CN1347759A - Fume purifying catalyst and its prepn and application - Google Patents
Fume purifying catalyst and its prepn and application Download PDFInfo
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- CN1347759A CN1347759A CN 01127900 CN01127900A CN1347759A CN 1347759 A CN1347759 A CN 1347759A CN 01127900 CN01127900 CN 01127900 CN 01127900 A CN01127900 A CN 01127900A CN 1347759 A CN1347759 A CN 1347759A
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- purifying catalyst
- fume
- fume purifying
- carrier
- dipping
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Abstract
The fume purifying catalyst consists of CuO, NiO, CoO, MnO2, Cr2O3, BaO, Fe2O3, CaO, gamma-Al2O3 and La2O3, CeO, Pt, Pd, Rh, Ru and other active components; is prepared through the steps of material compounding, liquid compounding, soaking, stoving roasting, reducing, etc.; and is used in catalytic purification of kitchen fume. The catalyst can convert various fume, oil stain and carcinogen into CO2 and water completely. With low catalytic conversion temperature, low cost, complete conversion and no secondary pollution, the catalyst may be used in household, hotal and restaurant.
Description
(1) technical field
The present invention relates to the kitchen oil fume purifying technical field, specifically be meant a kind of fume purifying catalyst and its production and application.
(2) background technology
The fume pollution of catering trade is that a kind of serious environmental is polluted, and is perplexing the construction and the development in many cities and towns for a long time.The oil smoke composition more complicated that cooking food produced, the variation of a series of complexity can take place in general edible oil and food under hot conditions, produce a large amount of thermal oxide catabolites, wherein partially decomposed product is dispersed in the air with the smog form, forms oil smoke.For example, edible oil is heated to 170 ℃ of low smoke that the initial stage decomposition will occur, and along with temperature continues to raise, decomposition rate is accelerated, and when temperature reaches 250 ℃, a large amount of oil smoke can occur.In the food cooking process, the formation approach of oil smoke is mainly: the thermal oxide of the contained lipid of grease and food itself is decomposed; The rice Maillard reaction takes place in carbohydrate, protein, amino acid etc. in the food; Interactional secondary response product between the centre of above-mentioned reaction or the end product.The oil smoke complicated component is done gas-chromatography-mass spectral analysis with oil smoke gas, can measure more than 20 kind of composition, mainly contains aldehyde, ketone, hydrocarbon, aliphatic acid, alcohol, aromatic compound, ester, lactone and heterocyclic compound etc.In addition, also contain carcinogens such as Bap, volatility nitrous acid, heterocyclic amine compound in the oil smoke, as benzo [a] pyrene (Bap), dibenzo [a, h] anthracene (DbahA), benzo [a] anthracene (BaA), dibenzo [a, b] anthracene (DbabA) and benzo [e] pyrene multiple polycyclic aromatic hydrocarbons such as (Bep).Chinese residents have the traditional habit of high-temperature cooking, and the fume pollution that the cooking is produced is very serious.
Kitchen fume processing method traditionally concentrates on the room ventilation always, as establishing methods such as exhaust fan, smoke exhaust in the kitchen.Good ventilation is effectively to lower polluting, but this processing mode does not just add directly being discharged in the atmosphere of processing to the oil smoke of generation in the kitchen, and these oil smoke health of contaminated environment and harmful to human seriously still.At present, it is several that the oil smoke treatment technology of home and abroad mainly contains inertial separation, electrostatic precipitation, filtration and washing etc.Wherein, inertial separation is that the change by airflow direction makes oil mist particles lean on inertia to separate from air-flow, and the required equipment of this technology is simple, and pressure drop is less, but purification efficiency is not high, only is applicable to oil smoke preliminary treatment and the occasion not high to the fume purifying effect requirements; Modes such as two-region electro-deposition or flushing two-region electric precipitation are then adopted in electrostatic precipitation, its principle is when oil smoke enters high voltage electric field, oil mist particles is charged at electric field action equipment, the purification efficiency height of this technology, pressure drop is less, but the pole plate of cleaning equipment is difficulty relatively, and regular maintenance is very complicated, and also has the liquid waste processing problem when adopting douche; It is when oil smoke passes through filter course that filtration then has filter cloth filtration, fiber filter etc., its principle, be removed by effects such as power captures, and this technology purification efficiency height, reliable, pressure drop is big, but the protective effect time of individual layer is short; Washing has Wen's scrubbing tower, spray column etc., it is by the gas-liquid contact oil smoke to be shifted to liquid phase from gas phase, according to the character of cleaning solution, can remove the oil smoke smell simultaneously, but this technology is low to the smoke particle thing purification efficiency of submicron order, and has the handling problem of cleaning solution.Moreover, above-mentioned various technology all exist operating cost height and secondary pollution problems, make it to be difficult to for a long time apply.
