HIGHLY CHLORINE- AND WATER-RESISTANT CATALYST, PREPARATION METHOD THEREFOR AND USE THEREOF

Abstract

A preparation method for a highly chlorine- and water-resistant catalyst is provided. A mixture of at least one of SnO.sub.2, GeO.sub.2, and MoO.sub.2 with CeO.sub.2 is used as a catalyst support, face-centered cubic ruthenium oxide is used as an active component, and the catalyst with excellent chlorine- and water-resistance is prepared through selective adsorption regulation, which can realize safe and efficient purification of chlorine-containing organic waste gas at temperatures below 250° C.

Claims

1. A preparation method for a highly chlorine- and water-resistant catalyst, comprising the following steps: (1) mixing MO.sub.x with CeO.sub.2 to obtain a MO.sub.xCeO.sub.2 support, wherein the MO.sub.x is at least one of SnO.sub.2, GeO.sub.2, and MoO.sub.2; (2) mixing ruthenium acetylacetonate, a reductant, and a stabilizer to obtain a first mixture, and carrying out a reduction reaction on the first mixture to obtain face-centered cubic (FCC) RuO.sub.x; (3) mixing the MO.sub.xCeO.sub.2 support obtained in step (1) with the FCC RuO.sub.x obtained in step (2) and water to obtain a second mixture, and carrying out supporting on the second mixture at a predetermined pH to obtain a catalyst precursor; and (4) calcining the catalyst precursor obtained in step (3) to obtain the highly chlorine- and water-resistant catalyst; wherein step (1) and step (2) have no order of priority.

2. The preparation method according to claim 1, wherein in step (1), the mixing is ball-milling, and the ball-milling is carried out at a rotation speed of 200-500 r/min for 6-24 h.

3. The preparation method according to claim 1, wherein in step (1), the MO.sub.x is 5-40% by mass of the MO.sub.xCeO.sub.2 support.

4. The preparation method according to claim 1, wherein in step (2), the reduction reaction is carried out at a temperature of 160-200° C. for 1-3 h, and the FCC RuO.sub.x has a particle size of 0.4-8 nm.

5. The preparation method according to claim 1, wherein in step (3), a mass of Ru in the FCC RuO.sub.x is 0.01-2% of a mass of the MO.sub.xCeO.sub.2 support.

6. The preparation method according to claim 1, wherein in step (3), the predetermined pH is determined by an isoelectric point of the MO.sub.xCeO.sub.2 support such that the FCC RuO.sub.x has a strong interaction with the MO.sub.x rather than the CeO.sub.2, and the supporting is carried out at a temperature of 40-60° C. for 1-6 h.

7. The preparation method according to claim 1, wherein in step (4), the calcining is carried out at a temperature of 300-450° C. for 2-6 h.

8. A chlorine- and water-resistant catalyst prepared by the preparation method according to claim 1.

9. The chlorine- and water-resistant catalyst according to claim 8, wherein in step (1) of the preparation method, the mixing is ball-milling, and the ball-milling is carried out at a rotation speed of 200-500 r/min for 6-24 h.

10. The chlorine- and water-resistant catalyst according to claim 8, wherein in step (1) of the preparation method, the MO.sub.x is 5-40% by mass of the MO.sub.xCeO.sub.2 support.

11. The chlorine- and water-resistant catalyst according to claim 8, wherein in step (2) of the preparation method, the reduction reaction is carried out at a temperature of 160-200° C. for 1-3 h, and the FCC RuO.sub.x has a particle size of 0.4-8 nm.

12. The chlorine- and water-resistant catalyst according to claim 8, wherein in step (3) of the preparation method, a mass of Ru in the FCC RuO.sub.x is 0.01-2% of a mass of the MO.sub.xCeO.sub.2support.

13. The chlorine- and water-resistant catalyst according to claim 8, wherein in step (3) of the preparation method, the predetermined pH is determined by an isoelectric point of the MO.sub.xCeO.sub.2support such that the FCC RuO.sub.x has a strong interaction with the MO.sub.x rather than the CeO.sub.2, and the supporting is carried out at a temperature of 40-60° C. for 1-6 h.

14. The chlorine- and water-resistant catalyst according to claim 8, wherein in step (4) of the preparation method, the calcining is carried out at a temperature of 300-450° C. for 2-6 h.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0022] FIG. 1 is an XRD pattern of RuO.sub.x/SnO.sub.2CeO.sub.2 prepared in Example 1;

[0023] FIG. 2 is an HR-TEM image of FCC RuO.sub.x in Example 1;

[0024] FIG. 3 is a graph showing the catalytic activity of the catalysts prepared in Examples 1-3;

[0025] FIG. 4 is a graph showing the stability of the catalysts prepared in Examples 1-3; and

[0026] FIG. 5 is a GC/MS pattern of by-products of the catalysts prepared in Examples 1-2.

