section.
  • the purpose of the cam 115 is to impact on the belt filter, thereby forcing the fine material on the belt filter to fall onto the second belt filter section.
  • the belt filter apparatus 110 differs from the belt filter apparatus 10 in that it includes removal means, here a further cam 120 , which is located towards the end of the second belt filter section 114 . In use the cam 120 will impact on the belt filter to ensure that all fine material is displaced therefrom.
  • the agitator formation could comprise a combination of cams and blowers.
  • the second belt filter section 114 need not necessarily be exposed include members of the agitator formation 116 and that only the first belt filter section 112 will be exposed to the effects of the agitator formation 116 .
  • the belt filter apparatus need not comprise a first and second belt filter section but could merely comprise a single belt filter section with a single belt filter having an agitator formation for redistributing fine material transported thereon.
  • the belt filter need not necessarily be provided in the form of a non-woven fabric but could also be a micro-pore fabric.
  • the belt filter apparatus of the invention need not only be employed for drying coal slurry but could be also find application in drying any slurry or liquid containing a combination of fines and liquids, whether organic or inorganic.
  • the belt filter apparatus of the invention can be modular in nature to allow it to have more than just two belt filter sections, consequently allowing for a number of mechanical placements through the use of the means for mechanically placing.
  • the means for mechanical placing can simply be provided in the form of a drop-off point such that partially dry fine material is mechanically placed and thus redistributed as it falls under the influence of gravity form the first belt filter section onto the second belt filter section.
  • Advantages of the belt filter apparatus and the method of the invention includes low implementation, operating and maintenance costs as well as immediate water recovery and recycling. Making use of a belt filter as described above further reduces down-time and consequently increases efficiency.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Drying Of Solid Materials (AREA)
  • Filtering Materials (AREA)
  • Filtration Of Liquid (AREA)
  • Treatment Of Fiber Materials (AREA)
US12/299,386 2006-05-04 2007-05-04 Belt Filter Apparatus Abandoned US20090200248A1 (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
ZA200603554 2006-05-04
ZA2006/03554 2006-05-04
ZA200607876 2006-09-20
ZA2006/07876 2006-09-20
PCT/IB2007/051680 WO2007129273A2 (en) 2006-05-04 2007-05-04 Belt filter apparatus

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
PCT/IB2007/051680 A-371-Of-International WO2007129273A2 (en) 2006-05-04 2007-05-04 Belt filter apparatus

Related Child Applications (1)

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US12/841,620 Division US8153003B2 (en) 2006-05-04 2010-07-22 Belt filter apparatus

Publications (1)

Publication Number Publication Date
US20090200248A1 true US20090200248A1 (en) 2009-08-13

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Application Number Title Priority Date Filing Date
US12/299,386 Abandoned US20090200248A1 (en) 2006-05-04 2007-05-04 Belt Filter Apparatus
US12/841,620 Expired - Fee Related US8153003B2 (en) 2006-05-04 2010-07-22 Belt filter apparatus

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US12/841,620 Expired - Fee Related US8153003B2 (en) 2006-05-04 2010-07-22 Belt filter apparatus

Country Status (7)

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US (2) US20090200248A1 (ru)
EP (2) EP2253365B1 (ru)
AP (2) AP2008004693A0 (ru)
AU (2) AU2007246734A1 (ru)
CA (1) CA2651980C (ru)
EA (2) EA014392B1 (ru)
WO (1) WO2007129273A2 (ru)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20120103893A1 (en) * 2009-03-09 2012-05-03 Univenture, Inc. Method and apparatus for separating particles from a liquid
WO2013181204A1 (en) * 2012-05-30 2013-12-05 Flsmidth A/S Adjustable vacuum pan baffle for horizontal belt filter
WO2014008511A1 (en) * 2012-07-06 2014-01-09 Strain Cornelius Compartmentally expandable rotating belt filter for energy use reduction
WO2015179576A1 (en) * 2014-05-21 2015-11-26 Blue Water Technologies, Inc. Support structure for fluid treatment systems having belted filtration systems
WO2019046462A1 (en) * 2017-08-30 2019-03-07 Nanotech Energy, Inc. METHODS, DEVICES AND SYSTEMS FOR THE TREATMENT AND FILTRATION OF CARBON COMPOSITIONS
US11192082B2 (en) 2016-02-26 2021-12-07 Nanotech Energy, Inc. Methods, devices and systems for processing of carbonaceous compositions

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11724217B2 (en) * 2017-01-23 2023-08-15 Schlumberger Technology Corporation Fluid and solid material separator
CN111974038B (zh) * 2020-08-13 2022-08-30 冯平仓 一种隔膜式压滤机隔膜板

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US3531404A (en) * 1968-04-01 1970-09-29 Union Tank Car Co Sewage treatment system
US3669272A (en) * 1970-04-30 1972-06-13 Friedrich Bilabel Band filter with vacuum suction chamber
US3836681A (en) * 1972-03-01 1974-09-17 J Dodd Device and method of recovering sticky particulate materials such as algae
US4105558A (en) * 1975-04-08 1978-08-08 Heinrich Hans J Apparatus for draining of muddy liquids
US4986910A (en) * 1984-06-11 1991-01-22 Nippon Kokan Kabushiki Kaisha Apparatus for dehydrating sludge
US5133883A (en) * 1990-05-21 1992-07-28 Elektronweg 24 Method for removing liquid from a mixture of liquid and solid matter
US5730767A (en) * 1996-07-30 1998-03-24 Pneumafil Corporation Sealing apparatus in a belt-type filter