(3) summary of the invention
The objective of the invention is to overcome the deficiencies in the prior art part, a kind of fume purifying catalyst and its production and application is provided, utilize this catalyst treatment oil smoke, with low cost, non-secondary pollution, the purification efficiency height, flue gas after being purified can reach national strict emission control standards, and promptly cooking fume discharge standard (trying) is (GWPB5-2000).
A kind of fume purifying catalyst of the present invention, it is characterized in that it is made up of according to mass percent following active component: CuO is 5～25%, and NiO is 5～25%, and CoO is 5～25%, MnO
2Be 4～25%, Cr
2O
3Be 2～6%, BaO is 2～5%, Fe
2O
3Be 2～5%, CaO is 2～5%, γ-Al
2O
3Be 10～40%.Active component can also comprise the oxide of rare earth element ce, La, and its mass percent is: La
2O
3Be 0～10%, CeO is 0～20%.Active component also can comprise precious metal element Pt, Pd, Rh and Ru, and its mass percent is: Pt is 0～1%, and Pd is 0～1%, and Rh is 0～1%, and Ru is 0～1%.
The preparation method of a kind of fume purifying catalyst of the present invention is characterized in that it comprises the steps and process conditions:
First step batching
γ-Al
2O
3Consumption be mass percent γ-Al
2O
3/ carrier=10～15%, the consumption of other active component is according to itself and γ-Al
2O
3Corresponding proportioning convert.
The second step dosing
Water dissolves needed metal nitrate crystal and alumina gel fully respectively, then two kinds of solution is mixed, and makes maceration extract.
The 3rd step dipping and oven dry
Carrier is dipped in the maceration extract, floods after 3～30 minutes, place drying box, dried 1～5 hour down at 100～200 ℃.
In order to make more being adsorbed on more equably on the carrier of active component in the mixed liquor, can adopt the repeatedly method of dipping, promptly can repeatedly repeat above-mentioned dipping, drying course under the same conditions.
The 4th one-step baking
To place high temperature furnace through the carrier after dipping and the oven dry, 300～600 ℃ of following roastings 1～5 hour.
The reduction of the 5th step
Carrier is placed reduction apparatus, purged 10～20 minutes with nitrogen earlier, be heated to 200～400 ℃ then, feed hydrogen and reduced 1～5 hour, it is cooled off naturally, obtain product.
For avoiding blasting, after cooling off naturally, carrier can feed the remaining hydrogen in the nitrogen purging reduction apparatus again.
A kind of fume purifying catalyst of the present invention is applied to the catalytic purification of kitchen fume, and the concentration range of purifying oil fume is 10～1000mg/m
3, purification temperature is 200～500 ℃, oil smoke gas air speed is 5000～25000/h.
