CN106322476A - Kitchen fume purification and waste heat recovery and utilization integrated device - Google Patents
Kitchen fume purification and waste heat recovery and utilization integrated device Download PDFInfo
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- CN106322476A CN106322476A CN201610927831.2A CN201610927831A CN106322476A CN 106322476 A CN106322476 A CN 106322476A CN 201610927831 A CN201610927831 A CN 201610927831A CN 106322476 A CN106322476 A CN 106322476A
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24C—DOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
- F24C15/00—Details
- F24C15/20—Removing cooking fumes
- F24C15/2035—Arrangement or mounting of filters
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24H—FLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
- F24H4/00—Fluid heaters characterised by the use of heat pumps
- F24H4/02—Water heaters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B30/00—Heat pumps
- F25B30/02—Heat pumps of the compression type
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/80—Type of catalytic reaction
- B01D2255/802—Photocatalytic
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0275—Other waste gases from food processing plants or kitchens
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/12—Hot water central heating systems using heat pumps
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- Environmental & Geological Engineering (AREA)
- Combustion & Propulsion (AREA)
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Abstract
The invention provides a kitchen fume purification and waste heat recovery and utilization integrated device, and belongs to the technical field of kitchen air adjustment and heat recovery and utilization. A fume purification system comprises an exhaust fan, a fume inertia separation pipe segment, an ultraviolet light fume catalysis pipe segment, a fume electrostatic precipitation pipe segment, a fume activated carbon adsorption pipe segment, a first draught fan and a fume pipe segment evaporator, all of which are connected in sequence. A waste heat recovery system comprises a cooking range segment evaporator, a compressor, a throttling device and a condenser. According to the device, the purification efficiency can be improved, and fume contaminants are fully decomposed and recovered; through the application of an air filter device and a heat pump, on the premise of saving energy, the quality of indoor air of a kitchen is improved, and comfort is enhanced; through a waste heat recovery part and the application of the heat pump, waste heat in the kitchen is fully recovered and utilized, the heat is stored and reasonably utilized through a phase change water tank, and energy is saved; and the kitchen fume purification efficiency is improved, and the harm caused by fumes to people and the environment is reduced.
Description
Technical field
The invention belongs to air in kitchen regulation and heat recovery and utilization technical field, be specifically related to a kind of kitchen oil fume purifying
With heat recovery integrated apparatus.
Background technology
In recent years, the attention degree of living environment is improved by people day by day, and indoor environment has become focus of concern, with
The raising day by day of expanding economy and living standards of the people, kitchen flue gas problem has become a focus being concerned by people, more
Carrying out the most people and come to realise the kitchen flue gas harmful effect to indoor environment, kitchen flue gas is primarily referred to as kitchen operation and produces
Deep fat flue gas, these flue gases are even more serious to the harm of people to the hazard ratio medicated cigarette of human body.
World oil crisis constantly highlights, and combustion gas becomes important energy-conservation topic as non-renewable energy resources, how to save
The use of combustion gas, the utilization rate improving combustion gas becomes the focus of concern.How in the design in kitchen, to improve it further energy-conservation
Performance, is possible not only to make people directly be benefited from saving combustion gas, and effectively utilizing and combustion gas resource for combustion gas resource
Protection all have important practical significance.In kitchen, the utilization ratio of heat becomes energy-conservation important indicator, common stove
The capacity usage ratio of stove is at 55%-60%, and range hood also discharges high-temperature gas, if this part surplus can reclaim profit again
With, the saving to the energy has great meaning.
Summary of the invention
In order to solve the problems referred to above that prior art exists, the invention provides a kind of kitchen oil fume purifying and waste heat recovery
Utilize integrated apparatus.
