CA2063041A1 - Process for the production of gas-permeable nets of noble metals for catalytic processes - Google Patents

Process for the production of gas-permeable nets of noble metals for catalytic processes

Info

Publication number
CA2063041A1
CA2063041A1 CA002063041A CA2063041A CA2063041A1 CA 2063041 A1 CA2063041 A1 CA 2063041A1 CA 002063041 A CA002063041 A CA 002063041A CA 2063041 A CA2063041 A CA 2063041A CA 2063041 A1 CA2063041 A1 CA 2063041A1
Authority
CA
Canada
Prior art keywords
palladium
rhodium
nickel
nets
platinum
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
CA002063041A
Other languages
French (fr)
Inventor
Siegfried Blass
Horst Duebler
Thomas Stoll
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.)
Evonik Operations GmbH
Original Assignee
Individual
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=25901946&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=CA2063041(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Individual filed Critical Individual
Publication of CA2063041A1 publication Critical patent/CA2063041A1/en
Abandoned legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0009Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/50Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • B01J35/58Fabrics or filaments
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/46Ruthenium, rhodium, osmium or iridium
    • B01J23/464Rhodium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74Iron group metals
    • B01J23/755Nickel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/892Nickel and noble metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/89Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with noble metals
    • B01J23/8926Copper and noble metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/50Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
    • B01J35/56Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B21/00Nitrogen; Compounds thereof
    • C01B21/20Nitrogen oxides; Oxyacids of nitrogen; Salts thereof
    • C01B21/24Nitric oxide (NO)
    • C01B21/26Preparation by catalytic or non-catalytic oxidation of ammonia
    • C01B21/265Preparation by catalytic or non-catalytic oxidation of ammonia characterised by the catalyst
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B21/00Nitrogen; Compounds thereof
    • C01B21/20Nitrogen oxides; Oxyacids of nitrogen; Salts thereof
    • C01B21/24Nitric oxide (NO)
    • C01B21/26Preparation by catalytic or non-catalytic oxidation of ammonia
    • C01B21/267Means for preventing deterioration or loss of catalyst or for recovering lost catalyst
    • DTEXTILES; PAPER
    • D04BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
    • D04BKNITTING
    • D04B1/00Weft knitting processes for the production of fabrics or articles not dependent on the use of particular machines; Fabrics or articles defined by such processes
    • D04B1/14Other fabrics or articles characterised primarily by the use of particular thread materials
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2101/00Inorganic fibres
    • D10B2101/20Metallic fibres
    • DTEXTILES; PAPER
    • D10INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10BINDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
    • D10B2403/00Details of fabric structure established in the fabric forming process
    • D10B2403/02Cross-sectional features
    • D10B2403/024Fabric incorporating additional compounds
    • D10B2403/0242Fabric incorporating additional compounds enhancing chemical properties

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Textile Engineering (AREA)
  • Catalysts (AREA)
  • Knitting Of Fabric (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Wire Processing (AREA)

Abstract

ABSTRACT OF THE DISCLOSURE

Wires of platinum containing 4 to 12% rhodium or 4 to 12% palladium and rhodium and wires of palladium containing 2 to 15% nickel or 2 to 15% copper or 2 to 15% nickel and copper which must have a diameter of 50 to 120 µm, a tensile strength of 900 to 1050 N/mm2 and an elastic limit of 0.5 to 3% are used for the knitting of round nets for use as catalysts in the oxidation of ammonia and as recovery nets for platinum metals. A flat knitting machine with 7 to 14 needles per inch and a sinking depth (loop length) of 2 to 6 mm is also used.

Description

2 ~? $ ,~ ~? ~ 1 This invention relates to a process for the production of gas-permeable nets of noble metals for catalytic processes, more particularly for the catalytic oxidation of ammonia with air or for recovery of the platinum metals which volatilize in the catalytic oxidation of ammonia by knitting of wires of platinum or palladium alloys on knitting machines.

The use of noble metal catalysts in the form of gas-permeable nets is an established method of operating certaincatalytic processes with optimal yields. A well-known example is the use of platinum/rhodium catalyst nets in the oxidation of ammonia for the production of nitric acid.

The net form of the catalysts affords several advantages over other catalyst configurations. For example, the net form provides for large surface development coupled with high mechanical strength. In wire drawing and wire weaving, manufacturers have established production methods for processing the catalytically active metals and metal alloys.
These catalyst nets are made in web form on looms and are cut to size in circular form in accordance with the dimensions of the oxidation plants. This results in the accumulation of considerable noble metal waste which has to be reprocessed.
- .:
However, nets have the advantage that, with their loops, they form a homogeneous structure of metal wires and free ',- throughflow openings for the reaction gases.
:
There are no inhomogeneities, for example in the form of seams or welds which impede uniform gas flow.