The present invention compared with prior art has following outstanding advantage and effect:
1. adopt catalyst provided by the invention to purify kitchen fume, purification efficiency height.Catalyst provided by the invention is applied to fume purifying; oil smoke concentration after the processing reaches or has surpassed the cooking fume discharge standard (No. [2000] 47, environment-development) and cooking fume discharge standard (trying) latest requirement (GWPB5-2000) of State Environmental Protection Administration's issue; non-secondary pollution can directly discharge.Catalyst provided by the invention is to the clean-up effect of oil smoke, can measure in the following way: adopt TH-880IV type microcomputer dust parallel sampling instrument to carry out the oil smoke sampling, carry out quantitative analysis with infrared spectrometer, extract soot gas with isokinetic sampling's method, with cooking fume-collecting in the mist collecting head, the acquisition filter heart of having collected oil smoke is placed polytetrafluoroethylene sleeve with cover, carry out ultrasonic cleaning with carbon tetrachloride as solvent, move into constant volume in the colorimetric cylinder, with the content of determination of infrared spectroscopy oil smoke.Oil smoke removal efficiency test result is as shown in table 1.Table 1
| Oil smoke concentration (mg/m 3) | Removal efficiency (%) | |
| 1. enter the mouth (unprocessed) | ???????82.74 | ????????/ |
| 2. floss hole (300 ℃ of catalyzed conversions) | ????1.47 | ????96.55 |
| 3. enter the mouth (unprocessed) | ????85.29 | ??????/ |
| 4. floss hole (350 ℃ of catalyzed conversions) | ????1.46 | ????98.21 |
2. utilize catalyst provided by the invention to purify kitchen fume, with the Organic Waste Gas Pollution thing, promptly most of organic compound, ammonia, hydrocyanic acid, carbon monoxide etc. are converted into the CO that does not have secondary pollution
2And water, the clean-up effect under 200～500 ℃ just can meet strict emission control standards.The catalytic purification reaction temperature is low, does not produce nitrogen oxide, and is safe to use, even the concentration of oxygen is lower, and also can complete oxidation and be not subjected to the influence of steam.Soot gas is as shown in table 2 in the purified treatment effect by catalyst of the present invention.Table 2
| Treated substance | Operating temperature (℃) | Concentration (mg/m before handling 3) | Concentration (mg/m after the processing 3) |
| Methacrylaldehyde | ????200 | ????1000 | ????＜2 |
| Vegetable oil (peanut oil) | ????350 | ????500 | ????＜2 |
| Carbon monoxide | ????150 | ????4000 | ????＜2 |
3. use catalytic purification provided by the invention and handle oil smoke, the equipment needed thereby compact conformation, volume is less, and the system works noise is low, and the equipment pressure drop is not high, and operation maintenance is convenient and expense is lower, is fit to family and medium and small dining room and uses, and is suitable for face width.
(4) specific embodiment
Embodiment one:
Make carrier (300 hole/cm of hole density with the honeycomb ceramics pottery
2, wall approaches 0.2～0.25mm), gets γ-Al according to 10% of carrier quality
2O
3, and according to 5% CuO, 5% NiO, 5% CoO, 25% MnO
2, 2% Cr
2O
3, 2% BaO, 3% Fe
2O
3, 2% CaO, γ-Al of 40%
2O
3, 10% CeO and 1% Pd the mass percent batching.Be γ-Al by volume
2O
3: the ratio of water=1: 7 is γ-Al
2O
3Dissolving fully, water mixes all dissolvings of all the other batchings then with two kinds of solution simultaneously, makes maceration extract.Carrier flooded 3 minutes in maceration extract after, place drying box,, repeat twice above-mentioned dipping, drying course 100 ℃ of oven dry 1 hour down.Subsequently carrier is placed high temperature furnace 300 ℃ of following roastings 1 hour.Again carrier is placed reduction apparatus, purged 10 minutes with nitrogen earlier, be heated to 200 ℃ then, the hydrogen that fed 1 hour reduces, and it is cooled off naturally, promptly obtains a kind of fume purifying catalyst of the present invention.10 centimetres of catalyst bed layer heights, the about 200Pa of bed pressure drop.Heat the iron pan that fills peanut oil with electric furnace, to the oil boiling.The clarifier that has air exhauster and catalyst is installed above oil cauldron, and catalyst volume is 1.6 liters.The exhaust gas flow of catalyst of flowing through is 65m