To achieve these goals, the present invention provides following technical scheme: a kind of kitchen oil fume purifying and waste heat recovery are sharp
With integrated apparatus, including lampblack purifying system and residual neat recovering system；
Described lampblack purifying system includes that the exhaust fan being sequentially connected with, oil smoke inertial separation pipeline section, ultraviolet light oil smoke are catalyzed
Pipeline section, oil smoke electrostatic precipitation pipeline section, oil smoke activated carbon adsorption pipeline section, the first blower fan and oil smoke pipeline section vaporizer, described waste heat returns
Receipts system includes cooking stove section vaporizer, compressor, throttling arrangement and condenser, and described oil smoke inertial separation pipeline section uses inertia to divide
Purifying oil smoke from method, described ultraviolet light oil smoke catalysis pipeline section uses ultraviolet catalytic method to purify oil smoke, described
Oil smoke electrostatic precipitation pipeline section uses electrostatic high-pressure process of cleaning to purify oil smoke, and described oil smoke activated carbon adsorption pipeline section uses to be inhaled
Oil smoke is purified by attached method；
Oil smoke enters described oil smoke inertial separation pipeline section by described exhaust fan, and described oil smoke inertial separation pipeline section removes institute
Stating big smoke particle in oil smoke, described oil smoke carries out pretreatment and obtains primary oil flue gas, described primary oil flue gas enters described
Ultraviolet light oil smoke catalysis pipeline section, the grease molecules in described primary oil flue gas is aoxidized by described ultraviolet light oil smoke catalysis pipeline section
And remove fine particle aerosol therein and obtain two grades of cooking fumes, described two grades of cooking fumes enter described high-pressure electrostatic precipitation pipe
Section, carries out three grades of cooking fumes of oil smoke isolated, described three grades of cooking fumes in the highfield of described high-pressure electrostatic precipitation pipeline section
Enter described oil smoke activated carbon adsorption pipeline section and described three grades of cooking fumes are filtrated to get level Four cooking fume, described level Four oil smoke
Gas is sent into described oil smoke pipeline section vaporizer by described first blower fan, when described level Four cooking fume is by described oil smoke pipeline section vaporizer
Carrying out heat exchange with the coil pipe in described oil smoke pipeline section vaporizer, after heat exchange, the working medium in described oil smoke pipeline section vaporizer is vaporized into
It is the first low temperature low pressure gas, and becomes low-temperature oil flue gas after described level Four cooking fume heat exchange；
Cooking stove high ambient temperatures gas when described cooking stove section vaporizer and work carries out heat exchange, in described cooking stove section vaporizer
The working medium heat absorption vaporization in portion, is vaporized into the second low temperature low pressure gas after heat exchange, described compressor absorbs from described oil smoke pipeline section
Second low temperature low pressure gas of the first low temperature low pressure gas of vaporizer and described cooking stove section vaporizer also compresses it into high temperature
Gases at high pressure, described high temperature and high pressure gas is discharged into described condenser again, and described high temperature and high pressure gas is put in described condenser
Heat is also condensed into highly pressurised liquid, then through the cold-producing medium that the throttling of described throttling arrangement is low-pressure low-temperature, again goes into described oil smoke
Pipeline section vaporizer and the heat absorption vaporization of described cooking stove section vaporizer；
Cold water enters described condenser from cold water oral siphon road, and is formed with high temperature and high pressure gas heat exchange in described condenser
Hot water, described hot water is discharged from hot water effluent's pipeline.
Preferably, also include that air handling system, described air handling system include that the air inlet inertia being sequentially connected with divides
From section, air electrostatic dedusting section, the first air activated carbon adsorption pipeline section, the second blower fan, air-treatment vaporizer and air outlet, enter
Air port inertial separation section uses inertial separation method to purify sucking air, and described air electrostatic dedusting section uses electrostatic high-pressure
Process of cleaning purifies sucking air, and described first air activated carbon adsorption pipeline section uses absorption method to carry out only sucking air
Change；
Air is entered described air electrostatic dedusting section by described air inlet inertial separation section to carry out being electrolysed dedusting, after dedusting
Air carries out filtration treatment by described first air activated carbon adsorption pipeline section, is sent by described second blower fan through filtered air
Entering described air-treatment vaporizer, air is by during described air-treatment vaporizer inside and in described air-treatment vaporizer
Coil pipe carries out heat exchange, and after heat exchange, the vaporization of the working medium in described air-treatment vaporizer becomes the 3rd low temperature low pressure gas, and enters
Becoming Cryogenic air after entering the air heat-exchange of described air-treatment vaporizer, Cryogenic air is fed to kitchen through described air outlet
Space；
Described compressor absorbs from the 3rd low temperature low pressure gas of described air-treatment vaporizer with from described oil smoke
First low temperature low pressure gas of pipeline section vaporizer and from the second low temperature low pressure gas of described cooking stove section vaporizer and pressed
Shorten high temperature and high pressure gas into.
Preferably, described air handling system also includes the second air activated carbon adsorption pipeline section, the 3rd blower fan and air quantity control
Making sheet, described second air activated carbon adsorption pipeline section uses absorption method to purify sucking air；
Air is entered the second air activated carbon adsorption pipeline section by described amount panel and carries out filtration treatment, through the sky filtered
Gas is delivered to described air outlet by described 3rd blower fan, enters kitchen space by described air outlet.