Nets made in the same way are also used in the recovery of no~le metals, for example in the oxidation of ammonia. A

2~3~ i1 large part of the noble metals which volatilize from the platinum/rhodium catalyst nets during the process is - collected in nets of palladium alloys.

Woven nets have a number of disadvantages attributable to their production process, including the time required to set up the loom, weaving in considerable lengths and cutting out of the circular nets from rectangular webs with approx.
35% waste.

High production costs are incurred by long set-up times and the high percentage of waste and by the large amounts of expensive noble metals tied up on the loom which necessitates considerable capital outlay.

~he woven nets can also be replaced by other gas-permeable configurations. For example, perforated metal foils and metal fibre nonwovens (DE-PS 15 94 716), metal felts (DE-PS 28 29 035) or folded tubular wire nets (DE-OS 22 48 811) are known.
.~
However, these configurations have never been successfully used in practice, above all because they adversely affect the flow conditions prevailing in the reaction zone.
':
Knitted nets have recently been mentioned in connection with the recovery of noble metals in the oxidation of ammonia (EP-PS 0 077 121). However, no particulars of their form or production are provided.

`~ EP-OS 0 364 153 describes a process for the production ; of nets of noble metal alloys, more particularly for the catalytic oxidation of ammonia and the recovery of noble 2~3~ ~ ~

metals, in which wires of noble metal alloys are knitted together with an auxiliary thread of natural fibres or a synthetic material on a knitting machine. For weights per unit area of more than 200 g/m2, pure noble metal alloy wires cannot be knitted without auxiliary threads because the wires break and tear during the knitting process, the tensile strength, wire diameter, ductility and surface friction factor of the material ~eing said to play a part. The disadvantage of including an auxiliary thread in the knitting process is that it has to be removed before the nets are used, which can be done by burning or dissolving. Both methods are complicated and can lead to contamination of the metal alloys which can adversely affect their catalytic activity or recovery level.

Accordingly, the present invention provides a process for the production of gas-permeable nets of noble metals for catalytic processes, more particularly for the catalytic oxidation of ammonia or for recovery of the platinum metals which volatilize in the catalytic oxidation of ammonia by knitting of wires of platinum or palladium alloys on knitting ; machines, in which no auxiliary thread would have to be knitted and the weights per unit area of more than 300 g/m2 required for the particular process could still be achieved.

More particularly, the invention provides a process for the production of gas-permeable noble metal for a catalytic process, comprising: knitting a wire on a knitting machine, wherein: (a) said wire is a platinum-rhodium alloy containing 4 to 12 weight percent rhodium, a platinum-palladium-rhodium alloy containing 4 to 12 weight percent palladium and rhodium, a palladium-nickel alloy containing 2 to 15 weight percent nickel, a palladium-copper alloy containing 2 to 15 weight percent copper, or a palladium-2 ~

nickel-copper alloy containing 2 to 15 weight percent nickel and coppper; (b) said wire has a diameter of from 50 to 120 ~m, a tensile strength, Rm, of from 900 to 1,050 N/mm2, and an elastic limit, A, of from 0.5 to 3.0 percent; and (c) said knitting machine is a flat knitting machine with a gauge, number of needles per inch, of from 7 to 14, and a sinking depth, loop length, of from 2 to 6 mm.

In many cases, it is of advantage to knit two and more wires toqether.

Providing these wire and knitting machine parameters are observed, nets having satisfactorily formed loops can be knitted - surprisingly without auxiliary threads - from platinum/rhodium wires, for example containing 10~ by weight rhodium, or from palladium/nickel wires, for example containing S% by weight nickel, and do not produce any inhomogeneities when used in gas streams.
,.
Wire breaks are not discernible or do not occur during the knitting process. Weights per unit area of more than 300 - 20 g/m2 can readily be achieved.

The use of flat knitting machines affords the further advantage that the knitted nets can be directly made in their final dimensions, i.e. in the exact diameter required for the plant, so that there is no accumulation of waste for subsequent reprocessing as in the usual circular cutting of woven nets.
:.
The following ~xamples are intended to illustrate the invention:

~ n ~

Example 1 A flat knittinq machine with 12 needles per inch was used for the production of a 2300 mm diameter round catalyst net for the oxidation of ammonia. The net was knitted from a 76 ~m diameter wire of 90 platinum/10 rhodium rhodium, the wire being used in doubled form. It had a tensile strength of 930 N/mm2 and an elastic limit of 1%. The sinking depth durinq knitting was 2.8 mm. A net having a weight per unit area of approximately 600 g/m2 was obtained. The net-produced excellent results when used in ammonia oxidation - plants.

