CN102240659B - Equipment for integrally treating oil-water separation of kitchen garbage - Google Patents
Equipment for integrally treating oil-water separation of kitchen garbage Download PDFInfo
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- CN102240659B CN102240659B CN2011101150765A CN201110115076A CN102240659B CN 102240659 B CN102240659 B CN 102240659B CN 2011101150765 A CN2011101150765 A CN 2011101150765A CN 201110115076 A CN201110115076 A CN 201110115076A CN 102240659 B CN102240659 B CN 102240659B
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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
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/10—Waste collection, transportation, transfer or storage, e.g. segregated refuse collecting, electric or hybrid propulsion
Abstract
The invention relates to equipment for integrally treating oil-water separation of kitchen garbage, composed of four parts as follows: an electronic display controller, a garbage material storage separator, an oil-water separation tank and an oil-water product recycling device. Safe and high-efficiency oil-water separation integrated treatment of the kitchen garbage is realized. Furthermore, resource and harmless treatments of the kitchen garbage are well realized. By means of the equipment disclosed by the invention, hogwash harm can be stopped at the source; and the shortage of resources in our country can be relieved.
Description
Technical field
The invention belongs to a kind of refuse treatment engineering technical field, relate to a kind of changing food waste treatment facility, especially relate to a kind of changing food waste water-oil separating integrated equipment for wastewater treatment.
Background technology
Along with improving constantly of China's constant development of economy and living standards of the people; The catering trade in each city has also got into the high speed development stage; But thing followed house refuse, changing food waste are seriously polluting urban environmental hygiene, bring great harm for the life health of numerous people.
Changing food waste is commonly called as " swill "; It is the residue after the meal of food and beverage enterprises such as hotel, dining room, dining room and family; Mainly comprise rice and wheaten foods remnants, vegetables, vegetable oil, animal oil, meat bone class, fishbone etc., the animal and plant wet goods contains the organic substance of abundant biomass energy.Changing food waste is a kind of potential resource that receives long-standing neglect, owing to utilize improper many social concerns that produced.With regard to quantity, the discharge capacity of big city such as Beijing, Shanghai every day all surpasses kiloton, and medium-sized city such as Ningbo, Chengdu also all has to surpass hundreds of tons every day.
At present, China's rapid economic development urban population increases rapidly, and the people's lives level improves constantly, and urban restaurant trade is become increasingly prosperous, and the generation of changing food waste is unprecedentedly increased.The National urban sales of the catering industry were 10,345 hundred million yuan in 2006, reached 12,352 hundred million yuan in 2010, every year on average with 17.9% speed increment.Do not comprise small-sized cities and towns, annual more than 2,000 ten thousand tons of the changing food wastes that produce in national big and medium-sized cities.
Compare with other domestic wastes; The changing food waste water content is high, content of organics is high, and fat content and salt content are high, and poisonous and harmful substance (like heavy metal etc.) content is few; But the speed that rots is fast; It is perishable rotten to be prone to grow bacterium, particularly high temperature season, causes a large amount of rapidly breedings of harmful substances such as pathogenic microorganism, mycotoxin.Therefore, if can not get dealing carefully with, will cause adverse effect to environment and health.
Existing changing food waste treatment technology mainly comprises both at home and abroad: physics fragmentation, high temperature aerobic composting, anaerobic fermentation, earthworm are handled, dried heat is handled.These technology all have application abroad, and have obtained certain effect.
American-European developed country is because the changing food waste generation is less, and it is main that its processing mode pours sewer with the physics fragmentation, but this processing mode is also incompatible to the big national conditions of Chinese changing food waste generation, can increase the processing load of sewage treatment plant on the contrary.
Current, domestic changing food waste treatment technology mainly is to adopt/anaerobic organism fermentation or heat treated mode, and its product mainly contains two kinds of fertilizer and protein feed raw materials.But owing to contain rich nutrient substances in the changing food waste, more development trend is that its processing is processed as the protein feed raw material, so not only makes resource obtain utilizing, and more can effectively alleviate the situation of " people and animals strive grain ".But; Most of technology just directly is processed into the protein feed raw material after with changing food waste letter sorting, preliminary treatment, dehydration, drying; And ignored the risk that changing food waste exists as feed; Then possibly there are the problem of potential safety hazard in pathogenic microorganism wherein and animal derived materials if can not deal carefully with.In 20 end of the centurys, worldwide popular of livestock and poultry communicate illness such as rabid ox disease, itch makes people recognize that fully homology eats the seriousness of problem mutually.Therefore, a kind of method of utilizing producing protein feed material by utilizing food wastes is provided at present,, reduces homology phase eating habit danger to ensure meal kitchen class feed product quality.
