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WO1999047467A2 - Method for producing sand-lime bricks from lime residues-containing cyanide - Google Patents

Method for producing sand-lime bricks from lime residues-containing cyanide Download PDF

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Publication number
WO1999047467A2
WO1999047467A2 PCT/DE1999/000643 DE9900643W WO9947467A2 WO 1999047467 A2 WO1999047467 A2 WO 1999047467A2 DE 9900643 W DE9900643 W DE 9900643W WO 9947467 A2 WO9947467 A2 WO 9947467A2
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WO
WIPO (PCT)
Prior art keywords
lime
sand
residues
cyan
bricks
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.)
Ceased
Application number
PCT/DE1999/000643
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German (de)
French (fr)
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WO1999047467A3 (en
Inventor
Holger Fischer
Reinhard Fischer
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Individual
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Application filed by Individual filed Critical Individual
Priority to AU38094/99A priority Critical patent/AU3809499A/en
Publication of WO1999047467A2 publication Critical patent/WO1999047467A2/en
Publication of WO1999047467A3 publication Critical patent/WO1999047467A3/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B28/00Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
    • C04B28/18Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing mixtures of the silica-lime type
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B18/00Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
    • C04B18/04Waste materials; Refuse
    • C04B18/0481Other specific industrial waste materials not provided for elsewhere in C04B18/00
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/00474Uses not provided for elsewhere in C04B2111/00
    • C04B2111/00767Uses not provided for elsewhere in C04B2111/00 for waste stabilisation purposes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/60Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

Definitions

  • Lime residues containing cyan are treated with silica sand or silica sand residues in an autoclave at at least 110 ° C and 2 bar pressure with water vapor, whereby CaCN 2 is broken down into CaCO 3 and ammonia.
  • the process of stone production corresponds to the known manufacturing process of sand-lime bricks.
  • the stones are then treated with steam in an autoclave at 180 ° C and 10 bar pressure for 8 hours.
  • Calcium hydrosilicates are formed and the cyan compounds are decomposed in 1.25 kg CaCO 3 and 425 g ammonia.
  • the ammonia-containing water vapor is removed from the autoclave and 425 g of ammonia are converted to 1.650 kg of ammonium sulfate with 1.225 kg of sulfuric acid.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Civil Engineering (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

Lime residues containing cyanogen are treated with silica sand or silica sand residues in autoclaves at a temperature of at least 110 °C and at a pressure of 2 bars, whereby CaCN2 is broken down into CaCO3 and ammonia.

Description

PatentanmeldungPatent application

Verfahren zur Herstellung von Kalksandsteinen aus cyanidhaltigen KalkrückständenProcess for the production of sand-lime bricks from limestone residues containing cyanide

ZusammenfassungSummary

Cyanhaltige Kalkrückstände werden mit Silikasand oder Silikasand-Rückständen im Autoklaven bei mindestens 110°C und 2 bar Druck mit Wasserdampf behandelt, wodurch CaCN2 in CaCO3 und Ammoniak zerlegt wird.Lime residues containing cyan are treated with silica sand or silica sand residues in an autoclave at at least 110 ° C and 2 bar pressure with water vapor, whereby CaCN 2 is broken down into CaCO 3 and ammonia.

Stand der TechnikState of the art

Die Herstellung von Kalksandsteinen aus kieselsäurereichem Sand und Kalk ( CaO oder Ca(OH)2 ) ist seit Jahrzehnten ein sehr gut bekannter technischer Prozeß.The production of sand-lime bricks from silica-rich sand and lime (CaO or Ca (OH) 2 ) has been a very well-known technical process for decades.

Ost-Rassow, Lehrbuch der chemischen Technologie, S. 401 - 402Ost-Rassow, Textbook of Chemical Technology, pp. 401 - 402

Auch die Verwendung von silikatischen Abgängen der Mineralaufbereitung ist gängige Praxis.The use of silicate minerals from mineral processing is also common practice.

Pigott, P. G., Valdez, E. G., Dean, K. C, Dry pressed building bricks from copper mill tailings, US Bureau of Mines Report of Investigations No. 7537, 1971Pigott, P.G., Valdez, E.G., Dean, K.C, Dry pressed building bricks from copper mill tailings, US Bureau of Mines Report of Investigations No. 7537, 1971

Cyanhaltige Rückstände aus der Chemischen Industrie und aus und der Mineralgewinnung stellen ein Problem für die Umwelt dar. Sie müssen entweder in geeigeneten Deponien abgelagert oder in aufwendigen Verfahren entgiftet werden.Cyan-containing residues from the chemical industry and from and mineral extraction pose a problem for the environment. They either have to be deposited in suitable landfills or have to be detoxified using complex processes.