- Example 2 A two-bed flat knitting machine with 10 needles per inch lS was used for the production of circular recovery nets for the oxidation of ammonia. The wire (composition: 95 palladium/5 nickel) had a diameter of 90 ~m, a tensile strength of 920 N/mm and an elastic limit of 1%. The sinking depth during knitting was 3.9 mm. A 3700 mm diameter net with a weight per unit area of 500 g/m2 was obtained when the wire was used in doubled form. The recovery level of platinum metals in ammonia oxidation plants was at least as high as that achieved with corresponding woven nets.

Claims (6)

1. A process for the production of a gas-permeable noble metal net for a catalytic process, comprising:
knitting a wire on a knitting machine, wherein:

(a) said wire is a platinum-rhodium alloy containing 4 to 12 weight percent rhodium, a platinum-palladium-rhodium alloy containing 4 to 12 weight percent palladium and rhodium, a palladium-nickel alloy containing 2 to 15 weight percent nickel, a palladium-copper alloy containing 2 to 15 weight percent copper, or a palladium-nickel-copper alloy containing 2 to 15 weight percent nickel and copper;

(b) said wire has a diameter of from 50 to 120 µm, a tensile strength, Rm, of from 900 to 1,050 N/mm2, and an elastic limit, A, of from 0.5 to 3.0 percent; and (c) said knitting machine is a flat knitting machine with a gauge, number of needles per inch, of from 7 to 14, and a sinking depth, loop length, of from 2 to 6 mm.
2. The process of claim 1, wherein said net is adapted for the catalytic oxidation of ammonia, or the recovery of platinum metals which volatilize during the catalytic oxidation of ammonia.
3. The process of claim 2, wherein said net has a weight of at least 300 g/m2.
4. The process of claim 3, wherein at least two wires are knitted together.
5. The process of claim 4, wherein the net has a circular shape.
6. A gas-permeable noble metal net produced by the process of any one of claims 1 to 5.
CA002063041A 1991-03-16 1992-03-13 Process for the production of gas-permeable nets of noble metals for catalytic processes Abandoned CA2063041A1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
DE4108625 1991-03-16
DEP4108625.2 1991-03-16
DE4206199A DE4206199C1 (en) 1991-03-16 1992-02-28
DEP4206199.7 1992-02-28

Publications (1)

Publication Number Publication Date
CA2063041A1 true CA2063041A1 (en) 1992-09-17

Family

ID=25901946

Family Applications (1)

Application Number Title Priority Date Filing Date
CA002063041A Abandoned CA2063041A1 (en) 1991-03-16 1992-03-13 Process for the production of gas-permeable nets of noble metals for catalytic processes

Country Status (22)

Country Link
EP (1) EP0504723B1 (en)
JP (1) JPH0564746A (en)
KR (1) KR920017714A (en)
CN (1) CN1035042C (en)
AT (1) ATE93410T1 (en)
AU (1) AU644725B2 (en)
BG (1) BG60171B1 (en)
BR (1) BR9200886A (en)
CA (1) CA2063041A1 (en)
CS (1) CS75792A3 (en)
DE (2) DE4206199C1 (en)
DK (1) DK0504723T3 (en)
ES (1) ES2046903T3 (en)
FI (1) FI921093A (en)
HU (1) HU211812B (en)
IL (1) IL101187A0 (en)
MX (1) MX9201108A (en)
NO (1) NO300671B1 (en)
PL (1) PL166988B1 (en)
RU (1) RU2017520C1 (en)
TR (1) TR26402A (en)
YU (1) YU24892A (en)