Preferably, described residual neat recovering system also includes that filter, described filter are arranged on described cold water oral siphon road
On.
Preferably, described residual neat recovering system also includes water tank, and described water tank passes through described hot water effluent's pipeline with described
Condenser connects.
Preferably, it is provided with phase-change material in described water tank.
Preferably, described phase-change material is expanded graphite/paraffin composite phase change material.
Kitchen oil fume purifying and heat recovery integrated apparatus that the present invention provides pass through inertial separation method, ultraviolet light
The composite oil smoke cleaning part that catalysis method, electrostatic high-pressure process of cleaning, absorption method combine can improve purification efficiency, fully decomposes
Reclaim pollutants from cooking fume, remove oil smoke abnormal smells from the patient, strengthen kitchen indoor environment and reduce the oil smoke pollution for air；Pass through air
Regulation part, uses air filter and heat pump, on the premise of saving the energy, improves kitchen indoor air quality, strengthens
Comfortableness；By waste heat recovery part, use heat pump, fully reclaim the waste heat in kitchen and be used, by phase transformation water tank
Carry out heat storing Appropriate application, save the energy.Improve kitchen oil fume purifying efficiency, reduce oil smoke and human and environment is caused
Harm；Improve kitchen indoor air environment, strengthen kitchen comfortableness；Improve the utilization rate of the energy in kitchen, reduce energy
Loss, saves the energy, fume purifying, air in kitchen regulation, kitchen residual heat is reclaimed, and green reasonably combines.
Accompanying drawing explanation
Kitchen oil fume purifying that Fig. 1 provides for the embodiment of the present invention and the structural representation of heat recovery integrated apparatus
Figure；
Fig. 2 is the structural representation of water tank in this device.
In the present embodiment, the implication of each labelling is as described below:
1: exhaust hood 2: oil smoke inertial separation pipeline section 3: ultraviolet light oil smoke catalysis pipeline section
4: oil smoke electrostatic precipitation pipeline section 5: oil smoke activated carbon adsorption pipeline section 6: the first blower fan
7: oil smoke pipeline section vaporizer 8: cooking stove section vaporizer 9: compressor 10: throttling arrangement
11: condenser 12: water tank 13: filter 14: air outlet
15: Boiler pressure control plate 16: cooking stove 17: cold water oral siphon road 18: hot water effluent's pipeline
19: phase-change material 20: discharge pipe line
2-1: air inlet inertial separation section 4-1: air electrostatic dedusting section
5-1: the first air activated carbon adsorption pipeline section the 5-2: the second air activated carbon adsorption pipeline section
6-1: the second blower fan the 6-2: the three blower fan
7-1: air-treatment vaporizer
Detailed description of the invention
Below in conjunction with the accompanying drawings, the detailed description of the invention of the present invention is further described.Following example are only used for more
Clearly demonstrate technical scheme, and can not limit the scope of the invention with this.
Embodiment 1
Present embodiments provide a kind of kitchen oil fume purifying and heat recovery integrated apparatus, such as Fig. 1 and Fig. 2 institute
Showing, including lampblack purifying system and residual neat recovering system, lampblack purifying system includes exhaust fan 1, the oil smoke inertia being sequentially connected with
Separate pipeline section 2, ultraviolet light oil smoke catalysis pipeline section 3, oil smoke electrostatic precipitation pipeline section 4, oil smoke activated carbon adsorption pipeline section the 5, first blower fan 6
With oil smoke pipeline section vaporizer 7, residual neat recovering system includes cooking stove section vaporizer 8, compressor 9, throttling arrangement 10 and condenser 11,
In the present embodiment, throttling arrangement 10 is conventional choke valve.Oil smoke inertial separation pipeline section 2 uses inertial separation method to carry out oil smoke only
Changing, ultraviolet light oil smoke catalysis pipeline section 3 uses ultraviolet catalytic method to purify oil smoke, and oil smoke electrostatic precipitation pipeline section 4 uses quiet
Oil smoke is purified by electricity high-pressure dust-cleaning method, and oil smoke activated carbon adsorption pipeline section 5 uses absorption method to purify oil smoke.
