CN2738871Y - Biological mud oil-fume purifying apparatus - Google Patents

Biological mud oil-fume purifying apparatus Download PDF

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Publication number
CN2738871Y
CN2738871Y CNU2004201139969U CN200420113996U CN2738871Y CN 2738871 Y CN2738871 Y CN 2738871Y CN U2004201139969 U CNU2004201139969 U CN U2004201139969U CN 200420113996 U CN200420113996 U CN 200420113996U CN 2738871 Y CN2738871 Y CN 2738871Y
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CN
China
Prior art keywords
mud
oil
fume
purifying apparatus
biology
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Expired - Fee Related
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CNU2004201139969U
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Chinese (zh)
Inventor
廖雷
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Guilin University of Technology
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Guilin University of Technology
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Priority to CNU2004201139969U priority Critical patent/CN2738871Y/en
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Publication of CN2738871Y publication Critical patent/CN2738871Y/en
Anticipated expiration legal-status Critical
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

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  • Activated Sludge Processes (AREA)

Abstract

The utility model discloses a biological mud oil-fume purifying apparatus, comprising a biology mud ditch (4), a dehydration column (7), a gas-collecting channel (1), a suction blower (9) and a temperature controller (10). The biology mud ditch (4) is made of the non-corrodible steel or the ferroconcrete, and the bottom of the biology mud ditch(4) is uniformly provided with a jet aeration pipes (3) which jets the biology mud (5) which inoculates the good microorganisms into the biology mud ditch (4). When the oil smoke passes the biology mud layer in the apparatus, the contamination is adsorbed by the mud and degraded by the microorganisms, realizing the separation of the oil and the water and achieving the discharge standard. The oil-fume purifying apparatus collects the collecting fume system, the processing system and the controlling system in one, to form the compact conformation and reduce the taken space. The oil-fume purifying apparatus has high treatment efficiency. The eliminating rate of the oil reaches 95%, and the eliminating rate of the peculiar smell reaches 90%. The oil-fume purifying apparatus has high anti-interference capability, high anti-impact strength and low energy consumption, which can make use of the heat energy of the fume to automatically adjust the reaction temperature. The utility model has the advantages of high price ratio, convenient installing and debugging, safe operating and no secondary pollution.