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GB2274071A (en) * 1993-01-06 1994-07-13 Pgp Ind Inc Catalyst pack
DE4300791A1 (en) * 1993-01-14 1994-07-21 Heraeus Gmbh W C Knitted wire made of precious metal and process for its manufacture
DE4411774C1 (en) * 1994-04-06 1995-08-17 Degussa Metal gauze catalyst for gas reaction, esp. ammonia oxidn. to nitric acid
US6073467A (en) * 1994-04-06 2000-06-13 Degussa Aktiengesellschaft Catalyst gauzes for gaseous reactions
JP2002100180A (en) 2000-09-22 2002-04-05 Toshiba Corp Magnetic disk unit
RU2298433C2 (en) * 2001-02-08 2007-05-10 Умикор АГ энд Ко. КГ. Three-dimensional catalytic nets braided in two or more layers
CN100457935C (en) * 2005-11-09 2009-02-04 贵研铂业股份有限公司 Palladium-base alloy for recovering platinum catalyst and recovering net
CN100362134C (en) * 2005-11-17 2008-01-16 常州市裕和金属材料有限公司 New process for separating metal fiber copper protective layer by catalytic ammonia leaching method
DE102011016044A1 (en) 2011-04-04 2012-10-04 Jens Kopatsch Preparing woven, knitted and/or crocheted metal-, precious metal- or alloy grids, comprises deforming or molding wire with non-circular peripheral shape via pulling, rolling, pressing or shape-changing radiation to produce shaped wire
CN103623815A (en) * 2013-07-24 2014-03-12 上海派特贵金属有限公司 Novel platinum-rhodium alloy knitted catalytic set gauze and preparation method thereof
EP3056267A1 (en) 2015-02-12 2016-08-17 Umicore AG & Co. KG Catalyst gauze and installation for the catalytic oxidation of ammunia
EP3779005A1 (en) 2019-08-16 2021-02-17 Umicore Ag & Co. Kg Knitting of precious metal nets with common material at the periphery, net from precious metal obtained thereby and a process using the precious metal net
EP3795728A1 (en) 2019-09-17 2021-03-24 Umicore Ag & Co. Kg Knitting of precious metal networks and a method using same
EP3812154B1 (en) * 2019-10-21 2023-05-17 Heraeus Deutschland GmbH & Co. KG Method for making a catalyst system for gas reactions
EP3900826A1 (en) 2020-04-22 2021-10-27 UMICORE AG & Co. KG Pure metal network for catalysing gas phase reactions
DE102020120927B4 (en) 2020-08-07 2024-01-25 Jens Kopatsch Process for producing networks with a tertiary structure for the catalytic conversion of fluids
EP4247554B1 (en) 2020-11-17 2024-06-12 Umicore AG & Co. KG Pure metal network for catalysing gas phase reactions
EP4001483A1 (en) 2020-11-17 2022-05-25 UMICORE AG & Co. KG Precious metal net for catalysing gas phase reactions, method of making same and its use in an ammonia oxiditation process
EP4310209A1 (en) * 2022-07-19 2024-01-24 Yara International ASA Method for recovering volatile pt or pd and system thereof
DE202024101437U1 (en) 2024-03-22 2024-03-28 Umicore Ag & Co. Kg Knitted net packing for ammonia decomposition

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FR771524A (en) * 1933-07-06 1934-10-10 Comptoir General Des Metaux Pr Improvement in platinum fabrics used as catalysts
US3881877A (en) * 1971-10-05 1975-05-06 Matthey Bishop Inc Catalyst supporting screen
DE2829035A1 (en) * 1978-07-01 1980-01-10 Heraeus Gmbh W C Silver or platinum metal catalyst in form of fibre felt - used for ammonia oxidn. and mfr. of hydrogen cyanide and formaldehyde
DE2855102A1 (en) * 1978-12-20 1980-07-17 Inst Nawozow Sztucznych W Pula Catalyst contg. platinum and palladium based layers - used in oxidn. of ammonia to form nitric oxide
GB2062486B (en) * 1979-11-08 1984-09-19 Johnson Matthey Co Ltd Catalytic gauze packs
AU550041B2 (en) * 1981-08-12 1986-02-27 Engelhard Corporation Recovering platinum and rhodium in nitric acid plant
DE3781629T2 (en) * 1986-08-06 1993-02-18 Engelhard Corp PLATINUM-COATED PLATINUM AND RHODIUM CATALYST FIBERS, THEIR PRODUCTION AND USE FOR THE OXYDATION OF AMMONIA.
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Also Published As

Publication number Publication date
NO920986D0 (en) 1992-03-13
BR9200886A (en) 1992-11-17
PL293835A1 (en) 1993-03-08
RU2017520C1 (en) 1994-08-15
KR920017714A (en) 1992-10-21
NO920986L (en) 1992-09-17
HU9200872D0 (en) 1992-05-28
CS75792A3 (en) 1992-10-14
CN1065027A (en) 1992-10-07
BG60171B2 (en) 1993-11-30
YU24892A (en) 1994-06-10
JPH0564746A (en) 1993-03-19
TR26402A (en) 1995-03-15
HU211812B (en) 1995-12-28
PL166988B1 (en) 1995-07-31
EP0504723B1 (en) 1993-08-25
IL101187A0 (en) 1992-11-15
DE4206199C1 (en) 1992-11-12
ATE93410T1 (en) 1993-09-15
BG60171B1 (en) 1993-12-27
ES2046903T3 (en) 1994-02-01
DK0504723T3 (en) 1993-11-29
FI921093A (en) 1992-09-17
DE59200009D1 (en) 1993-09-30
EP0504723A1 (en) 1992-09-23
NO300671B1 (en) 1997-07-07
AU644725B2 (en) 1993-12-16
MX9201108A (en) 1992-12-21
AU1291792A (en) 1992-09-17
FI921093A0 (en) 1992-03-13
HUT63589A (en) 1993-09-28
CN1035042C (en) 1997-06-04

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Legal Events

Date Code Title Description
FZDE Discontinued