In the present embodiment, when operation principle and the flow process of lampblack purifying system are specifically, collected kitchen work by exhaust hood 1
The soot gas produced, oil smoke enters oil smoke inertial separation pipeline section 2 by exhaust fan 1, uses inertial separation method to process oil herein
Smog, be oil fume by grid time by change airflow direction so that oil fume granule by inertia with collision from air-flow
Separate, flow into oil groove, this pipeline section purification efficiency the highest (about 50%～70%), be suitable for pretreatment, oil smoke inertial separation
Pipeline section 2 removes big smoke particle in fume eliminating, oil smoke carries out pretreatment and obtains primary oil flue gas, and primary oil flue gas enters ultraviolet light
Oil smoke catalysis pipeline section 3, ultraviolet light oil smoke catalysis pipeline section 3 uses the special Burdick lamp of 185nm by the grease molecules in one-level oil smoke
Chain cuts off, and forms little grease molecules, and the most this ultraviolet light produces ozone after reacting with the oxygen in air, and ozone is by little oils and fats
Molecular oxidation, generates water and carbon dioxide and trace white powder, and the Organic substance in oil smoke is aoxidized by photodissociation, the abnormal flavour in flue
Eliminating the most therewith, obtain two grades of cooking fumes, two grades of cooking fumes enter high-pressure electrostatic precipitation pipeline section 4, and two grades of cooking fumes are by height
During pressure electrostatic precipitation pipeline section 4, by 220v voltage by transformator transformation to volts up to ten thousand, the most rectified device is converted into unidirectional current,
Constituting a highfield between two-plate, arrive dust collecting electrode after smoke particle is electrically charged, oil smoke flows down along pole plate, locates after collection
Reason, thus reach the purpose that oil smoke separates, obtain three grades of cooking fumes.Three grades of cooking fumes enter oil smoke activated carbon adsorption pipeline section 5, oil
Being provided with high surface area porous solid absorption thing in cigarette activated carbon adsorption pipeline section 5, three grades of cooking fumes are by oil smoke activated carbon
Filter pipeline section 5 time with high surface area porous solid absorption thing (such as activated carbon) joint so that it is in one or more components
Under the molecular attraction of surface of solids lack of equilibrium or the effect of chemical bond force, mutually collision, intercept, separate from air and
Absorption, at the surface of solids, is purified and is filtrated to get level Four cooking fume, and soot gas can go through oil smoke inertial separation pipeline section 2
Except big smoke particle, oil smoke is carried out pretreatment, enter ultraviolet light oil smoke catalysis pipeline section 3 and can aoxidize grease molecules and be formed smelly
Oxygen, goes to eliminate the unusual smell, and entering, high-pressure electrostatic precipitation pipeline section 4 removing aerocolloidal to fine particle is very competent, oil smoke activated carbon
Absorption pipeline section 5 carries out last filtration as the protective measure of vaporizer 7 front end to cooking fume, and four combinations mutually make up not
Foot, excellent, shortens the later maintenance cycle.
Level Four cooking fume is sent into oil smoke pipeline section vaporizer 7 by the first blower fan 6, and level Four cooking fume passes through oil smoke pipeline section vaporizer
Carrying out heat exchange with the coil pipe in oil smoke pipeline section vaporizer 7 when 7, after heat exchange, the vaporization of the working medium in oil smoke pipeline section vaporizer 7 becomes
First low temperature low pressure gas, and after level Four cooking fume heat exchange, become low-temperature oil flue gas, low-temperature oil flue gas is at oil smoke pipeline section
Carrying out heat exchange with heating agent in vaporizer 7, and do not contact, the oil smoke pipeline section vaporizer 7 after heat exchange is exhausted from system, or profit again
With.
Inertial separation method, electrostatic high-pressure process of cleaning, absorption method and ultraviolet catalytic method are carried out reasonable combination by the present embodiment,
Owing to ultraviolet catalytic method is the highest to the requirement of pipeline, so being used alone relatively difficult, the present embodiment have selected ultraviolet light and urges
Change method and former three compound use, learn from other's strong points to offset one's weaknesses, reach the best effect of purifying oil fume.