Description

Biological mud fume purifier of fume
Technical field
The utility model relates to a kind of kitchen oil fume purifying device, particularly relates to a kind of biological mud fume purifier of fume.
Background technology
Oil smoke is a kind of gaseous contaminant that people produce in the cooking food process, is edible oil and the food volatile matter at high temperature and the mixture of condensate aerosol and aqueous vapor, indoor dusty gas thereof.Compare with industrial smoke, oil content content height in the oil flue waste gas, viscosity is big, also has peculiar smell.On form, contain liquid, solid, gas three-phase pollutant simultaneously.Its chemical composition mainly is an organic matter, and kind is more, and is water-soluble relatively poor.
At present, the main industrial ventilation cleaner that adopts is handled oil smoke on the market, main type has mechanical type, filtering type, electrostatic, wet type, combined type etc., and low, the instant effect of these equipment development costs has been obtained certain effect aspect the pollution of oil smoke aerosol in control food and drink oil smoke.But because the greasy dirt viscosity that is captured down is big, strong adhesion, cause the resistance of separation equipment to increase, filtrate can not clean and utilize, isolation of purified equipment stops up, cause the action time of equipment continuous effective short, safeguard cleaning and running expense height, be easy to a difficult problem such as secondary pollution, and these equipment are generally not good to escaping gas treatment effect in the oil smoke; Abroad based on the physico-chemical process of thermal oxide burning method and catalytic purification method owing to being difficult to reduce cost significantly and safety issue restricts it and applies.There is following problem in existing specifically fume treating device: the effective storage life of (1) cleaning equipment is short.Most every month or need clean once half a year, especially outstanding for electrostatic separation equipment and this situation of filter plant.(2) some cleaning equipment complex structures efficiently, Operation and maintenance are had relatively high expectations, as electrostatic precipitation, isolated by filtration, wet scrubbing or the like.(3) most of cooking fume control equipments are only paid attention to the removal of oil smoke droplet, and are that the removal of peculiar smell is not included.And the resident is very big to the penetrating odor suggestion of the outer mist extractor of the catering trade at present.(4) efficient cleaning equipment cost and operating cost are higher, equipment cost mainly is meant apparatus body cost and material cost (the disposable filtrate used as filter plant), and operating cost comprises maintenance cost, cleaning expense etc. (cleaning oil pollution and the maintenance that separate with isolated by filtration and Wen as electrostatic separation).(5) research of home-use cooking fume cleaner seldom mainly utilizes the mechanical type fume exhausting fan directly to efflux at present, though family kitchen oil smoke discharge amount is few, because its One's name is legion, drain time is concentrated, and the total emissions amount still can not be ignored.Therefore, the characteristics big according to oil smoke viscosity are used new waste gas pollution control and treatment theoretical principle, and it is a privileged direction that the special-purpose oil smoke of development of new is administered.
Summary of the invention
The purpose of this utility model is to provide a kind of practicality, outer cooking fume purifier easily, oil smoke gas is through the biological mud layer in the device, pollutant is adsorbed and microbial degradation by mud, realizes Oil-gas Separation and qualified discharge, solves the outer mist extractor problem that disturbs residents.
The utility model is achieved in that biological mud ditch mixes earth by stainless steel, plastics or reinforcing bar and makes, the jet-flow aeration pipe is evenly arranged in biological mud ditch bottom, places groove approximately to 2/3rds groove eminences [liquid level gauge demonstration] in the active bio mud of having inoculated superior microorganism; Air inlet pipe connects gas skirt and is fixed in groove and covers with the jet-flow aeration pipe and link to each other, and dehydrating tower is fixed on groove and covers by being connected and fixed device, and temperature controller links to each other by magnetic valve with water inlet pipe, and water inlet pipe covers by being bolted to groove, and bottom land has mud discharging mouth; Air-introduced machine is installed on poor covering, and links to each other with dehydrating tower by air entraining pipe; The sensor of temperature controller stretches in the biological mud.
Characteristics of the present utility model are biological mud ditch, it is different with the operation principle of existing fume purifier of fume, the former is the organic assembling of biological and materialization principle, the latter only is physical principle or the principles of chemistry and simple combination thereof, biological mud is the activated sludge of having inoculated superior microorganism, oil flue waste gas enters biological mud layer in the jet-flow aeration mode, pollutants such as oil content are at first separated from gas by effects such as activated sludge absorption, absorptions, play biochemical reaction with microorganism then and generate small-molecule substance (CO 2, H 2O etc.), some difficult degradation things form the excess sludge discharge with microbial metabolic products.Be provided with the jet-flow aeration pipe, mud discharging mouth, water inlet and attemperating unit etc. in the biological mud ditch.Temperature control system can set up temperature bound (20 ℃~35 ℃) on their own, and inflow links to each other with attemperating unit, temperature surpass the upper limit then automatically water inlet be lower than lower limit and then stop into water.
The beneficial effects of the utility model are, collection collection cigarette, processing are one with control system, and compact conformation takes up an area of less; The treatment effeciency height, the oil content clearance can reach 95%, and the peculiar smell clearance can reach 90%; Antijamming capability is strong; Excellent in cushion effect; Energy consumption is low, can utilize the heat energy auto-control reaction temperature of flue gas self; The cost performance height.Installation and Debugging convenience, security of operation, non-secondary pollution.
Description of drawings
Fig. 1 is the utility model flow chart.
Fig. 2 is the utility model side view.
Reference numeral: the 1-gas skirt, the 2-air inlet pipe, 3-jet-flow aeration pipe, the biological mud ditch of 4-, the biological mud of 5-, 6-is connected and fixed device, the 7-dehydrating tower, 8-induced duct, 9-air-introduced machine, 10-temperature controller, 11-magnetic valve, the 12-water inlet pipe, 13-liquid level gauge, 14-sensor, 15-mud discharging mouth, 16-groove lid.
The specific embodiment
Below in conjunction with drawings and Examples the utility model is further specified.
As shown in Figure 2, biological mud ditch (4) is made by stainless steel, and jet-flow aeration pipe (3) is evenly arranged in the bottom, places groove approximately to 2/3rds groove eminences [liquid level gauge (13) demonstration] in the active bio mud (5) of having inoculated superior microorganism.Air inlet pipe (2) connection gas skirt (1) is fixed in groove lid (16) and upward links to each other with jet-flow aeration pipe (3), dehydrating tower (7) is fixed on the groove lid (16) by being connected and fixed device (6), temperature controller (10) links to each other by magnetic valve (11) with water inlet pipe (12), water inlet pipe (12) is by being bolted on the groove lid (16), and bottom land has mud discharging mouth (15); Gas skirt (1) is installed on kitchen range top top, and air-introduced machine (9) is installed on poor lid (16) and goes up and install shockproof and noise-stop device, and links to each other with dehydrating tower (7) by air entraining pipe (8); After connecting power supply, oil smoke and part air are under suction function, be inhaled into gas skirt (1), quicken to enter jet aeration tube (3) ejection in the groove then, fully contact with biological mud (5), carry out material and heat transmission, after the realization Oil-gas Separation, gas exports discharge through air-introduced machine (9) after entering dehydrating tower (7) dehydration.Simultaneously, the sensor (14) of temperature controller (10) stretches in the biological mud (5), can set up temperature bound (30 ℃~35 ℃) on their own, and temperature surpasses then water inlet automatically of the upper limit in groove, is lower than lower limit until temperature and then stops into water.To the preceding discharge section mud to three of start in second day/two groove eminences.

