Method for cleaning exhaust and industrial gases

专利摘要:
In this specification there is described a process for the purification of gases containing noxious constituents and especially the catalytic purification of gases containing noxious oxides of nitrogen. A gas containing the noxious oxides and including oxygen and a gaseous reducing fuel, is passed at a temperature above the ignition temperature of the gas and the fuel through a catalyst comprising an inert material impregnated or coated with a mixture or alloy of platinum and rhodium metals and rhodium is present in an amount of between 20 and 50 weight percent of the total metal content of the catalyst. The invention also includes catalysts for carrying out the above process.
公开号:SU1069606A3
申请号:SU1619887
申请日:1971-02-10
公开日:1984-01-23
发明作者:Джеймз Кейт Экрис Гари；Митчел Хатчингз Роберт
申请人:Джонсон,Мэтти Энд Ко.,Лимитед (Фирма)；
IPC主号:

专利说明:

e
ABOUT)
with
The invention relates to methods for purifying waste industrial gases and exhaust gases of internal combustion engines from impurities of carbon monoxide and organic compounds and may find application in industries associated with wire enameling, with painting and drying of machine parts, in printing and other industries using organic solvents, as well as in the chemical industry in the vapor-phase oxidation of organic compounds, in the production of ethylene and ethylene oxide, in the operation of washed furnaces and engines combustion it.
A known method of purification of gases from organic substances by burning 1.
However, this method is not always justified due to the need to simultaneously burn the fuel 1.
The closest in technical essence and the achieved result to the proposed method is the purification of industrial waste gases and exhaust gases of internal combustion engines, including passing them through a catalyst containing platinum or palladium or rhodium or ruthenium and a refractory catalytically active metal oxide (I - IX groups of the periodic system of elements on an inert carrier 2.
It is known that, for example, platinum catalysts are stable close to temperatures of at least 750 ° C and are resistant to poisoning in most catalysts, excluding lead and phosphorus.
The initial temperature of the gas stream supplied to the catalytic purification, i.e. ignition temperature, is 230-480s by a known method, i.e. quite high.
The aim of the invention is to reduce the ignition temperatures of impurities during the cleaning process.
The goal is achieved by the method of purification of exhaust and industrial gases from carbon monoxide and organic compounds by passing them through a catalyst containing platinum and a refractory catalytically active metal oxide II - IX groups of the periodic system of elements on an inert carrier, and using a catalyst containing platinum mixed with rhodium or in the form of their alloy at a concentration of rhodium 20-50 May. of their total content, and as an inert carrier, a ceramic material selected from the group including zirconmullite, mullite, i-alumina, silimanite, magnesium silicates, zircon, petalite, spodumene, cordierite, and aluminosilicates.
The catalyst on the carrier, used according to the proposed method of gas cleaning, consists of a refractory oxide deposited on an inert ceramic material and catalytically active metals of platinum and rhodium.
The inert carrier of the cat aggler used is a rigid, porous, cellular refractory ceramic material, such as, for example, ziru equulite, mullite, alpha-alumina, silimanite, magnesium silicates, zircon, petalite, spodumene, cordierite, and silicates. A suitable proprietary product is Torvex, sold by DuPont, and is a refractory honeycomb structure made from llit ceramics.
The refractory catalytically active oxides are 1-50%, preferably 5-30% relative to the total weight of the supported catalyst. These oxides are one or more of the metal oxides H, P and fX of periods of the periodic system of elements that have atomic numbers not exceeding 40.
Platinum and rhodium make up 0.0510% by reference to the total weight of the supported catalyst, preferably 0.5-2.0%.
Externally, the catalyst is a rigid honeycomb structure or blocks with multiple openings or channels. Honeycombs usually occupy almost the entire cross section of a catalytic reactor with a seal between them and the walls to prevent bypassing part of the gas flow. It is convenient to use regularly spaced systems of tightly adjoining units or sequentially spaced separate units for reactors with a large cross-sectional area.
The catalyst units are placed in the reactor so that the overall direction of the cellular channels coincides with the direction of the gas flow through the reactor. Blocks can be / positioned so that the flow of gas through the reactor is radial or transverse with respect to the total flow of gas.
Lreemer 1. To determine ignition temperatures, i.e. inlet temperatures at which the oxidation reactions of impurities "become self-sustaining, as well as for determining the inlet temperatures 5 required for 90% oxidation
impurities, use catgie-eator, states of platinum alloy and rhodium with the content of the latter 35 wt.% and active alumina on torvex. The results are shown in Table. one.
As follows from the table. 1, the ignition temperature of impurities in the gas to be purified, with the exception of hydrogen, is 150-425 s, which is lower than the corresponding values of a known method (230-480 s). For the 90% oxidation of impurities most commonly encountered in practice, temperatures of 150-500 ° C are necessary.
Note 2. A gas containing, in May.%: Methane 1.5, oxygen 3, the rest is nitrogen, with an insignificant amount of oxides of nitrogen and argon is fed to the purification. Use the catalyst, as in example 1, but with a different ratio of platinum and rhodi. Ignition temperatures are determined at a rhodium content of 0-100% of the total metal content. The results are shown in Table. 2
From tab. 2, it follows that the cattoi interval of low ignition temperatures corresponds to a rhodium content of 20–50 wt.% (Optimally 30–40;. Wt.%), An extremely low value is observed at 35 wt.%.
Example 3. Catalyst efficiency was tested in the purification of exhaust gases from a laboratory single-cylinder diesel engine operating indoors. Engine performance is given in Table. 3
The tests are carried out in three operating modes - idle, medium and high loading. The characteristics of exhaust compositions in these modes (average for 10 tests) are given in Table 5. four
When using the idle mode, the exhaust gas temperature of 950 ° C is too low for the catalytic reaction to take place.
Tests show that the catalyst becomes spectacular at 170 ° C and its activity rapidly increases with increasing exhaust gas temperature.
The catalyst is less efficient with respect to the purification of particles of a shaft, however, they are continuously removed from the catalyst during its operation due to catalytic oxidation,
0 therefore the catalyst does not lose its activity.
Example 4. A loop gas of nitric acid production at a pressure of 5.3 kg / cm, containing 3% by volume of oxygen and 2000 hours per million of oxides of nitrogen, into which 1.78% by volume of methane or natural gas is introduced through the catalyst. . The catalyst contains 35% rhodium and 65% platinum
0 on mullite (Torvex).
The ignition temperature is 25 ° C, the oxidation state of methane is 90%.
As follows from the examples, the proposed method of gas cleaning ensures the reduction of the ignition temperature of impurities to 150-425 ° C against 230-480 ° C by a known method.
Table 1
Hydrogen
Carbon dioxide
Benzene
Toluene
Xylene
Alpha pinen
Mesityl oxide
Ethanol
n-heptane
Methylisobutyl ketone
Methyl ethyl ketone
20
150-200 250-300 250-300 250-300 250-300 250-300 250-300 250-300 300-350 300-350
DO1 methylformamide
Ethyl acetate
Methane (air)
Methane (3% Oj / N5}
Thiophene
Pyridine
Chlorbutan
Hydrogen sulphide
Carbon disulfide Ratio Fh: Pt .. in “, 0: 100 5:95 20:80 35:65 50:50 100: 0 i J lIntensity of the T test of the brake, the efficiency of the run of the top Liv, kg / h
0.23
7.5
2.33 11.0
2.81
Continued table. one
350-400 400-450 400-450 400-450 400-450 400-450 450-500 400-425 375-400
33.9
600
96
54.0
1,190
487
52.6
1,170
597 Table The temperature of ignition, with m. "(. 425. 410 330 315 325 400 Table 3 Consumption 1 Air temperature, rev / min exhaust kg / C, C
Note. Dma concentration is expressed in flue
Cartridge units.
Table 4