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0027] The present invention provides a preparation method for a chlorine- and water-resistant catalyst, comprising the following steps: [0028] (1) mixing MO.sub.x with CeO.sub.2 to obtain a MO.sub.xCeO.sub.2 support, wherein MO.sub.x is at least one of SnO.sub.2, GeO.sub.2 and MoO.sub.2; [0029] (2) mixing ruthenium acetylacetonate, a reductant and a stabilizer, and carrying out a reduction reaction to obtain FCC RuO.sub.x; [0030] (3) mixing the MO.sub.xCeO.sub.2 support obtained in step (1) with RuO.sub.x obtained in step (2) and water, and carrying out supporting at a certain pH to obtain a catalyst precursor; and [0031] (4) calcining the catalyst precursor obtained in step (3) to obtain a chlorine- and water-resistant catalyst; [0032] wherein step (1) and step (2) have no order of priority.

[0033] In the present invention, MO.sub.x is mixed with CeO.sub.2 to obtain a MO.sub.xCeO.sub.2 support.

[0034] In the present invention, MO.sub.x is at least one of SnO.sub.2, GeO.sub.2 and MoO.sub.2, and MO.sub.x is preferably rutile-type. In the present invention, MO.sub.xCeO.sub.2 is a support material of the catalyst and is used for supporting ruthenium oxide.

[0035] In the present invention, the mixing is preferably ball-milling, the ball-milling is preferably carried out at a rotation speed of 200-500 r/min, and the ball-milling is preferably carried out for 6-24 h.

[0036] In the present invention, in step (1), MO.sub.x is preferably 5-40%, and more preferably 10-15%, by mass of the MO.sub.xCeO.sub.2 support.

[0037] In the present invention, ruthenium acetylacetonate, a reductant and a stabilizer are mixed, and a reduction reaction is carried out to obtain FCC RuO.sub.x. In the present invention, ruthenium oxide RuO.sub.x with a face-centered cubic structure is prepared by solvent reduction method using ruthenium acetylacetonate as a precursor of an active component Ru in the presence of a reductant and a stabilizer.

[0038] In the present invention, the reductant is preferably triethylene glycol (TEG), and the stabilizer is preferably polyvinylpyrrolidone (PVP). In the present invention, ruthenium acetylacetonate is used as a precursor of an active component Ru, and the stabilizer is used for preventing the aggregation of nanoparticles and thus achieving the effect of stabilizing the reaction system.

[0039] In the present invention, the reductant and ruthenium acetylacetonate are preferably in a molar ratio of (20-1000):1; the stabilizer and ruthenium acetylacetonate are preferably in a molar ratio of (0.1-20):1.

[0040] In the present invention, the reduction reaction is preferably carried out at a temperature of 160-200° C., and the reduction reaction is preferably carried out for 1-3 h.

[0041] In the present invention, after the reduction reaction is completed, the product obtained by the reduction reaction is preferably subject to separation and washing sequentially to obtain RuO.sub.x.

[0042] In the present invention, the separation is preferably centrifugal separation, and a solvent used for the washing is preferably acetone or toluene. In the present invention, operations of the separation are not particularly limited, and any operation known to those skilled in the art can be used.

[0043] In the present invention, RuO.sub.x preferably has a particle size of 0.4-8 nm. In the present invention, controlling the particle size of RuO.sub.x can further improve the dispersibility and catalytic activity of the active component, thereby further improving the chlorine- and water-resistance of the catalyst.

[0044] In the present invention, after the MO.sub.xCeO.sub.2 support and RuO.sub.x are obtained, the MO.sub.xCeO.sub.2 support is mixed with RuO.sub.x and water, and supporting is carried out at a certain pH to obtain a catalyst precursor. In the present invention, during the supporting, the surface of MO.sub.X in the support is negatively charged due to the deprotonation reaction of hydroxyl groups, the surface of RuO.sub.x is positively charged due to the protonation reaction of hydroxyl groups, and the surface of CeO.sub.2 in the support is positively charged due to the protonation reaction of hydroxyl groups, so that RuO.sub.x is preferentially and selectively adsorbed on MO.sub.x in the support under electrostatic interaction, and a small part of RuO.sub.x is adsorbed on CeO.sub.2 in the support under weak interaction; when MO.sub.x is in the rutile crystal form, under strong electrostatic interaction, RuO.sub.x shows good dispersibility on MO.sub.X due to the similar unit cell parameters.

[0045] In the present invention, the mass of Ru in RuO.sub.x is preferably 0.01-2% of the mass of the MO.sub.xCeO.sub.2 support. In the present invention, by controlling the mass of RuO.sub.x, the low-temperature chlorine-resistance of the catalyst can be further improved. In the present invention, the amount of water used is not particularly limited as long as full mixing of the support and RuO.sub.x can be ensured.

