CA1065833A

CA1065833A - Catalyst for use in treating gas

Info

Publication number: CA1065833A
Application number: CA244,394A
Authority: CA
Inventors: Kunio Kimura; Atsushi Nishino; Kazunori Sonetaka
Original assignee: Matsushita Electric Industrial Co Ltd
Current assignee: Panasonic Holdings Corp
Priority date: 1975-01-29
Filing date: 1976-01-28
Publication date: 1979-11-06
Also published as: DE2603161C3; US4065406A; GB1495101A; AU1054276A; AU502340B2; JPS5430398B2; JPS5187186A; DE2603161A1; DE2603161B2; FR2299081A1; FR2299081B1

Abstract

ABSTRACT OF THE DISCLOSURE
A catalyst for oxidation of carbon monoxide, nitrogen monoxide, or sulfur dioxide comprises a mixture of, by weight, 45 to 75% manganese dioxide, 15 to 25% calcium aluminate, 5 to 15% iron oxyhydroxide, and 2 to 20% copper hydroxycarbonate. To prepare the catalyst, water is added to the mixture which is then formed into a body of desired shape and cured preliminarily in air and then in the presence of water e.g. in steam, to solidify the body. The solidified body can also be heated at a temperature between 220°C and 850°C for 1 to 5 hours.

Description

~S8~3 ;:
Background of the Invention The same inventors as those of the present invention proposed a catalyst for use in purifying exhaust ;
gas, said catalyst comprising manganese dioxide, calcium aluminate and heat resistant aggregate. This catalyst has ;
been disclosed in U.S. Patent No. 3,905,917. The inventors have found that a catalyst comprising a mixture of manganese dioxide, calcium aluminate, iron oxyhydroxide and copper hydroxycarbonate and a catalyst prepared by heating said mixture are superior to the catalyst disclosed in U.S.
Patent No. 3,905,917 in the catalytic action of oxidation ~-of carbon monoxide, nitrogen monoxide or sulfur dioxide.
The present invention is based on this discovery. ;
This invention seeks to provide an improved catalyst for use in treating~gas, particularly for oxidation of carbon monoxide (CO), nitrogen monoxide (NO) or sulfur dioxide (SO2), and a process of preparing such a catalyst.
According to one aspect of this invention there i`
is provided a catalyst comprising a mixture of from 45 to 75% by weight of manganese dioxide, from 15 to 25% by weight of calcium alumina~e, from 5 to 15% by weight of iron oxy-hydroxide, and Erom 2 to 20% by weight of copper hydroxy-carbonate.
Such a catalyst can be used for oxidiæing CO, NO
or SO2 contained in air or oxygen-containing gas to CO2, NO2 or SO3, respectively.
According to another aspect of this invention there is provided a process of preparing a catalyst, comprising the steps of: adding water to a mixture of from 45 to 75%
by weight of manganese dioxide, from 15 to 25~ by weight of calcium aluminate, from 5 to 15% by weight of iron oxy-,., ~.

5~333 hydroxide, and from 2 to 20% by weight of copper hydroxy-carbonate; forming the mixture into a body of a desired shape, carrying out preliminary curing of the body in air;
and accomplishing curing of the body in the presence of water to solidify the body.
The mixture preferably comprises from 2 to 10 by weight of copper hydroxycarbonate.
The process preferably includes the further step of heating the solidi*ied body at a temperature between 220C
and 850C for 1 to 5 hours.
The manganese dioxide is preferably r-MnO2 having pH values of from 4 to 8.
The calcium aluminate preferably comprises principally xCaO A~2O3, and calcium aluminate comprising from 60 to 85~ of ~23 and from 40 to 15% of CaO is suitably used. Alternatively, cements commercially available under the names of Alumina cement or High alumina cement may be used. The calcium aluminate is used as a binder.
Iron oxyhydroxide is FeO(OH).
29 Copper hydroxycarbonate is CuCO3 Cu(OH)2 or 2CuCO3 Cu(OH)2-~6583~

: ~.
The catalyst can be used over a wide temperature range of from 100C to 850C in oxidizing CO, NO and SO2 contained in air or oxygen-containing gas to CO2, NO2 and SO3, respectively.