Claims (2)

1, a kind of biological mud fume purifier of fume, comprise gas skirt (1), air inlet pipe (2), air-introduced machine (9), it is characterized in that evenly layout jet-flow aeration pipe (3) of biological mud ditch (4) bottom, place groove approximately to 2/3rds groove eminences [liquid level gauge (13) demonstration] in the active bio mud (5) of having inoculated superior microorganism, air inlet pipe (2) connection gas skirt (1) is fixed in groove lid (16) and upward links to each other with jet-flow aeration pipe (3), dehydrating tower (7) is fixed on the groove lid (16) by being connected and fixed device (6), temperature controller (10) links to each other by magnetic valve (11) with water inlet pipe (12), water inlet pipe (12) is by being bolted on the groove lid (16), and bottom land has mud discharging mouth (15); Air-introduced machine (9) is installed on the poor lid (16), and links to each other with dehydrating tower (7) by air entraining pipe (8); The sensor (14) of temperature controller (10) stretches in the biological mud (5).
2, biological mud fume purifier of fume as claimed in claim 1 is characterized in that described biological mud ditch (4) mixes earth by stainless steel, plastics or reinforcing bar and makes.
CNU2004201139969U 2004-11-05 2004-11-05 Biological mud oil-fume purifying apparatus Expired - Fee Related CN2738871Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2004201139969U CN2738871Y (en) 2004-11-05 2004-11-05 Biological mud oil-fume purifying apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2004201139969U CN2738871Y (en) 2004-11-05 2004-11-05 Biological mud oil-fume purifying apparatus

Publications (1)

Publication Number Publication Date
CN2738871Y true CN2738871Y (en) 2005-11-09

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Application Number Title Priority Date Filing Date
CNU2004201139969U Expired - Fee Related CN2738871Y (en) 2004-11-05 2004-11-05 Biological mud oil-fume purifying apparatus

Country Status (1)

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CN (1) CN2738871Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101975746A (en) * 2010-09-07 2011-02-16 桂林理工大学 Method for determining rate constant for micro-biological degradation of restaurant oil smoke pollutants
CN103920393A (en) * 2014-04-22 2014-07-16 桂林理工大学 Treatment method for performing solid phase catalytic oxidation on cooking oil fume through camellia shell carbon-fenton-like reagent

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101975746A (en) * 2010-09-07 2011-02-16 桂林理工大学 Method for determining rate constant for micro-biological degradation of restaurant oil smoke pollutants
CN101975746B (en) * 2010-09-07 2012-02-15 桂林理工大学 Method for determining rate constant for micro-biological degradation of restaurant oil smoke pollutants
CN103920393A (en) * 2014-04-22 2014-07-16 桂林理工大学 Treatment method for performing solid phase catalytic oxidation on cooking oil fume through camellia shell carbon-fenton-like reagent
CN103920393B (en) * 2014-04-22 2016-04-06 桂林理工大学 The processing method of oil-tea camellia husks charcoal-Fenton-type reagent solid catalysis oxidation kitchen fumes

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C19 Lapse of patent right due to non-payment of the annual fee
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