Dining room rubbish mainly contains two kinds through the prior art that anaerobic fermentation obtains biogas at present:
The first obtains biogas from refuse landfill.The advantage of this method is that procurement cost is low, treats that the landfill yard landfill waste is abundant, and normally when being about to closing, direct cannulation goes into by the extraction of landfill waste depths to get final product.The shortcoming of the method is that anaerobic methane production efficient is poor, and atmosphere pollution.This is because landfill yard is in wide-open environment; In the rubbish can the rotten organic matter overwhelming majority be to become thoroughly decomposed at good oxygen condition (or half good oxygen condition); Several years such as have only even make more than 10 years when before enough thick rubbish cover layer (generally about 10 meters) being arranged by the landfill waste top; Could really make before to be in anaerobic state by landfill waste, but this moment in the rubbish can rotten organic matter seldom.But we can feel still that sometimes the category sludge gas amount is very big, and that only is because by the quantity of refuse of the landfill cause that is too big really.Though so scheme is cheap, the anaerobic methane production poor efficiency can not obtain high benefit.
It two is rubbish to be stored in the airtight container through anaerobic fermentation obtain biogas.The advantage of this method is that to obtain biogas efficient high because in the rubbish can rotten organic matter be in basically fully become thoroughly decomposed in the anaerobic environment stable.Weak point is that to expend cost too high, mainly expends: gentle circulation ventilation etc. is pulverized, forces to stir, added to refuse classification (organic waste is sorted out), organic waste.All these cost costs all are to become thoroughly decomposed as early as possible in order to quicken organic waste, shorten the anaerobic fermentation cycle, generally can be controlled in 30 days.The enough subsidies of anarchy although consequently the biogas benefit is fine, but still are not enough to offset cost, if will be difficult to keep on the go.Though so scheme anaerobic methane production efficient is high, cost is too high, can not obtain high benefit.
Existing storing bulk material silo generally adopts steel construction or reinforced concrete structure, accomplishes in case build, and its warehouse height all is changeless.The warehouse material is except that satisfying the requirement of strength; Adequate thickness also must be arranged to form the rigidity that whole silo body has resistance to deformation; So just can guarantee no matter buy securities with all one's capital or hole capital after selling all securities in the silo; Whole silo body all is stable, and we are referred to as " rigidity silo " this silo, and existing silo belongs to the rigidity silo basically.
Because of the warehouse thickness of rigidity silo is to thicken with the silo capacity, so if build big capacity rigidity silo, cost can be very expensive.
The dining room discarded object has the characteristics of himself, when carrying out sanitary landfills, has problems such as floor space is big, secondary pollution, potential safety hazard; It is maximum to burn the minimizing degree, and initial investment and operating cost are higher, processing procedure possibly produce danger wastes such as bioxin, flying dust, receive common people's degree of awareness to limit and supervise restriction, and burning disposal is still promoted difficulty; The compost treatment organic solid castoff exists then that heavy metal is difficult to separate, nitrogen loss is serious, energy consumption is big, shortcomings such as the high and difficult collection of odorous gas concentration.
Anaerobic fermentation is under anaerobic, and it is CH that organic matter is carried out decomposition and inversion
4And CO
2Process.Have following advantage: (1) floor space is little, the processing cycle short; (2) sweat can produce methane as clean energy source and high-quality humus fertilizer; (3) sweat is controlled easily, does not produce secondary pollution; (4) but complete closed handle, can not pollute surrounding enviroment.
More to anaerobic fermentation research at present, the fermentation of individual event anaerobic fermentation and diphasic anaerobic is arranged; Mesophilic digestion and hot fermentation; Wet type fermentation, dry type fermentation and half dry type fermentation.
Anaerobic fermentation in the past is often to single material; Carbon-nitrogen ratio, moisture content, acid-base value etc. are in smaller scope; Need the parameter of adjusting many; Particularly the single fermentation material can produce feedback inhibition to methane backeria, has the ammonia nitrogen concentration height, has inhibitory action, fermentation load to hang down the characteristics such as solid holdup is low that reach to methanogen and hydrogenogen like manure fermentation; Changing food waste has that oil content is big, foreign matter is many, solid holdup is high, the characteristics of the easy acidifying of fermentation substrate; Domestic waste has that the content of organic matter is low, composition is big with the space-time fluctuation, the characteristics big to the anaerobic fermentation system impulsive force.Build treatment facility respectively to various discarded objects in addition, investment is big and be difficult to bring into play the scale effect.Particularly the inhibition factor of single material is obvious, and material adjusting difficulty is very big.