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US2101109A (en) * 1935-01-23 1937-12-07 William R Thomson Method of and apparatus for the extraction of liquid from materials
US3358834A (en) * 1965-02-17 1967-12-19 Belson Corp Method and apparatus for filtering liquids
SU902788A1 (ru) * 1980-06-25 1982-02-07 Всероссийский Ордена Трудового Красного Знамени Научно-Исследовательский И Проектно-Технологический Институт Механизации И Электрификации Сельского Хозяйства Ленточный вакуум-фильтр
SE457057B (sv) * 1985-10-21 1988-11-28 Bat O Fangst Ab Filteranordning med blaasorgan
DE4302922C1 (de) * 1993-02-03 1994-08-11 Klein Alb Gmbh Co Kg Verfahren und Vorrichtung zum Behandeln von Schlämmen
DK1471988T3 (da) * 2001-12-28 2007-06-18 Univ Danmarks Tekniske Filtreringsfremgangsmåde og apparat

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3531404A (en) * 1968-04-01 1970-09-29 Union Tank Car Co Sewage treatment system
US3669272A (en) * 1970-04-30 1972-06-13 Friedrich Bilabel Band filter with vacuum suction chamber
US3836681A (en) * 1972-03-01 1974-09-17 J Dodd Device and method of recovering sticky particulate materials such as algae
US4105558A (en) * 1975-04-08 1978-08-08 Heinrich Hans J Apparatus for draining of muddy liquids
US4986910A (en) * 1984-06-11 1991-01-22 Nippon Kokan Kabushiki Kaisha Apparatus for dehydrating sludge
US5133883A (en) * 1990-05-21 1992-07-28 Elektronweg 24 Method for removing liquid from a mixture of liquid and solid matter
US5730767A (en) * 1996-07-30 1998-03-24 Pneumafil Corporation Sealing apparatus in a belt-type filter

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8286801B2 (en) * 2009-03-09 2012-10-16 Univenture, Inc. Method and apparatus for separating particles from a liquid
US20120103893A1 (en) * 2009-03-09 2012-05-03 Univenture, Inc. Method and apparatus for separating particles from a liquid
WO2013181204A1 (en) * 2012-05-30 2013-12-05 Flsmidth A/S Adjustable vacuum pan baffle for horizontal belt filter
US10029195B2 (en) * 2012-07-06 2018-07-24 Nexom (Us), Inc. Compartmentally expandable rotating belt filter for energy use reduction
WO2014008511A1 (en) * 2012-07-06 2014-01-09 Strain Cornelius Compartmentally expandable rotating belt filter for energy use reduction
US20150157965A1 (en) * 2012-07-06 2015-06-11 Blue Water Technologies, Inc. Compartmentally expandable rotating belt filter for energy use reduction
CN104968407A (zh) * 2012-07-06 2015-10-07 蓝水科技有限公司 用于能源使用减少的可隔腔室地扩张的转动带过滤器
EP2869904A4 (en) * 2012-07-06 2016-05-18 Blue Water Technologies Inc COMPARTMENTALLY EXPANDABLE ROTARY BAND FILTER FOR REDUCING ENERGY CONSUMPTION
WO2015179576A1 (en) * 2014-05-21 2015-11-26 Blue Water Technologies, Inc. Support structure for fluid treatment systems having belted filtration systems
US10786766B2 (en) 2014-05-21 2020-09-29 Nexom (Us), Inc. Support structure for fluid treatment systems having belted filtration systems
US11192082B2 (en) 2016-02-26 2021-12-07 Nanotech Energy, Inc. Methods, devices and systems for processing of carbonaceous compositions
US11752479B2 (en) 2016-02-26 2023-09-12 Nanotech Energy, Inc. Methods, devices and systems for processing of carbonaceous compositions
WO2019046462A1 (en) * 2017-08-30 2019-03-07 Nanotech Energy, Inc. METHODS, DEVICES AND SYSTEMS FOR THE TREATMENT AND FILTRATION OF CARBON COMPOSITIONS

Also Published As

Publication number Publication date
EP2021095A2 (en) 2009-02-11
US20110042292A1 (en) 2011-02-24
CA2651980A1 (en) 2007-11-15
EA200802276A1 (ru) 2009-06-30
EP2253365B1 (en) 2014-01-08
AU2010206076B2 (en) 2012-05-10
AU2010206076A1 (en) 2010-08-19
CA2651980C (en) 2015-07-07
EA201001150A1 (ru) 2011-02-28
EP2253365A1 (en) 2010-11-24
WO2007129273B1 (en) 2008-05-29
AP2008004693A0 (en) 2008-12-31
WO2007129273A2 (en) 2007-11-15
US8153003B2 (en) 2012-04-10
AP2010005330A0 (en) 2010-08-31
AP3056A (en) 2014-12-31
WO2007129273A3 (en) 2008-03-27
AU2007246734A1 (en) 2007-11-15
EA017033B1 (ru) 2012-09-28
EA014392B1 (ru) 2010-10-29

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