.. . .
When the catalyst is used at temperatures above :
220C, copper hydroxycarbonate changes to CuO, and when the .~ .
catalyst is used above 275C, iron oxyhydroxide changes - to ~-Fe2O3. When the catalyst is heated at temperatures of ~` .
about 300C and 600C, it has the following compositions:

2 23 Y Fe2O3 - CuO (300C) ~-Mn2O3 - xCaO A~203 - ~-Fe203 - CuO (600C) When the catalyst is prepared by the process without the further heating step and is used at temperatures above 220C, the catalyst becomes the same as if it had been prepared by the process including the further heating step. :
The catalyst prepared in both ways can be used at temperatures hoth above and below 220C. -: :
i " , ;. .'',~', '.:' ; 20 .. . .

~. :

~4~ :
'~,'''," .

. . ... . . . . . .

3LC~65833 As stated above, the catalyst of the present inven~ion ef~ectively oxidizes CO, NO or SO2 to change CO, NO or SO2 to CO2, NO2 or SO3, respectively, and SO3 is combined with ~nOx (x = 1 or 2) and CaO in the catalyst to produce finally CaSO4. Accordingly, the catalyst is suitably used in treating gas toxygen-containing gas) containing CO, NO or SO2.
The superiority of the catalyst o~ the present invention will be shown in the examples.
The present invention is illustrated by the following examples with reference to the accompanying drawings. Unless otherwise set forth, all proportions (~) in this specification are by weight. In the drawings:
Figs. 1 to 3 are graphs illustrating the oxidation of CO as a function of temperature;
Figs. 4 and 5 are graphs illustrating the oxidation of CO as a function of the contents of iron oxyhydroxide and copper hydroxycarbonate, respectively;
Fig. 6 schematically illustrates a home oil heater in which a catalyst may be used;
Fig. 7 is a graph illustrating the removal of S2 as a function o time in the oil heater of Fi~. 6; and Fig. ~ is a graph illustrating the oxidation o~
WO as A function of temperatur~.
Example 1 Samples Nos. 1, 2, 3, 4, 5, 6 and 7 were provided, whiah comprise various weight percentages o~ the ingredients as shown in Table 1, as follows:

,~ ~

~ 5~33 .- .. .~.
Table 1 ~ Sample No.
Ingredient (%) ~ 1 2 3 4 5 6 7 _ . ._ . ..... _ . _ _ .. ~:
~-MnO2 65 65 65 65 70 75 80 Calcium aluminate 20 20 20 20 20 20 20 Iron oxyhy~roxide 10 15 -Copper hydroxycarbonate 5 15 Ferric oxide 10 10 Copper oxide 5 5 _ '', ~
The ingredients were mixed, and to 100 parts ~by ; weight) of the mixture was added 10 parts of water. Columnar shaped bodies having a size of 5 mm~ x 5 mm were made of the mixtures. The shaped bodies were dried in air and then sub-jected to the curing ln s~eam having a temperature o~ 65C to 95C ~or 1 hour.
65 g of each o the cured shaped bodies was filled in a quartz tube having an inside diameter o~ 30 mm. A gas ; including oxygen (15%) and nitrogen (84%), containing 1,500 ppm of carbon monoxide, was passed through the quartz tube ~
at a space velocity of 10,000 hr 1. Percentages oE oxidation ` `
o~ carbon monoxide are shown in FIG. 1.
From the results as shown in FIG. 1, it is evident that Sample No. 1 including iron oxyhydroxide and copper hydroxycarbonate is superior to other catalysts (Sample Nos.
2-7) and Sample No. 3 including copper hydroxycarbonate is superior to other catalysts of Sample Nos. 2 and 4-7 in the catalytic action of oxidation o~ carbon mon~xide.
. ~. . .
Calcium aluminate in this Example comprises alumina (54%), calcium oxide ~38%), ~erric oxide and titanium oxide `
' ... , , . , ':
. ,., " ., ~ ~651333 : .

(remainder). Calcium aluminate including 15 to 40~ of calcium oxide may be used.

~xample 2 Sample Nos. 11, 12, 13, 14 and 15 were provided which comprise various weight percentages of the ingredients as shown in Table 2, by repeating the same procedure as that of Example 1 and then heating the curea shaped bodies at a temperature of 800C for 4 hours.

Table 2 =~_ _No. _ __ _ __ Ingredient (~) 11 12 13 14 15 __ __ . _ ._ _ . _ ~-MnO2 65 65 75 75 80 Calcium aluminate20 20 20 20 20 Iron oxyhydroxide10 _ _ _ Copper hydroxycarbonate 5 5 5 _ Ferric oxide 10 Copper oxide _ ~

Percentages of oxida-tion oE carbon monoxide were measured in the same manner as -that oE Example 1. The results obtained are shown in FIG. 2. In FIG. 2, Curve No. 1 oE FIG.
1 also is shown with a view to comparing Sample No. 1 (Com-position A) with Sample No. 11 (Composition B).
From the results as shown in FIG. 2, it is evident that Sample No. 11 ~catalyst of the present invention, Com-position B) is superior to other catalysts (Sample Nos. 12, 13, 1~ and 15) in ~he catalytic action of oxidation of carbon monoxide at elevated temperatures and that Sample No. 1 (com-position A) is superior to Sample No. 11 (Composition B) in the catalytic action at lower temperatures than 200C.