Edmonds, C.J., Cyanide destruction. Gold mill effluents, Proc. Annu. Meet. Can. Miner. Process., 5^ (1973), pp. 275-286. Editor: Joe, E..G. Publisher: Can. Miner. Process., Ottawa, Ont.Edmonds, C.J., Cyanide destruction. Gold mill effluents, Proc. Annu. Meet. Can. Miner. Process., 5 ^ (1973), pp. 275-286. Editor: Joe, E..G. Publisher: Can. Miner. Process., Ottawa, Ont.

Kroeger, Edwin Bane, Analysis and comparison of cyanide detoxification methods from spent heaps, Dissertation, Univ. of Alaska, Fairbanks, AK, USAKroeger, Edwin Bane, Analysis and comparison of cyanide detoxification methods from spent heaps, dissertation, Univ. of Alaska, Fairbanks, AK, USA

Es ist bekannt , Calciumcyanamid mit Wasserdampf unter Druck nach der Formel:It is known to use calcium cyanamide with steam under pressure according to the formula:

CaCN2 + 3 H2O = CaCO3 + 2 NH3 in Calciumcarbonat und Ammoniak zu zerlegen.Decompose CaCN 2 + 3 H 2 O = CaCO 3 + 2 NH 3 in calcium carbonate and ammonia.

Bisher wurden viele Verfahren beschrieben um cyanhaltige Reststoffe mit dazu speziell entwickelten Verfahren zu entgiften.So far, many processes have been described to detoxify cyanide residues using specially developed processes.

Der Gedanke, einen Produktionsprozeß mit der gleichzeitigen Entgiftung des Cyans zu verbinden ist neu.The idea of combining a production process with the simultaneous detoxification of the cyan is new.

Dabei sollen cyanhaltige Kalkrückstände zur Herstellung von Kalksandsteinen verwendet werden. Bei durchgeführten Versuchen hat sich überraschend gezeigt, daß bei gleichem Anteil von CaOH2 in der Sand-Kalk-Mischung und bei einem SiO2-Gehalt von über 95% im Sand durch die Bildung von CaCO3 bei der Zersetzung des CN2 die Festigkeit sich um 8 % erhöht.Lime residues containing cyan are to be used for the production of sand-lime bricks. Experiments carried out have shown, surprisingly, that with the same proportion of CaOH 2 in the sand-lime mixture and with an SiO 2 content of over 95% in the sand, the strength is reduced by the formation of CaCO 3 during the decomposition of the CN 2 increased by 8%.

Das erfindungsgemäße, neuartige Verfahren besteht darin, Kalkrückstände mit hohem Gehalt an CaO und/oder CaOH2, die mit Cyanverbindungen verunreinigt sind, mit Silikasand hoher Reinheit und geringer Korngröße zu vermischen und zu Steinen zu pressen. Die Presslinge werden üblicherweise in Autoklaven bei mindestens 160° C und mindestens 6 bar durch mehrere Stunden behandelt.The novel method according to the invention consists in mixing lime residues with a high content of CaO and / or CaOH 2 , which are contaminated with cyan compounds, with silica sand of high purity and small grain size and pressing them into stones. The compacts are usually treated in autoclaves at at least 160 ° C and at least 6 bar for several hours.

Dabei finden folgende Umsetzungen statt:The following implementations take place:

Si02 + Ca(OH)2 + H20 = CaHSi02 + H20 CaCN2 + 3 H2O = CaCO3 + 2 NH3 Si0 2 + Ca (OH) 2 + H 2 0 = CaHSi0 2 + H 2 0 CaCN 2 + 3 H 2 O = CaCO 3 + 2 NH 3

Nach Beendigung des Autoklavenprozesses wird das Ammoniak-Wasserdampf- Gemisch aus dem Autoklaven abgezogen und z.B. mit Schwefelsäure in Ammoniumsulfat umgewandelt und damit einer weiteren Nutzung zugeführt.After the autoclave process has ended, the ammonia / water vapor mixture is withdrawn from the autoclave and e.g. converted into ammonium sulfate with sulfuric acid and thus used for further use.

