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 processesInfo
- 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
Links
- 238000000034 method Methods 0.000 title claims description 24
- 229910000510 noble metal Inorganic materials 0.000 title claims description 14
- 230000003197 catalytic effect Effects 0.000 title claims description 13
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 30
- 238000009940 knitting Methods 0.000 claims abstract description 23
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 19
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims abstract description 18
- 230000003647 oxidation Effects 0.000 claims abstract description 16
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 16
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 15
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910052751 metal Inorganic materials 0.000 claims abstract description 12
- 239000002184 metal Substances 0.000 claims abstract description 12
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 10
- 238000011084 recovery Methods 0.000 claims abstract description 10
- 229910052703 rhodium Inorganic materials 0.000 claims abstract description 10
- 239000010948 rhodium Substances 0.000 claims abstract description 10
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 9
- 229910052763 palladium Inorganic materials 0.000 claims abstract description 6
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910052802 copper Inorganic materials 0.000 claims abstract description 5
- 239000010949 copper Substances 0.000 claims abstract description 5
- -1 platinum metals Chemical class 0.000 claims abstract description 5
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 claims abstract 4
- 229910000881 Cu alloy Inorganic materials 0.000 claims description 4
- 229910000629 Rh alloy Inorganic materials 0.000 claims description 4
- 229910000990 Ni alloy Inorganic materials 0.000 claims description 2
- PXXKQOPKNFECSZ-UHFFFAOYSA-N platinum rhodium Chemical compound [Rh].[Pt] PXXKQOPKNFECSZ-UHFFFAOYSA-N 0.000 claims description 2
- 239000003054 catalyst Substances 0.000 abstract description 8
- BALRIWPTGHDDFF-UHFFFAOYSA-N rhodium Chemical compound [Rh].[Rh] BALRIWPTGHDDFF-UHFFFAOYSA-N 0.000 description 7
- 229910001252 Pd alloy Inorganic materials 0.000 description 3
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 229910001260 Pt alloy Inorganic materials 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 229910001092 metal group alloy Inorganic materials 0.000 description 2
- 238000009941 weaving Methods 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- YOCUPQPZWBBYIX-UHFFFAOYSA-N copper nickel Chemical compound [Ni].[Cu] YOCUPQPZWBBYIX-UHFFFAOYSA-N 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000010814 metallic waste Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000012958 reprocessing Methods 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 238000005491 wire drawing Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/58—Fabrics or filaments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/46—Ruthenium, rhodium, osmium or iridium
- B01J23/464—Rhodium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/74—Iron group metals
- B01J23/755—Nickel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts 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
- B01J23/892—Nickel and noble metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/89—Catalysts 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
- B01J23/8926—Copper and noble metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/20—Nitrogen oxides; Oxyacids of nitrogen; Salts thereof
- C01B21/24—Nitric oxide (NO)
- C01B21/26—Preparation by catalytic or non-catalytic oxidation of ammonia
- C01B21/265—Preparation by catalytic or non-catalytic oxidation of ammonia characterised by the catalyst
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/20—Nitrogen oxides; Oxyacids of nitrogen; Salts thereof
- C01B21/24—Nitric oxide (NO)
- C01B21/26—Preparation by catalytic or non-catalytic oxidation of ammonia
- C01B21/267—Means for preventing deterioration or loss of catalyst or for recovering lost catalyst
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04B—KNITTING
- D04B1/00—Weft knitting processes for the production of fabrics or articles not dependent on the use of particular machines; Fabrics or articles defined by such processes
- D04B1/14—Other fabrics or articles characterised primarily by the use of particular thread materials
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2101/00—Inorganic fibres
- D10B2101/20—Metallic fibres
-
- D—TEXTILES; PAPER
- D10—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B—INDEXING SCHEME ASSOCIATED WITH SUBLASSES OF SECTION D, RELATING TO TEXTILES
- D10B2403/00—Details of fabric structure established in the fabric forming process
- D10B2403/02—Cross-sectional features
- D10B2403/024—Fabric incorporating additional compounds
- D10B2403/0242—Fabric 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.
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.
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.
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.
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) |
Families Citing this family (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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. |
DE68900928D1 (en) * | 1988-10-12 | 1992-04-09 | Johnson Matthey Plc | METAL FABRIC. |
-
1992
- 1992-02-28 DE DE4206199A patent/DE4206199C1/de not_active Expired - Lifetime
- 1992-03-10 IL IL101187A patent/IL101187A0/en unknown
- 1992-03-11 DK DK92104159.6T patent/DK0504723T3/en active
- 1992-03-11 ES ES199292104159T patent/ES2046903T3/en not_active Expired - Lifetime
- 1992-03-11 EP EP92104159A patent/EP0504723B1/en not_active Expired - Lifetime
- 1992-03-11 DE DE92104159T patent/DE59200009D1/en not_active Expired - Lifetime
- 1992-03-11 AT AT92104159T patent/ATE93410T1/en not_active IP Right Cessation
- 1992-03-12 YU YU24892A patent/YU24892A/en unknown
- 1992-03-12 TR TR92/0241A patent/TR26402A/en unknown
- 1992-03-13 MX MX9201108A patent/MX9201108A/en not_active IP Right Cessation
- 1992-03-13 BR BR929200886A patent/BR9200886A/en not_active IP Right Cessation
- 1992-03-13 CS CS92757A patent/CS75792A3/en unknown
- 1992-03-13 BG BG096061A patent/BG60171B1/en unknown
- 1992-03-13 NO NO920986A patent/NO300671B1/en not_active IP Right Cessation
- 1992-03-13 AU AU12917/92A patent/AU644725B2/en not_active Expired - Fee Related
- 1992-03-13 JP JP4054705A patent/JPH0564746A/en active Pending
- 1992-03-13 CA CA002063041A patent/CA2063041A1/en not_active Abandoned
- 1992-03-13 PL PL92293835A patent/PL166988B1/en unknown
- 1992-03-13 RU SU925011029A patent/RU2017520C1/en active
- 1992-03-13 FI FI921093A patent/FI921093A/en not_active Application Discontinuation
- 1992-03-14 KR KR1019920004187A patent/KR920017714A/en not_active Application Discontinuation
- 1992-03-14 CN CN92101748A patent/CN1035042C/en not_active Expired - Lifetime
- 1992-03-16 HU HU9200872A patent/HU211812B/en not_active IP Right Cessation
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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