~65833 Example 3 .
: The same procedure as shown in Example 2 was re-peated except that Sample No. 1 was heated at temperatures of 120C, 300C and 500C, respectively, for 4 hours to obtain Sample Nos. 21, 22 and 23. ~ -Percentages of oxidation of carbon monoxide of -Sample Nos. 21, 22 and 23 were measured in the same manner as that shown in Example 1. The results are shown in FIG. 3.
~s seen from the results, the catalysts of the present inven-tion are excellent in the catalytic action of oxidation of ~, carbon monoxide also when they have been heated previously at temperatures of 120C, 300C and 500C. Curve No. 11 of FIG. 3 is the same as Curve No. 11 of FIG. 2.

Example 4 ~, .
Sample Nos. 31-36 were provided, which comprise various weight percentages of the ingredients as shown in ~: .
Table 3, by repeating the same procedure as that of Example :
1 . ,:

Table 3 ample No. ~ ~ _ Ingredient (%) ~ 31 32 33 34 35 36 - -- ................. ,, _ ...
~-MnO2 75 73 70 65 60 55 .
Calcium aluminate 20 20 20 20 20 20 Iron oxyhydroxide _ 2 5 10 15 20 Copper hydroxycarbonate _ _ 5 5 5 5 _ As shown above, iron oxyhydroxide is contained in an amount of from zero % to 20%.
Percentages of oxidation of carbon monoxide were measured at a temperature of 300C in the same manner as that of Example 1, and the results obtained are shown in FIG. 4.

-~651~33 From the results, it is evident that catalysts containing iron oxyhydroxide of 5 to 15% are excellen-t in the catalytic action of oxidation o~ carbon monoxide.

Example 5 Sample Nos. 41-48 were provided, which comprise various weight percentages of the ingredients as shown in Table 4, by repeating the same procedure as that of Example 2 except that the shaped bodies were heated at a temperature of 500C, instead of 800C, for 4 hours.

Table 4 ~ .
Sample No.
Ingre-li Gn- ~ 4 I 42 43 44 45 46 ~ 48 y-MnO2 70 69 68 67 65 60 55 50 Calcium aluminate 20 20 20 20 20 20 20 20 Iron oxyhydroxide 10 10 10 10 10 10 10 10 Copper hydroxycarbonate _ 1 2 3 5 10 15 20 As shown above, copper hydroxycarbonate is contained in an amount oE from zero ~ to 20~.
Pexcentages of oxidation of carbon monoxide were measured at a temperature of 200C, and the results obtained are shown in FIG. 5. From the results obtained, it is evident that catalysts containing copper hyclroxycarbonate oE 2 to 10 are excellent in the catalytic action o oxidation of carbon monoxide.

Example 6 In this example, removal of SO2 by the catalyst o the present invention is illustrated. In FIG. 6, a ront view o a home oil heater is shown.

An oil (refined kerosene) is burned in the cylinder of heat resisting glass 1 having an inside diameter of 165 mm, "' ' ' ', ~ ,,, ' ' ': '.

~L~65833 in which the wire netting 2 and the metallic cylinder 3 are equipped with. A waste gas rises and passes through the layer of catalyst 4 which is held between two metallic screens 5 and 6, said screens being of 10 meshes. The layer of catalyst 4 consists of 127 pieces of Sample No. 11 in Example 2. The space velocity of the waste gas was about 10,000 hr 1.
In FIG. 7, Curve a shows an amount of SO2 which has been produced in the oil heater and Curve b shows an amount ~ -f S2 which has been removed by the catalyst. As shown by the curves, SO2 can completely be removed by the catalyst `
over 600 hours after the start of using the catalyst.
In this catalytic action, SO2 contained in an exhaust gas first is oxidized to SO3 and then SO3 is changed to MnSO4 and CaSO~ by the interaction with MnOX (x = 1 or 2) and CaO in the catalyst.

Example 7 A home oil heater as shown in FIG. 6 was worked in a room of 2 m3. Fifteen minutes after the start, the content of CO in the room reached 40 ppm. On the contrary, the con-tent of CO reached over 400 ppm in an oil heater not provided with the catalyst.