In the present embodiment, operation principle and the flow process of residual neat recovering system are specifically, when cooking stove section vaporizer 8 and work
Cooking stove 16 high ambient temperatures gas carries out heat exchange, the working medium heat absorption vaporization within cooking stove section vaporizer, is vaporized into second low after heat exchange
Temperature low-pressure gas, compressor 9 absorbs from the first low temperature low pressure gas of oil smoke pipeline section vaporizer 7 and cooking stove section vaporizer 8
Second low temperature low pressure gas also compresses it into high temperature and high pressure gas, and high temperature and high pressure gas is discharged into condenser 11 again, and high temperature is high
Calm the anger body heat release be condensed into highly pressurised liquid in condenser 11, then the cold-producing medium being low-pressure low-temperature through throttling arrangement 10 throttling,
Again go into oil smoke pipeline section vaporizer 7 and the heat absorption vaporization of cooking stove section vaporizer 8；
Cold water enters condenser 11 from cold water oral siphon road 17, and forms heat with high temperature and high pressure gas heat exchange in condenser 11
Water, hot water is discharged from hot water effluent's pipeline 18.So iterative cycles work, the heat energy in cooking fume and cooking stove is constantly pumped into
In water, make water temperature gradually rise, finally reach about 55 DEG C, be just suitable for people and use.
Further, this device also includes air handling system, and air handling system includes that the air inlet being sequentially connected with is used to
Property segregation section 2-1, air electrostatic dedusting section 4-1, the first air activated carbon adsorption pipeline section 5-1, the second blower fan 6-1, air-treatment
Vaporizer 7-1 and air outlet 14, air inlet inertial separation section 2-1 uses inertial separation method to purify sucking air, air
Electrostatic precipitation section 4-1 uses electrostatic high-pressure process of cleaning to purify sucking air, and the first air activated carbon adsorption pipeline section 5-1 adopts
Purify sucking air by absorption method；
In the present embodiment, operation principle and the flow process of air handling system are specifically, air is by air inlet inertial separation section
2-1 enters air electrostatic dedusting section 4-1 to carry out being electrolysed dedusting, and the air after dedusting passes through the first air activated carbon adsorption pipeline section 5-
1 carries out filtration treatment, is sent into air-treatment vaporizer 7-1 through filtered air by the second blower fan 6-1, and air is by air
Heat exchange is carried out with the coil pipe in air-treatment vaporizer 7-1, described air-treatment evaporation after heat exchange when reason vaporizer 7-1 is internal
Working medium vaporization in device 7-1 becomes the 3rd low temperature low pressure gas, and becomes after entering the air heat-exchange of air-treatment vaporizer 7--
Cryogenic air, Cryogenic air is fed to kitchen space through air outlet 14；
Compressor 9 absorbs from the 3rd low temperature low pressure gas of air-treatment vaporizer 7-1 and evaporates from oil smoke pipeline section
First low temperature low pressure gas of device 7 and from the second low temperature low pressure gas of cooking stove section vaporizer 8 and to compress it into high temperature high
Calming the anger body, this system is mainly used in using summer.
For adapting to the different times demand to indoor environment, the air handling system of the present embodiment also includes that the second air is lived
Property charcoal absorption pipeline section 5-2, the 3rd blower fan 6-2 and Boiler pressure control plate 15, the second air activated carbon adsorption pipeline section 5-2 uses absorption method
Purify sucking air.
Its operation principle and flow process are particularly as follows: air is entered the second air activated carbon adsorption pipeline section 5-by Boiler pressure control plate 15
2 carry out filtration treatment, are delivered to air outlet 14 through filtered air by the 3rd blower fan 6-2, enter kitchen by air outlet 14 empty
Between.
Air in kitchen adjusting means is as the equipment of a kind of annual regulation indoor environment, and season in summer in winter two can conditioning chamber
Temperature.Boiler pressure control plate 15 is closed, and right-side device is run, and winter, air inlet 2 was closed, and left-side device runs.This device improves kitchen
Room indoor air environment, strengthens kitchen comfortableness；Improve the utilization rate of the energy in kitchen, reduce energy loss, save the energy.
At residual neat recovering system, the present embodiment also also includes that filter 13, filter 13 are arranged on cold water oral siphon road 17
On, filter before cold water is entered condenser 11, extend the service life of condenser 11.
Further, residual neat recovering system also includes water tank 12, and water tank 12 is by hot water effluent's pipeline 18 and condenser 11
Connection, cold water enters condenser 11, and forms hot water with high temperature and high pressure gas heat exchange in condenser 11 from cold water oral siphon road 17,
Hot water is discharged into water tank 12 from hot water effluent's pipeline 18, and can be discharged by the discharge pipe line 20 on water tank 12.