权利要求:
Claims (1)
[1]
(57) METHOD FOR CLEANING EXHAUST AND INDUSTRIAL GASES from impurities of carbon monoxide and organic compounds by passing them through a catalyst containing platinum and refractory catalytically active metal oxide of groups IX of the periodic system of elements on an inert carrier, characterized in that, in order to reduce the ignition temperature of impurities during the cleaning process, use a catalyst containing platinum mixed with rhodium or their alloy at a concentration of rhodium 20-50 wt.% of their total content, and as an inert carrier nomic material selected from. § a group including zirconmachllite, mullite, oC-alumina, silymanite, magnesium silicates, zircon, petalite, spodumene, cordierite and aluminosilicates.

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同族专利:

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公开号 | 公开日

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NL7013587A|1971-03-18|

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BE756151A|1971-02-15|

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JPS5621645A|1981-02-28|

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ES383629A1|1973-05-01|

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DE2045487A1|1971-03-25|

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JPS5319554B1|1978-06-21|

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NL170375C|1982-11-01|

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CA984125A|1976-02-24|

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DE2045488A1|1971-04-08|

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GB1330841A|1973-09-19|

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SU375830A3|1973-03-23|

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DE2045487C2|1985-05-23|

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NL170809C|1983-01-03|

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FR2061385A5|1971-06-18|

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FR2061384A5|1971-06-18|

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BE756150A|1971-02-15|

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DE2045488C3|1978-10-05|

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DE2045488B2|1978-01-26|

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SU402198A3|1973-10-12|

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法律状态:

优先权:

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申请号 | 申请日 | 专利标题

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GB4554569|1969-09-16|

---