Example 8 In this example, ox.idat.ion of NO is illustrated.
Sample No. 51 was prepared by repeating the same procedure as that of Example 2 except that cobalt hydroxy-carbonate was used instead of copper hydroxycarbonate of Sample No. 1.
Oxidations of NO by using Samples No. 1, No. 51 and granular platinum (Pt) catalyst were compared in the same manner as that of Example 1 by using nitrogen gas con-taining 3% o oxygen and 1,000 ppm of NO at a space velocity of 8,000 hr 1.

~ ~5~3 The results obtained are shown in FIG. 8. As seen from the results, excellent catalyst for oxidation o~ NO at lower temperatures can be obtained by adding cobalt hydro~y-carbonate in an amount up to 10% to the catalysts of the pre-sent invention.
Oxides of cobalt, copper, vanadium and silver also may be added to the catalysts of the present invention.

Example 9 Mechanical strength of the catalysts o~ the present invention may be improved by adding rein~orcing ~illers to the catalysts.
Silica, asbestos, ceramic fibers (e.g. dealkalizated glass ~iber) and metallic wire (e.g. iron or copper wire having a size of 0.5 mm(~ x 30 mm) may be used as the rein-~orcing fillers.
Test pieces o~ the catalysts were prepared as ~llows:
Ingredients and rein~orcing filler as shown in the ~ollowing Table 5 were mixed with a small amount o~ water, and the mixtures were molded at a pressure of 0.5 ton/cm~ to obtain shaped bodies having a size o~ ~0 x 20 x 5 mm. Bending strength of the test pieces were measured at a room temperature and a~ter heating at a temperatuxe oE 500C Eor ~ hours.
The results obtained are shown in Table 5.

~L~65833 .
Table 5 ..
..

~ est piece No. _ _ _ . ~:
gredient ~ 61 62 63 64 65 relnforclng fllle ..
(parts by weight) ~ _ . .. .. ~ ~ ___ ': :
y-MnO2 6565 65 65 65 ~ . .
Calcium aluminate 2020 20 20 20 Iron oxyhydroxide 1010 10 10 10 Copper hydroxycarbonate 5 5 5 5 5 ;~ .
._ _ _ ,, silica Asbestos Glass Iron .-:.
Reinfor~ing filler _ fiber wire :.. :
_ ~ 10 --5 ~ 5 . A_____ ___=~ , ' ' .
Room : temperature 290 310 340 340 370 : Bending strength ~ , ~ _ - .
(kg/cm2) After heating at 250 260 290 300 320 :

... ,.. __ _ . , . ... : :;

As seen from the results, mechanical strength. of the catalyst can be improved by adding reinforcing fillers to ' the catalysts.

.

........ ..

Claims

THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:

1. A catalyst comprising a mixture of from 45 to 75 by weight of manganese dioxide, from 15 to 25% by weight of calcium aluminate, from 5 to 15% by weight of iron oxyhydroxide, and from 2 to 20% by weight of copper hydroxycarbonate.

2. A catalyst as claimed in claim 1 wherein said mixture comprises from 2 to 10% by weight of copper hydroxy-carbonate.

3. A catalyst as claimed in claim 1 or 2 and comprising a reinforcing filler.

4. A catalyst as claimed in claim 1 or 2 and comprising a reinforcing filler selected from silicon dioxide asbestos, glass fiber, and metallic wire.

5. A process of preparing a catalyst, comprising the steps of:
adding water to a mixture of from 45 to 75% by weight of manganese dioxide, from 15 to 25% by weight of calcium aluminate, from 5 to 15% by weight of iron oxyhydroxide, and from 2 to 20% by weight of copper hydroxycarbonate;
forming the mixture into a body of a desired shape;
carrying out preliminary curing of the body in air;
and accomplishing curing of the body in the presence of water to solidify the body.

6. A process as claimed in claim 5 wherein said mixture comprises from 2 to 10% by weight of copper hydroxy-carbonate.

7. A process as claimed in claim 5 or 6 wherein the curing is accomplished in steam at a temperature between 65°C
and 95°C.

8. A process as claimed in claim 5 or 6 and including the further step of heating the solidified body at a temperature between 220°C and 850°C for 1 to 5 hours.

9. A process as claimed in claim 5 or 6 wherein the curing is accomplished in steam at a temperature between 65°C
and 95°C, the process including the further step of heating the solidified body at a temperature between 220°C and 850°C for 1 to 5 hours.