3/ hr, air speed 10000/h.No matter still to be removal efficiency all reach concentration of emission and surpass national newest standards.Its concrete data are as shown in table 3.Table 3
| Numbering | Temperature (℃) | Absorbance | Concentration of emission (mg/m 3) | Purification efficiency (%) |
| ????1 | ??1.097 | ????84.61 | ??????0 | |
| ????2 | ????200 | ??0.394 | ????30.67 | ????63.75 |
| ????3 | ????250 | ??0.155 | ????12.33 | ????85.43 |
| ????4 | ????300 | ??0.199 | ????16.11 | ????80.97 |
| ????5 | ????350 | ??0.124 | ????9.86 | ????88.35 |
| ????6 | ????400 | ??0.036 | ????2.91 | ????96.57 |
| ????7 | ????450 | ??0.051 | ????4.39 | ????94.81 |
Embodiment two:
Make carrier with the honeycomb ceramics pottery, geometrical surface is 27cm
2Cm
-3, get γ-Al according to 15% of carrier quality
2O
3, and according to 15% CuO, 10% NiO, 25% CoO, 20% MnO
2, 4% Cr
2O
3, 4% BaO, 4% Fe
2O
3, 3% CaO and γ-Al of 15%
2O
3Mass percent batching.Be γ-Al by volume
2O
3: the ratio of water=1: 10 is γ-Al
2O
3Dissolving fully, water mixes all dissolvings of all the other batchings then with two kinds of solution simultaneously, makes maceration extract.Carrier flooded 30 minutes in maceration extract after, place drying box, at 200 ℃ of oven dry 5 hours down, the above-mentioned dipping of triplicate, drying course.Subsequently carrier is placed high temperature furnace 600 ℃ of following roastings 5 hours.Again carrier is placed reduction apparatus, purged 20 minutes with nitrogen earlier, be heated to 400 ℃ then, the hydrogen that fed 5 hours reduces, it is cooled off naturally, feed nitrogen again and purge remaining hydrogen, promptly obtain a kind of fume purifying catalyst of the present invention.The oil smoke gas air speed 5000/h of catalyst flows through.Under 300 ℃, inlet oil smoke concentration 82mg/m
3Purifying the back exit concentration is 1.47mg/m
3, no matter still to be removal efficiency all reach concentration of emission and surpass national newest standards.
Embodiment three to eight:
Adopt the Preparation of Catalyst condition identical, different catalysts prescription (mass percent) and oil smoke removal efficiency such as table 4 with embodiment two.Table 4
Claims (9)
1. fume purifying catalyst, it is characterized in that it is made up of according to mass percent following active component: CuO is 5～25%, and NiO is 5～25%, and CoO is 5～25%, MnO
2Be 4～25%, Cr
2O
3Be 2～6%, BaO is 2～5%, Fe
2O
3Be 2～5%, CaO is 2～5%, γ-Al
2O
3Be 10～40%.
2. a kind of fume purifying catalyst according to claim 1, the active component that it is characterized in that it can also comprise the oxide of rare earth element ce, La, its mass percent is: La
2O
3Be 0～10%, CeO is 0～20%.
3. a kind of fume purifying catalyst according to claim 1 and 2 is characterized in that its active component can also comprise precious metal element Pt, Pd, Rh and Ru, and its mass percent is: Pt is 0～1%, and Pd is 0～1%, and Rh is 0～1%, and Ru is 0～1%.
4. the preparation method of a fume purifying catalyst is characterized in that it comprises the steps and process conditions:
First step batching
The consumption of alumina gel is mass percent γ-Al
2O
3/ carrier=10～15%, the consumption of other active component is according to itself and γ-Al
2O
3Corresponding proportioning convert.
The second step dosing
Water dissolves needed metal nitrate crystal and alumina gel fully respectively, then two kinds of solution is mixed, and makes maceration extract.
The 3rd step dipping and oven dry
Carrier is dipped in the maceration extract, floods after 3～30 minutes, place drying box, dried 1～5 hour down at 100～200 ℃.
The 4th one-step baking
To place high temperature furnace through the carrier after dipping and the oven dry, 300～600 ℃ of following roastings 1～5 hour.
The reduction of the 5th step
Carrier is placed reduction apparatus, purged 10～20 minutes with nitrogen earlier, be heated to 200～400 ℃ then, feed hydrogen and reduced 1～5 hour, it is cooled off naturally, obtain product.
5. the preparation method of a kind of fume purifying catalyst according to claim 4 is characterized in that dipping process can adopt the repeatedly method of dipping, promptly can repeatedly repeat above-mentioned dipping, drying course under the same conditions.
6. the preparation method of a kind of fume purifying catalyst according to claim 4 is characterized in that after carrier cools off naturally, can feed the remaining hydrogen in the nitrogen purging reduction apparatus again.