Der Prozeß der Steinherstellung entspricht im übrigen dem bekannten Herstellungsverfahren von Kalksandsteinen.The process of stone production corresponds to the known manufacturing process of sand-lime bricks.

Es lassen sich auf diese Weise Kalk-Sandsteine herstellen , die den DIN- Spezifikationen entsprechen. Durch die Bildung von CaCO3 aus CaCN2 wird eine besondere Festigkeit der Steine erreicht.In this way, lime sandstones can be produced that meet the DIN specifications. Due to the formation of CaCO 3 from CaCN 2 , the stones are particularly strong.

Eine neuartige Variante des oben beschriebenen Verfahrens besteht darin, den üblichen Silika-Sand durch Sandabgänge der Mineralaufbereitung zu ersetzen, insbesondere solche, die durch Cyan kontaminiert sind. Dabei werden die Sande ebenfalls entgiftet. Man vermindert durch die Verwendung dieser Silika-Sande die bei einer Ablagerung auch nach einer Cyanentgiftung bestehende Gefährdung des Grundwassers durch lösliche Schwermetalle.A new variant of the process described above is to replace the usual silica sand with sand exits from mineral processing, especially those that are contaminated with cyan. The sands are also detoxified. The use of these silica sands reduces the risk to the groundwater caused by soluble heavy metals even when cyan is detoxified.

Kyle, J. H., Stability of metal-cyanide and hydroxide complexes, Publ. Australas. Inst. Min. Metall. (1997), 2/97 (World Gold '97), pp. 163-169Kyle, JH, Stability of metal-cyanide and hydroxide complexes, Publ. Australas. Inst. Min. Metal. (1997), 2/97 (World Gold '97), pp. 163-169

Das folgende Beispiel dient als Erläuterung des erfindungsgemäßen Verfahrens:The following example serves to explain the method according to the invention:

1 000 kg Silikasand oder Sandrückstände, z. B. von der Erzaufbereitung, mit mindestens 95 % SiO2 und einer Korngröße unter 0,3 mm werden mit 100 kg eines Kalkrückstandes, der mindestens 95 % CaO bzw. Ca(OH)2 enthält und mit 1 %, entsprechend 1 kg, Cyaniden kontaminiert ist, zu Steinen gepreßt. Besteht der Kalkrückstand überwiegend aus CaO, muß CaO vor dem Steinpressen durch Zusatz von Wasser in Ca(OH)2 umgewandelt werden.1,000 kg of silica sand or sand residues, e.g. B. from ore processing, with at least 95% SiO 2 and a grain size less than 0.3 mm with 100 kg of a lime residue that contains at least 95% CaO or Ca (OH) 2 and with 1%, corresponding to 1 kg, cyanides is contaminated, pressed to stones. If the lime residue consists mainly of CaO, CaO must be converted to Ca (OH) 2 by adding water before stone pressing.

Anschließend werden die Steine im Autoklaven bei 180°C und 10 bar Druck 8 Stunden mit Wasserdampf behandelt. Dabei werden Kalziumhydrosilikate gebildet und die Cyanverbindungen in 1,25 kg CaCO3 und 425 g Ammoniak zersetzt. Der ammoniak- haltige Wasserdampf wird aus dem Autoklaven entfernt und 425 g Ammoniak werden mit 1,225 kg Schwefelsäure zu 1,650 kg Ammonsulfat umgesetzt. The stones are then treated with steam in an autoclave at 180 ° C and 10 bar pressure for 8 hours. Calcium hydrosilicates are formed and the cyan compounds are decomposed in 1.25 kg CaCO 3 and 425 g ammonia. The ammonia-containing water vapor is removed from the autoclave and 425 g of ammonia are converted to 1.650 kg of ammonium sulfate with 1.225 kg of sulfuric acid.