In the present embodiment, being provided with phase-change material 19 in water tank 11, phase-change material 19 is expanded graphite/paraffin composite phase change
Material, phase-change material selects paraffin, and paraffin melting point is 47-64 DEG C, and the temperature distributing disproportionation in melting process is even, and expanded graphite has
There are good absorption property and heat conductivility, so selecting expanded graphite/paraffin composite phase change material.It is provided with phase in water tank 11
Becoming material 19 can also be into other phase-change material, and any satisfactory existing phase-change material can be used in the present embodiment,
The concrete material of phase-change material 19 is not limited by the present embodiment.
In sum, the kitchen oil fume purifying of embodiment offer and heat recovery integrated apparatus, use air source
Heat pump reclaims oil smoke and the waste heat of cooking stove generation, and the heat of recovery is delivered in water, for kitchen, be collected by phase transformation water tank
Waste heat is also stored in phase-change material by hot water.The oil smoke that can solve kitchen processes problem, improves the purification effect of oil smoke
Rate, improves the air quality after purifying, and reduces the harm that human body is caused by oil smoke, reduces atmospheric pollution；By the sky of this device
It is so incensed that to purification filtering and is cooled down, improving indoor air quality in summer, improving kitchen comfortableness；This device simultaneously can
Collect kitchen residual heat, and recycled the domestic hot-water making the use of applicable kitchen.
In the present embodiment, oil smoke pipeline section vaporizer 7, cooking stove section vaporizer 8, compressor 9, throttling arrangement 10 and condenser 11
The air source heat pump of composition, referred to as heat pump.
Embodiment described above is only the present invention preferably detailed description of the invention, and protection scope of the present invention is not limited to this,
Any those of ordinary skill in the art in the technical scope of present disclosure, the technical scheme that can become apparent to
Simple change or equivalence are replaced, and belong to protection scope of the present invention.
Claims (7)
1. a kitchen oil fume purifying and heat recovery integrated apparatus, it is characterised in that include lampblack purifying system and
Residual neat recovering system；
Described lampblack purifying system includes that the exhaust fan (1) being sequentially connected with, oil smoke inertial separation pipeline section (2), ultraviolet light oil smoke are urged
Change pipeline section (3), oil smoke electrostatic precipitation pipeline section (4), oil smoke activated carbon adsorption pipeline section (5), the first blower fan (6) and the evaporation of oil smoke pipeline section
Device (7), described residual neat recovering system includes cooking stove section vaporizer (8), compressor (9), throttling arrangement (10) and condenser (11),
Described oil smoke inertial separation pipeline section (2) uses inertial separation method to purify oil smoke, described ultraviolet light oil smoke catalysis pipeline section (3)
Using ultraviolet catalytic method to purify oil smoke, described oil smoke electrostatic precipitation pipeline section (4) uses electrostatic high-pressure process of cleaning to oil
Cigarette purifies, and described oil smoke activated carbon adsorption pipeline section (5) uses absorption method to purify oil smoke；
Oil smoke enters described oil smoke inertial separation pipeline section (2), described oil smoke inertial separation pipeline section (2) by described exhaust fan (1)
Removing big smoke particle in described oil smoke, described oil smoke carries out pretreatment and obtains primary oil flue gas, described primary oil flue gas enters
Entering described ultraviolet light oil smoke catalysis pipeline section (3), described ultraviolet light oil smoke catalysis pipeline section (3) is by the oils and fats in described primary oil flue gas
Molecule carries out aoxidizing and remove fine particle aerosol therein and obtains two grades of cooking fumes, and described two grades of cooking fumes enter described height
Pressure electrostatic precipitation pipeline section (4), carries out three grades of oil smoke of oil smoke isolated in the highfield of described high-pressure electrostatic precipitation pipeline section (4)
Gas, described three grades of cooking fumes enter described oil smoke activated carbon adsorption pipeline section (5), and described oil smoke activated carbon adsorption pipeline section (5) is to institute
Stating three grades of cooking fumes and carry out being filtrated to get level Four cooking fume, described level Four cooking fume is sent into described oil by described first blower fan (6)
Smoke pipe section vaporizer (7), described level Four cooking fume by described oil smoke pipeline section vaporizer (7) time with described oil smoke pipeline section vaporizer
(7) coil pipe in carries out heat exchange, and after heat exchange, the vaporization of the working medium in described oil smoke pipeline section vaporizer (7) becomes the first low-temp low-pressure
Gas, and become low-temperature oil flue gas after described level Four cooking fume heat exchange；
Cooking stove (16) high ambient temperatures gas when described cooking stove section vaporizer (8) and work carries out heat exchange, and described cooking stove section is evaporated
The working medium heat absorption vaporization that device (8) is internal, is vaporized into the second low temperature low pressure gas after heat exchange, described compressor (9) absorbs from institute
State the first low temperature low pressure gas and second low temperature low pressure gas of described cooking stove section vaporizer (8) of oil smoke pipeline section vaporizer (7)
And compressing it into high temperature and high pressure gas, described high temperature and high pressure gas is discharged into described condenser (11), described High Temperature High Pressure again
Gas heat release be condensed into highly pressurised liquid in described condenser (11), then through described throttling arrangement (10) throttling be low-pressure low-temperature
Cold-producing medium, again go into described oil smoke pipeline section vaporizer (7) and described cooking stove section vaporizer (8) heat absorption vaporization；
Cold water enters described condenser (11) from cold water oral siphon road (17), and with high temperature and high pressure gas in described condenser (11)
Heat exchange forms hot water, and described hot water is discharged from hot water effluent's pipeline (18).
