GAUZES HAVING A TERTIARY STRUCTURE FOR THE CATALYTIC CONVERSION OF FLUIDS
20230321644 · 2023-10-12
Inventors
Cpc classification
D04B1/14
TEXTILES; PAPER
International classification
C01B21/26
CHEMISTRY; METALLURGY
C01C3/02
CHEMISTRY; METALLURGY
Abstract
Three-dimensionally knitted noble metal gauzes, or sections of such gauzes, for carrying out catalytic reactions of fluids are knitted in two or multiple layers and the meshes of the individual layers are connected to one another in one form by a pile thread or multiple pile threads, so that the noble metal gauze has a tertiary structure.
Claims
1. Three-dimensionally weft-knitted noble-metal gauzes or partial pieces of such gauzes for carrying out catalytic reactions of fluids, wherein the gauzes are weft-knitted in two or more layers and the stitches of the individual layers are connected with one another by one pile thread or several pile threads in such a way that the noble-metal gauze has a tertiary structure.
2. Three-dimensionally weft-knitted noble-metal gauzes or partial pieces of such gauzes for carrying out catalytic reactions of fluids, wherein the gauzes are weft-knitted in two or more layers and the stitches of the individual layers are connected with one another by one pile thread or several pile threads in such a way that the noble-metal gauze has a tertiary structure, wherein partial regions of the pile thread or of the pile threads are disposed at greater than 0 degrees to less than 40 degrees relative to the gauze surface.
3. Three-dimensionally weft-knitted noble-metal gauzes or partial pieces of such gauzes for carrying out catalytic reactions of fluids, wherein the gauzes are weft-knitted in two or more layers and the stitches of the individual layers are connected with one another by one pile thread or several pile threads in such a way that individual stitches are selectively skipped, so that the noble-metal gauze has a tertiary structure.
4. Three-dimensionally weft-knitted noble-metal gauzes or partial pieces of such gauzes for carrying out catalytic reactions of fluids, wherein the gauzes are weft-knitted in two or more layers and the stitches of the individual layers are connected with one another by one pile thread or several pile threads in such a way that individual stitches are selectively skipped periodically, so that the noble-metal gauze has a tertiary structure.
5. Three-dimensionally weft-knitted noble-metal gauzes or partial pieces of such gauzes for carrying out catalytic reactions of fluids, wherein the gauzes are weft-knitted in two or more layers and the stitches of the individual layers are connected with one another by one pile thread or several pile threads in such a way that individual stitches are selectively skipped non-periodically, so that the noble-metal gauze has a tertiary structure.
6. Three-dimensionally weft-knitted noble-metal gauzes or partial pieces of such gauzes according to claim 1, wherein the stitches of the individual layers are connected with one another by pile threads in such a way that the gauze has a wavelike tertiary structure.
7. Three-dimensionally weft-knitted noble-metal gauzes or partial pieces of such gauzes according to claim 1, wherein the stitches of the individual layers are connected with one another by pile threads in such a way that the gauze has a non-symmetric tertiary structure.
8. Three-dimensionally weft-knitted noble-metal gauzes or partial pieces of such gauzes according to claim 1, wherein the stitches of the individual layers are connected with one another by pile threads in such a way that the gauze has a non-periodic tertiary structure.
9. Three-dimensionally weft-knitted noble-metal gauzes or partial pieces of such gauzes according to claim 1 for carrying out heterogeneous gas reactions.
10. Three-dimensionally weft-knitted noble-metal gauzes or partial pieces of such gauzes according to claim 1 for catalytic oxidation of ammonia with air for production of nitric acid (Oswald process).
11. Three-dimensionally weft-knitted noble-metal gauzes or partial pieces of such gauzes according to claim 1 for conversion of ammonia with methane in the presence of oxygen to hydrogen cyanide (Andrussow process).
Description
[0017] The invention present herein unites the advantages of both processes, since the gauzes produced with this process have not only a primary structure and secondary structure but also a tertiary structure. The tertiary structure, e.g. wavelike, is obtained in this case directly from the weft-knitting process and does not require any induction by a rigid surface that may be catalytically inactive.
[0018] For this purpose, a gauze in two or more layers of stitches is connected by pile threads in such a way that a tertiary structure, for example a wave pattern, is obtained. The tertiary structure may be symmetric but does not have to be. Even non-symmetric structures may be generated with this process. Gauzes for all reactor types may be weft-knitted without any need for a new reactor. Possible size limitations due to weft-knitting machines can be circumvented by joining several partial pieces together as one gauze. A production may be achieved by commercial machines, e.g. Stoll flatbed weft-knitting machines. The gauzes with secondary and tertiary structure can be produced directly in circular shape, or in partial pieces of a circular shape in composite gauzes for large reactors. A cutting-to-size of gauzes, which would produce cutting leftovers that have to be reprocessed, is not necessary.
[0019] The gauzes described here unite the advantages of the known three-dimensional gauzes (gauzes with secondary structure) with corrugated gauzes (gauzes with tertiary structure). Disadvantages are not created as a result.
[0020]
[0021] The invention present herein connects two layers of stitches by one or more pile threads. However, not all stitches are connected with one another, but instead stitches are selectively skipped and two layers of stitches are connected with one another in such a way that the pile threads exert, on the gauze, a pulling function that affects several stitches and leads to a desired tertiary structure, such as a wave pattern, for example.
[0022] The concept of the tertiary structure is of decisive importance and is to be understood in relation to the concept of the three dimensionality, which is not identical in meaning. The term “three-dimensional” is used in the documents EP 0 680 787 A1 and EP 1 358 010 B1. However, it does not mean and describe a tertiary structure in the present sense. The process described in those patents describes a connecting of several layers in a way that allows a gauze to grow in the third dimension. In the process, the actual gauze surface always remains planar, by analogy with a process in which planar gauzes would simply be stacked one above the other. With the process presented here, however, gauzes that have relief-like, non-planar topographic surfaces can be generated and are referred to here, in contrast to the three-dimensional gauzes, as gauzes with tertiary structure. In such gauzes, the individual layers are no longer parallel to one another in the manner of planes, as sketched in
[0023] Whereas the pile thread or pile threads in previous production processes, such as described in DE 101 05 624 A1 or US 6,073,467, for example, are oriented at 40 to 90 degrees to the gauze surface, the skipping of stitches means that at least partial regions of the pile thread or of the pile threads are disposed at greater than 0 degree to less than 40 degrees relative to the gauze surface or — in terms of the angle relative to the direction of gas flow — at greater than 50 degrees to less than 90 degrees. In this respect, reference is also made, for example to
[0024]
[0025] Due to the tertiary structure of the gauzes, the angle of admission of the gases becomes more favorable and a higher conversion can be achieved in the reaction. In principle, a gauze with a tertiary structure has a larger surface than a gauze without tertiary structure. Therefore a reactor incorporating the same number of gauze layers having tertiary structure is more effective, or else the same efficiency can be achieved with a smaller number of gauze layers. A more efficient reactor also reduces N.sub.2O emissions.
[0026]