Claims

Patentansprüche claims 1. Verfahren zur Herstellung von Kalksandsteinen, dadurch gekennzeichnet, daß cyanhaltige Kalkrückstände allein oder zusammen mit CaO und/oder Ca(OH)2 als Bindemittel für Quarz bei der üblichen Kalksandstein-Herstellung verwendet werden.1. A process for the production of sand-lime bricks, characterized in that cyan-containing lime residues are used alone or together with CaO and / or Ca (OH) 2 as binders for quartz in the conventional sand-lime brick production. 2. Verfahren zur Herstellung von Kalksandsteinen, dadurch gekennzeichnet, daß an Stelle von oder zusammen mit Quarzsand silikatische Abgänge der Mineral- Erz-aufbereitung verwendet werden.2. A process for the production of sand-lime bricks, characterized in that silicatic exits of the mineral ore processing are used instead of or together with quartz sand. 3. Verfahren zur Herstellung von Kalksandsteinen, dadurch gekennzeichnet, daß die beim Härten der Steine im Autoklaven entstehenden Dämpfe aus Wasserdampf und Ammoniak aus dem Autoklaven abgezogen werden und das Ammoniak chemisch gebunden wird.3. A process for the production of sand-lime bricks, characterized in that the vapors formed during the hardening of the stones in the autoclave are drawn off from the steam and ammonia from the autoclave and the ammonia is chemically bound. 4. Verfahren nach Anspruch 1 , dadurch gekennzeichnet, daß die cyanhaltigen Rückstände vor ihrer Verwendung von etwaigen Alkalien befreit werden.4. The method according to claim 1, characterized in that the cyan-containing residues are freed of any alkalis before they are used. 5. Verfahren nach Anspruch 2, dadurch gekennzeichnet, daß die silikatischen Aufbereitungsabgänge vor Ihrer Verwendung einem Prozeß zur Anreicherung der Kieselsäure unterworfen werden.5. The method according to claim 2, characterized in that the silicate treatment exits are subjected to a process for the enrichment of the silica before they are used. 6. Verfahren nach Anspruch 1 und 2, dadurch gekennzeichnet, daß die cyanhaltigen Kalkrückstände und die silikatischen Aufbereitungsabgänge vor der Steinherstellung in einem Autoklaven mit Wasserdampf bei einer Temperatur über 110 °C und Drücken über 2 bar durch Umwandlung des Cyans in Ammoniak entgiftet werden. 6. The method according to claim 1 and 2, characterized in that the cyan-containing lime residues and the silicate treatment exits are detoxified in an autoclave with steam at a temperature above 110 ° C and pressures above 2 bar by converting the cyan into ammonia.
PCT/DE1999/000643 1998-03-15 1999-03-12 Method for producing sand-lime bricks from lime residues-containing cyanide Ceased WO1999047467A2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU38094/99A AU3809499A (en) 1998-03-15 1999-03-12 Method for producing sand-lime bricks from lime residues-containing cyanide

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE1998111119 DE19811119A1 (en) 1998-03-15 1998-03-15 Lime-sandstone of increased strength is produced
DE19811119.3 1998-03-15

Publications (2)

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WO1999047467A2 true WO1999047467A2 (en) 1999-09-23
WO1999047467A3 WO1999047467A3 (en) 1999-12-09

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AU (1) AU3809499A (en)
DE (1) DE19811119A1 (en)
WO (1) WO1999047467A2 (en)
ZA (1) ZA992054B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103241994A (en) * 2012-02-02 2013-08-14 王熙成 Silty sandstone

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ZA711879B (en) * 1971-03-23 1972-05-31 L Grek Building element
JPS4883115A (en) * 1972-02-09 1973-11-06
JPS571482A (en) * 1980-06-05 1982-01-06 Ebara Infilco Co Ltd Caking method for cyanide-contng. solid waste
JPS571481A (en) * 1980-06-06 1982-01-06 Ebara Infilco Co Ltd Disposal of cyanide-contng. solid waste
SU1328332A1 (en) * 1985-03-20 1987-08-07 Московский химико-технологический институт им.Д.И.Менделеева Raw mixture for producing silicate brick
SU1305624A1 (en) * 1985-09-18 1987-04-23 Харьковский политехнический институт Raw mixture for manufacturing lime-and-sand articles
EP0380713B1 (en) * 1989-01-28 1993-03-17 RHEINISCHE BAUSTOFFWERKE GMBH & CO. KG Compaction of industrial dusts and disposal of the compacted material
US5286427A (en) * 1993-01-06 1994-02-15 George Koumal Method of environmental cleanup and producing building material using copper mine tailings waste material
CN1105653A (en) * 1994-01-18 1995-07-26 西安市环境保护局 Utilization and treatment method for industrial waste water

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103241994A (en) * 2012-02-02 2013-08-14 王熙成 Silty sandstone

Also Published As

Publication number Publication date
ZA992054B (en) 2000-03-20
AU3809499A (en) 1999-10-11
WO1999047467A3 (en) 1999-12-09
DE19811119A1 (en) 1999-09-16

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