7. the preparation method of a kind of fume purifying catalyst according to claim 4 is characterized in that carrier can be a honeycomb ceramic carrier.
8. the described fume purifying catalyst of claim 1 is applied to the catalytic purification of kitchen fume.
9. the application of a kind of fume purifying catalyst according to claim 8, the concentration range that it is characterized in that purifying oil fume is 10～1000mg/m
3, purification temperature is 200～500 ℃, oil smoke gas air speed is 5000～25000/h.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011279001A CN1140343C (en) | 2001-09-28 | 2001-09-28 | Fume purifying catalyst and its prepn and application |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB011279001A CN1140343C (en) | 2001-09-28 | 2001-09-28 | Fume purifying catalyst and its prepn and application |
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| Publication Number | Publication Date |
|---|---|
| CN1347759A true CN1347759A (en) | 2002-05-08 |
| CN1140343C CN1140343C (en) | 2004-03-03 |
Family
ID=4667810
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB011279001A Expired - Fee Related CN1140343C (en) | 2001-09-28 | 2001-09-28 | Fume purifying catalyst and its prepn and application |
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| Country | Link |
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| CN (1) | CN1140343C (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100391598C (en) * | 2006-06-20 | 2008-06-04 | 茂名学院 | NOx storage and reduction catalyst for purifying tail-gas of internal-combustion engine |
| CN102192528A (en) * | 2011-05-25 | 2011-09-21 | 浙江工业大学 | Energy-saving and environment-friendly agricultural kitchen range |
| CN102631933A (en) * | 2011-02-14 | 2012-08-15 | 中国石油化工股份有限公司 | Catalyst for removing NO in smoke and preparation method thereof |
| CN103785276A (en) * | 2014-01-24 | 2014-05-14 | 北京航空航天大学 | Method and device for purifying catering oil smoke by utilizing synergistic effect of low temperature plasma and catalysts |
| CN105222199A (en) * | 2015-11-14 | 2016-01-06 | 无锡清杨机械制造有限公司 | A kind of smoke exhaust ventilator with air-cleaning function |
| CN107029737A (en) * | 2017-05-24 | 2017-08-11 | 内蒙古科技大学 | A kind of mischmetal denitrating catalyst and preparation method thereof |
| CN109595624A (en) * | 2017-09-30 | 2019-04-09 | 江苏瑞丰科技实业有限公司 | A kind of separation of oil smoke and gas cleaning processing technique |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1268924C (en) * | 2004-04-30 | 2006-08-09 | 何宗彦 | Onsite oil smoke concentration detecting method and onsite detector for oil smoke concentration |
-
2001
- 2001-09-28 CN CNB011279001A patent/CN1140343C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100391598C (en) * | 2006-06-20 | 2008-06-04 | 茂名学院 | NOx storage and reduction catalyst for purifying tail-gas of internal-combustion engine |
| CN102631933A (en) * | 2011-02-14 | 2012-08-15 | 中国石油化工股份有限公司 | Catalyst for removing NO in smoke and preparation method thereof |
| CN102192528A (en) * | 2011-05-25 | 2011-09-21 | 浙江工业大学 | Energy-saving and environment-friendly agricultural kitchen range |
| CN103785276A (en) * | 2014-01-24 | 2014-05-14 | 北京航空航天大学 | Method and device for purifying catering oil smoke by utilizing synergistic effect of low temperature plasma and catalysts |
| CN103785276B (en) * | 2014-01-24 | 2016-04-27 | 北京航空航天大学 | The synergy of low temperature plasma and catalyst is utilized to purify the method and apparatus of kitchen fumes |
| CN105222199A (en) * | 2015-11-14 | 2016-01-06 | 无锡清杨机械制造有限公司 | A kind of smoke exhaust ventilator with air-cleaning function |
| CN107029737A (en) * | 2017-05-24 | 2017-08-11 | 内蒙古科技大学 | A kind of mischmetal denitrating catalyst and preparation method thereof |
| CN109595624A (en) * | 2017-09-30 | 2019-04-09 | 江苏瑞丰科技实业有限公司 | A kind of separation of oil smoke and gas cleaning processing technique |
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| Publication number | Publication date |
|---|---|
| CN1140343C (en) | 2004-03-03 |
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