Kitchen oil fume purifying the most according to claim 1 and heat recovery integrated apparatus, it is characterised in that also wrap
Including air handling system, described air handling system includes that air inlet inertial separation section (2-1) being sequentially connected with, air electrostatic remove
Dirt section (4-1), the first air activated carbon adsorption pipeline section (5-1), the second blower fan (6-1), air-treatment vaporizer (7-1) and air-supply
Mouth (14), air inlet inertial separation section (2-1) uses inertial separation method to purify sucking air, described air electrostatic dedusting
Section (4-1) uses electrostatic high-pressure process of cleaning to purify sucking air, and described first air activated carbon adsorption pipeline section (5-1) is adopted
Purify sucking air by absorption method；
Air is entered described air electrostatic dedusting section (4-1) by described air inlet inertial separation section (2-1) to carry out being electrolysed dedusting, removes
Air after dirt carries out filtration treatment, through filtered air by institute by described first air activated carbon adsorption pipeline section (5-1)
Stating the second blower fan (6-1) and send into described air-treatment vaporizer (7-1), air is by described air-treatment vaporizer (7-1)
Heat exchange is carried out with the coil pipe in described air-treatment vaporizer (7-1), described air-treatment vaporizer (7-1) after heat exchange during portion
In working medium vaporization become the 3rd low temperature low pressure gas, and become after entering the air heat-exchange of described air-treatment vaporizer (7-1)
For Cryogenic air, Cryogenic air is fed to kitchen space through described air outlet (14)；
Described compressor (9) absorbs from the 3rd low temperature low pressure gas of described air-treatment vaporizer (7-1) with from described
First low temperature low pressure gas of oil smoke pipeline section vaporizer (7) and the second low-temp low-pressure gas from described cooking stove section vaporizer (8)
Body also compresses it into high temperature and high pressure gas.
Kitchen oil fume purifying the most according to claim 2 and heat recovery integrated apparatus, it is characterised in that described
Air handling system also includes the second air activated carbon adsorption pipeline section (5-2), the 3rd blower fan (6-2) and Boiler pressure control plate (15),
Described second air activated carbon adsorption pipeline section (5-2) uses absorption method to purify sucking air；
Air is entered the second air activated carbon adsorption pipeline section (5-2) by described Boiler pressure control plate (15) and carries out filtration treatment, passes through
Filtered air is delivered to described air outlet (14) by described 3rd blower fan (6-2), enters kitchen by described air outlet (14) empty
Between.
Kitchen oil fume purifying the most according to claim 1 and heat recovery integrated apparatus, it is characterised in that described
Residual neat recovering system also includes filter (13), and described filter is arranged on described cold water oral siphon road (17).
Kitchen oil fume purifying the most according to claim 1 and heat recovery integrated apparatus, it is characterised in that described
Residual neat recovering system also includes water tank (12), and described water tank (12) is by described hot water effluent's pipeline (18) and described condenser
(11) connection.
Kitchen oil fume purifying the most according to claim 5 and heat recovery integrated apparatus, it is characterised in that described
Phase-change material (19) it is provided with in water tank (12).
Kitchen oil fume purifying the most according to claim 6 and heat recovery integrated apparatus, it is characterised in that described
Phase-change material (19) is expanded graphite/paraffin composite phase change material.