[0046] In the present invention, the supporting is preferably carried out at a temperature of 40-60° C.; the supporting is preferably carried out for 1-6 h; the pH of the solution during the supporting is preferably between an isoelectric point of MO.sub.x and an isoelectric point of RuO.sub.x; when MO.sub.x is SnO.sub.2, the pH is preferably 5-6; and the pH is preferably adjusted with a hydrochloric acid solution or a sodium hydroxide solution. In the present invention, by controlling the pH of the solution during the supporting, the most beneficial supporting effect is achieved.

[0047] In the present invention, after the supporting is completed, the product obtained by the supporting is preferably dried to obtain a catalyst precursor. In the present invention, operations of the drying are not particularly limited as long as the product is dried to a constant weight.

[0048] In the present invention, after the catalyst precursor is obtained, the catalyst precursor is calcined to obtain a chlorine- and water-resistant catalyst.

[0049] In the present invention, the calcining is preferably carried out at a temperature of 300-450° C.; and the calcining is preferably carried out for 2-6 h.

[0050] In the present invention, FCC RuO.sub.x is preferentially and selectively adsorbed on MO.sub.x of the MO.sub.xCeO.sub.2 support, which provides good chlorine poisoning-resistance, water-resistance and oxidation performance, and can be used for treating industrial organic waste gas containing chlorine-containing volatile organic compounds with high dechlorination efficiency and long catalytic life; the prepared catalyst can realize complete catalytic oxidation of various volatile organic compounds and chlorine-containing volatile organic compounds at temperatures below 250° C., and can maintain long-term water-resistance stability.

[0051] The present invention further provides a chlorine- and water-resistant catalyst prepared by the preparation method described in the above technical solutions.

[0052] In the present invention, the active component of the chlorine- and water-resistant catalyst is FCC RuO.sub.x, the support is MO.sub.xCeO.sub.2, and the catalyst features high activity, strong chlorine-resistance, strong water-resistance and the like, and can be widely used in the catalytic combustion treatment of chlorine-containing volatile organic compounds.

[0053] The present invention further provides use of the chlorine- and water-resistant catalyst described in the above technical solutions in treating a chlorine-containing volatile organic compound.

[0054] The technical solutions in the present invention will be clearly and completely described below with reference to the examples in the present invention. It is apparent that the described examples are only a part of the examples of the present invention, but not all of them. Based on the examples of the present invention, all other examples obtained by those of ordinary skill in the art without creative effort shall fall within the protection scope of the present invention.

EXAMPLE 1

[0055] The preparation of the chlorine- and water-resistant catalyst was conducted as follows.

[0056] (1) Rutile-type SnO.sub.2 and CeO.sub.2 nanorods in a mass ratio of 1:9 were ball-milled at a rotation speed of 300 r/min for 12 h to obtain a SnO.sub.2CeO.sub.2 support.

[0057] (2) Ruthenium acetylacetonate, TEG and PVP were mixed, and a reduction reaction was carried out in an oil bath at 185° C. for 3 h, followed by centrifugal separation and washing with acetone to obtain FCC RuO.sub.x with a size of 2.3 nm; wherein TEG and ruthenium acetylacetonate were in a molar ratio of 200:1; PVP and ruthenium acetylacetonate were in a molar ratio of 5:1.

[0058] (3) The SnO.sub.2CeO.sub.2 support obtained in step (1) was mixed with RuO.sub.x obtained in step (2) and water, the resulting mixture was stirred at 50° C. for 2 h for supporting, and then dried to obtain a catalyst precursor; wherein the pH of the solution during the supporting was 6, and the mass of Ru in RuO.sub.x was 1% of the mass of the SnO.sub.2CeO.sub.2 support.

[0059] (4) The catalyst precursor obtained in step (3) was calcined at 350° C. for 4 h to obtain a RuO.sub.x/SnO.sub.2CeO.sub.2 chlorine- and water-resistant catalyst.

[0060] The XRD pattern of RuO.sub.x/SnO.sub.2CeO.sub.2 prepared in Example 1 is shown in FIG. 1, and the TEM image of RuO.sub.x in Example 1 is shown in FIG. 2. It can be seen from FIG. 2 that RuO.sub.x was in a face-centered cubic structure and had a size of 2.3 nm.

[0061] The catalytic activity test of the chlorine- and water-resistant catalyst prepared in Example 1 was carried out on a fixed bed reactor, the loading amount of the catalyst was 1.0 g, the granularity was 40-60 mesh, and the initial gas concentrations were as follows: chlorobenzene=500 ppm, [O.sub.2]=10 vol %, N.sub.2 as a carrier gas, gas hourly space velocity (GHSV)=10000 h.sup.−1-. The reaction temperature for the test was 100-250° C., the results are shown in FIG. 3, the stability is shown in FIG. 4, and the GC/MS test results of the by-products are shown in FIG. 5.

