METHOD FOR MANUFACTURING A PHOTOCATALYTIC DEVICE, PHOTOCATALYTIC DEVICE, PHOTOCATALYTIC COMPOSITION AND GAS DEPOLLUTING APPARATUS
20230025309 · 2023-01-26
Inventors
Cpc classification
B01D53/8668
PERFORMING OPERATIONS; TRANSPORTING
B01D2253/306
PERFORMING OPERATIONS; TRANSPORTING
B01J37/0045
PERFORMING OPERATIONS; TRANSPORTING
F24F8/167
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01D53/885
PERFORMING OPERATIONS; TRANSPORTING
B01J21/063
PERFORMING OPERATIONS; TRANSPORTING
B01D2257/708
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J35/00
PERFORMING OPERATIONS; TRANSPORTING
B01D53/88
PERFORMING OPERATIONS; TRANSPORTING
B01J21/06
PERFORMING OPERATIONS; TRANSPORTING
B01J29/70
PERFORMING OPERATIONS; TRANSPORTING
B01J37/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The invention refers to a method for manufacturing a catalytic device, with the steps: a) providing a first catalyst having photocatalytic activity, a second catalyst, which is a different molecule than the first catalyst, and an adsorbent, each in a powdered state, b) mingling the first catalyst, the second catalyst and the adsorbent to form a catalytic composition and suspending them in a suspension liquid to form a slurry, and c) repeatedly coating the slurry onto a solid grid-like carrier having a plurality of through holes, configured to allow a gas to flow through the carrier, and evaporating the suspension liquid.
Claims
1. A method for manufacturing a catalytic device, comprising: a) providing a first catalyst having photocatalytic activity, a second catalyst which is a different molecule than the first catalyst, and an adsorbent, each in a powdered state, b) mingling the first catalyst, the second catalyst and the adsorbent to form a catalytic composition and suspending the catalytic composition in a suspension liquid to form a slurry, and c) repeatedly coating the slurry onto a solid grid-like carrier having a plurality of through holes, wherein the carrier configured to allow a gas to flow through the carrier, and evaporating the suspension liquid.
2. The method according to claim 1, wherein the through holes account for at least 80% of a volume of the carrier.
3. The method according to claim 1 wherein the slurry is binder-free.
4. The method according to claim 1 wherein the slurry is coated onto the carrier via spray-coating.
5. The method according to claim 1 wherein the first catalyst is titanium dioxide.
6. The method according to claim 5, wherein the titanium dioxide is in a form of a mixture of anatase and rutile with an anatase/rutile ratio between 60/40 and 99/1.
7. The method according to claim 1 wherein the second catalyst is a low-temperature catalyst.
8. The method according to claim 1 wherein the adsorbent is a zeolite.
9. The method according to claim 1 wherein the providing step provides in weight percent with regard to their total mass: between 27% and 30% of the first catalyst, between 11% and 17% of the second catalyst, and between 55% and 59% of the adsorbent.
10. A catalytic device obtained by a method according to claim 1.
11. A catalytic composition, comprising in weight percent with regard to its total mass and each in a powdered state, between 27% and 30% of a first catalyst having photocatalytic activity, between 11% and 17% of a second catalyst which is a different molecule than the first catalyst, and between 55% and 59% of an adsorbent.
12. The catalytic composition according to claim 11, wherein the first catalyst is titanium dioxide the second catalyst is manganese monoxide and the adsorbent is a zeolite.
13. The catalytic composition according to claim 11, wherein the adsorbent is a synthetic hydrophilic zeolite of type A.
14. The catalytic composition according to claim 11, wherein the first catalyst is photo-activated.
15. The catalytic composition according to claim 11, being a non-thermal catalyst, and comprising, in weight percent with regard to its total mass: between 27% and 30% of photo-activated titanium dioxide as the first catalyst, between 11% and 17% of manganese monoxide as the second catalyst, between 55% and 59% of synthetic hydrophilic zeolite of type A as the adsorbent.
16. A gas depolluting apparatus, comprising a catalytic device according to claim 10 and/or a catalytic composition comprising in weight percent with regard to total mass and each in a powdered state, between 27% and 30% of a first catalyst having photocatalytic activity, between 11% and 17% of a second catalyst which is a different molecule than the first catalyst, and between 55% and 59% of an adsorbent coated onto a carrier, wherein the catalytic device and/or the catalytic composition is at least partially provided within a designated flow path of gas to be depolluted.
17. The gas depolluting apparatus according to claim 16, further comprising at least one source of UV radiation arranged in the designated flow path and configured to irradiate the catalytic composition and/or the catalytic device in order to activate the first catalyst.
18. The gas depolluting apparatus according to claim 17, wherein the at least one source of UV radiation is arranged in the designated flow path and the catalytic device or catalytic composition is arranged upstream and a second catalytic device identical to the catalytic device or a second catalytic composition identical to the catalytic composition is arranged downstream of the at least one source of UV radiation.
Description
[0156] Embodiments of the invention will be explained with respect to the attached figures.
[0157]
[0158]
[0159]
[0160]
[0161] In
[0162] The carrier 2 has a longitudinal axis L, along which the length of the combs 4 extends. The combs 4 each have a hexagonal cross section, which preferably remains constant along their length. Correspondingly, the through holes 6 also have a hexagonal cross section.
[0163] In
[0164] However, in
[0165]
[0166] The depolluting unit 16 comprises two catalytic devices 8, of which only one is depicted in
[0167] The depolluting unit 16 further comprises a UV radiation source 20, designed as an array of four UV radiation emitting lamps 22. Preferably these are lamps emitting UV-C radiation. The lamps 22 are arranged within a unit frame 24. The unit frame 24 preferably comprises sockets 26 for removably mounting the UV emitting lamps 22. Preferably the unit frame 24 furthermore comprises at least one power supply for the UV emitting lamps 22.
[0168] The unit frame 24 also comprises two receptacles 28 to accommodate the catalytic devices 8. In
[0169] The gas to be depolluted flows through the carriers 2 and the UV radiation source 20 along the direction of flow F. Obviously, the direction of flow F, depending on the design of the gas depolluting apparatus, can also run in the opposite direction. The direction of flow F especially runs along the longitudinal axis L.
[0170] One advantage of the depolluting unit 16 being designed as depicted is, that the catalytic devices 8 and correspondingly the catalysts within the coating 10 of the carriers 2 are spatially very close to the UV radiation source 20. Therefore, the UV radiation can be used well for activating the photocatalyst, especially because on both sides of the UV radiation source 20 a catalytic device 8 is present. In addition, the waste heat of the lamps 22 can be used to enhance the catalytic activity of the second catalyst, which preferably is a low-temperature catalyst.
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REFERENCE SIGNS
[0172] 2 carrier [0173] 4 comb [0174] 6 through hole [0175] 8 catalytic device [0176] 10 coating [0177] 12 inner surface [0178] 14 outer surface [0179] 16 depolluting unit [0180] 18 carrier housing [0181] 20 UV radiation source [0182] 22 UV emitting lamp [0183] 24 unit frame [0184] 26 socket [0185] 28 receptacle [0186] 30 support surface