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| CN201610927831.2A CN106322476B (en) | 2016-10-31 | 2016-10-31 | A kind of kitchen oil fume purifying and heat recovery integrated apparatus |
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| CN201610927831.2A CN106322476B (en) | 2016-10-31 | 2016-10-31 | A kind of kitchen oil fume purifying and heat recovery integrated apparatus |
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| CN106322476A true CN106322476A (en) | 2017-01-11 |
| CN106322476B CN106322476B (en) | 2018-09-18 |
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| CN107178812A (en) * | 2017-07-27 | 2017-09-19 | 浙江大昱环保科技有限公司 | A kind of oil smoke static state cooling intercepts cleaning system |
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| CN107178812A (en) * | 2017-07-27 | 2017-09-19 | 浙江大昱环保科技有限公司 | A kind of oil smoke static state cooling intercepts cleaning system |
| CN108088074A (en) * | 2017-12-03 | 2018-05-29 | 天津大学 | Novel oil smoke heat recovery system and method based on absorption heat pump |
| CN108151366A (en) * | 2017-12-25 | 2018-06-12 | 广东伊蕾科斯环境科技有限公司 | A kind of building air exhaust waste heat reclaiming type air source heat pump system |
| CN107990389A (en) * | 2018-01-17 | 2018-05-04 | 浙江大昱环保科技有限公司 | A kind of interior circulation zero-discharging lampblack purifying system |
| CN108405181A (en) * | 2018-03-02 | 2018-08-17 | 朱浩淼 | A kind of fume purifying waste-heat recovery device |
| CN108344005A (en) * | 2018-03-27 | 2018-07-31 | 重庆大学 | Large and medium-sized kitchen residual heat recycling system |
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| CN110360619B (en) * | 2018-04-09 | 2020-11-24 | 宁波方太厨具有限公司 | Kitchen air conditioning system |
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| US20210325058A1 (en) * | 2018-06-29 | 2021-10-21 | Ningbo Fotile Kitchen Ware Co., Ltd. | Kitchen Air Conditioning System |
| CN108644848A (en) * | 2018-07-23 | 2018-10-12 | 蔡林祥 | A kind of photodissociation fume purifier of fume |
| CN109099584A (en) * | 2018-07-24 | 2018-12-28 | 哈尔滨工业大学 | A kind of kitchen ventilation residual neat recovering system having both hot water supply and tableware drying function |
| CN108895506B (en) * | 2018-08-28 | 2019-11-08 | 绍兴市德帏纺织科技有限公司 | A kind of residual heat using device of kitchen ventilator |
| CN108895506A (en) * | 2018-08-28 | 2018-11-27 | 李霞林 | A kind of residual heat using device of kitchen ventilator |
| CN109140558A (en) * | 2018-10-11 | 2019-01-04 | 浙江建设职业技术学院 | A kind of smoke exhaust ventilator flue gas heating combined equipment and method |
| CN109340851A (en) * | 2018-10-24 | 2019-02-15 | 哈尔滨工业大学 | A kind of kitchen ventilation oil removing and residual neat recovering system |
| CN110074552A (en) * | 2019-05-05 | 2019-08-02 | 成都马踏飞燕科技有限公司 | A kind of novel smokeless hot pot table |
| CN110230829A (en) * | 2019-07-10 | 2019-09-13 | 四川丞仕邦厨房设备有限公司 | A kind of multifunctional integrated range |
| CN110230829B (en) * | 2019-07-10 | 2024-03-12 | 四川丞仕邦厨房设备有限公司 | Multifunctional integrated kitchen range |
| WO2021135717A1 (en) * | 2019-12-31 | 2021-07-08 | 宁波方太厨具有限公司 | Kitchen air conditioning system |
| CN111156552A (en) * | 2020-01-03 | 2020-05-15 | 珠海格力电器股份有限公司 | Kitchen waste gas treatment method and device |
| CN112138514A (en) * | 2020-08-13 | 2020-12-29 | 黎本河 | Quick cooling separation and purification principle for kitchen oil smoke and water vapour industry waste miasma |
| CN112066421A (en) * | 2020-08-28 | 2020-12-11 | 江西摩力斯科技股份有限公司 | Novel purify integrated kitchen |
| CN113188167A (en) * | 2021-04-22 | 2021-07-30 | 冯卓林 | Kitchen oil smoke purifies energy-saving equipment |
| CN113188167B (en) * | 2021-04-22 | 2022-07-19 | 冯卓林 | Kitchen oil smoke purifies energy-saving equipment |
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