EXAMPLE 2

[0062] The preparation of the chlorine- and water-resistant catalyst was conducted as follows.

[0063] (1) Rutile-type SnO.sub.2 and CeO.sub.2 nanorods in a mass ratio of 1:4 were ball-milled at a rotation speed of 300 r/min for 24 h to obtain a SnO.sub.2CeO.sub.2 support.

[0064] (2) Ruthenium acetylacetonate, TEG and PVP were mixed, and a reduction reaction was carried out in an oil bath at 185° C. for 3 h, followed by centrifugal separation and washing with acetone to obtain FCC RuO.sub.x with a size of 2.3 nm; wherein TEG and ruthenium acetylacetonate were in a molar ratio of 200:1; PVP and ruthenium acetylacetonate were in a molar ratio of 5:1.

[0065] (3) The SnO.sub.2CeO.sub.2 support obtained in step (1) was mixed with RuO.sub.x obtained in step (2) and water, the resulting mixture was stirred at 50° C. for 2 h for supporting, and then dried to obtain a catalyst precursor; wherein the pH of the solution during the supporting was 5.5, and the mass of Ru in RuO.sub.x was 1% of the mass of the SnO.sub.2CeO.sub.2 support.

[0066] (4) The catalyst precursor obtained in step (3) was calcined at 400° C. for 4 h to obtain a RuO.sub.x/SnO.sub.2CeO.sub.2 chlorine- and water-resistant catalyst.

[0067] The catalytic activity test of the chlorine- and water-resistant catalyst prepared in Example 2 was carried out on a fixed bed reactor, the loading amount of the catalyst was 1.0 g, the granularity was 40-60 mesh, and the initial gas concentrations were as follows: chlorobenzene=1000 ppm, [O.sub.2]=10 vol %, [H.sub.2O]=5 vol %, N.sub.2 as a carrier gas, GHSV=10000 h.sup.−1. The reaction temperature for the test was 100-250° C., the results are shown in FIG. 3, the stability is shown in FIG. 4, and the GC/MS test results of the by-products are shown in FIG. 5.

EXAMPLE 3

[0068] The preparation of the chlorine- and water-resistant catalyst was conducted as follows.

[0069] (1) Rutile-type MoO.sub.2 and CeO.sub.2 nanospheres in a mass ratio of 1:9 were ball-milled at a rotation speed of 500 r/min for 6 h to obtain a MoO.sub.2CeO.sub.2 support.

[0070] (2) Ruthenium acetylacetonate, TEG and PVP were mixed, and a reduction reaction was carried out in an oil bath at 200° C. for 2 h, followed by centrifugal separation and washing with acetone to obtain FCC RuO.sub.x with a size of 3.5 nm; wherein TEG and ruthenium acetylacetonate were in a molar ratio of 100:1; PVP and ruthenium acetylacetonate were in a molar ratio of 5:1.

[0071] (3) The MoO.sub.2CeO.sub.2 support obtained in step (1) was mixed with RuO.sub.x obtained in step (2) and water, the resulting mixture was stirred at 50° C. for 2 h for supporting, and then dried to obtain a catalyst precursor; wherein the pH of the solution during the supporting was 5.5, and the mass of Ru in RuO.sub.x was 2% of the mass of the MoO.sub.2CeO.sub.2 support.

[0072] (4) The catalyst precursor obtained in step (3) was calcined at 350° C. for 4 h to obtain a RuO.sub.x/MoO.sub.2CeO.sub.2 chlorine- and water-resistant catalyst.

[0073] The catalytic activity test of the chlorine- and water-resistant catalyst prepared in Example 3 was carried out on a fixed bed reactor, the loading amount of the catalyst was 1.0 g, the granularity was 40-60 mesh, and the initial gas concentrations were as follows: dichloromethane=1000 ppm, [O.sub.2]=10 vol %, [H.sub.2O]=5 vol %, N.sub.2 as a carrier gas, GHSV=20000 h.sup.−1. The reaction temperature for the test was 100-250° C., the results are shown in FIG. 3, and the stability is shown in FIG. 4.

[0074] It can be seen from FIGS. 3 and 4 that the catalysts prepared in Examples 1-3 could realize complete catalytic oxidation of various chlorine-containing volatile organic compounds at temperatures below 250° C., and could maintain long-term stability and good water-resistance stability.

[0075] It can be seen from FIG. 5 that the catalysts prepared in Examples 1-2 showed good formation of by-products when tested at 250° C.

[0076] The above descriptions are only preferred embodiments of the present invention. It should be noted that those of ordinary skill in the art can also make several improvements and modifications without departing from the principle of the present invention, and such improvements and modifications shall fall within the protection scope of the present invention.