The dining room discarded object carries out anaerobic fermentation after the preliminary treatment; Can solve that the fermentation materials homogenieity is poor, fermentation efficiency is low, the tunning inhibitory action; Can enlarge simultaneously the biogas scale of producing; Promote liquid natural pond, natural pond slag quality, focus on various organic solid castoffs, improve the level of resource, innoxious and minimizing.
Changing food waste is different from other discarded objects (house refuse, industrial refuse, TRADE REFUSE, agricultural wastes etc.), and its characteristics are: 1, moisture content is high, about 72% (removal free water)-92% (containing free water); 2, complicated component, content of organics is high, about 90% (dry weight); 3, fat content is high; 4, contain anaerobic fermentation is had inhibiting salt; 5, because of not classification, contain 10% the impurity (being mainly chopsticks, plastics, paper, little metal, cutlery box, packing material etc.) of having an appointment, post-processed equipment (fermentation, dehydration, pipeline etc.) is had a negative impact.
The main method of present processing utensil rubbishes; Be that organic waste is handled through operations such as grease separation, preliminary sorting, Mechanical Crushing, hydraulic pulping, allotment slurry, anaerobic fermentations; Make changing food waste degrade fully; Finally decomposite biogas through anaerobic digestion, biogas after desulfurization is handled as using energy source; The natural pond slag is produced the high-quality fertilizer through control oxygen compost; Isolated grease can be recycled as regeneration raw material of industry oil.At the waste water reusable edible that processing procedure produces, final unnecessary waste water is through qualified discharge after the biochemical treatment; The foul smell that rubbish produces in the processing procedure is handled directly discharging of back up to standard through biofiltration.This processing method complex technical process, energy consumption is higher; The equipment that needs is many, and investment is high.
At present, the whereabouts of changing food waste mainly contains direction: the one, do not add processing and feed " swill pig " as raw material, through the food chain harm humans in virtually; The 2nd, from changing food waste, pulled out " waste oil " by some illegal retailers and be processed into " edible oil " and come into the market again, the grievous injury consumer health jeopardizes food security; The 3rd, directly discharge as rubbish, not only stop up the urban sewage pipeline, distribute rancid smell, and the severe contamination water source, environmental sanitation is caused enormous pressure.
Therefore, the integrated processing of changing food waste water-oil separating safely and efficiently can realize good changing food waste being carried out resource, harmless treatment, both can stop the harm of swill from the source, can alleviate the china natural resources problem of shortage again.
Summary of the invention
Technical problem to be solved by this invention provides a kind of changing food waste water-oil separating integrated equipment for wastewater treatment; Overcome the shortcoming of above-mentioned prior art; To the situation of domestic changing food waste profit complicated component, develop the present invention is stored split device, gun barrel and the mutual collaborative work of profit product retracting device four parts by electronic display controller, rubbish material electronic waste Integrated Processing Unit.
The objective of the invention is through designing a kind of changing food waste water-oil separating integrated equipment for wastewater treatment; This changing food waste water-oil separating integrated equipment for wastewater treatment stores split device, gun barrel and profit product retracting device four parts by electronic display controller, rubbish material and forms; Not only realized the integrated processing of changing food waste water-oil separating safely and efficiently; And can realize good changing food waste being carried out resource, harmless treatment; Both can stop the harm of swill from the source, can alleviate the china natural resources problem of shortage again.
For realizing above-mentioned purpose, the present invention realizes through following technical scheme:
A kind of changing food waste water-oil separating integrated equipment for wastewater treatment of the present invention comprises electronic display controller, it is characterized in that: comprise that also the rubbish material that is connected with electronic display controller respectively stores split device, gun barrel and profit product retracting device; Wherein, Said electronic display controller, rubbish material store split device, gun barrel and the mutual collaborative work of profit product retracting device four parts; Said electronic display controller is used for charging and the discharging that real-time monitoring rubbish material stores split device, gun barrel and profit product retracting device, and is done in such a manner the integrated processing procedure of changing food waste water-oil separating:
(1) said rubbish material stores split device and comprises U type or V-type housing, two seal cover boards; Be built in the first cylindrical Rose Box of housing inlet, a plurality of high speeds that are built in housing bottom vertically rotate teeter column, be built in the steam heater of housing liquid outlet, be built in the housing liquid outlet and at the second cylindrical Rose Box on steam heater top; Wherein, the height of the inlet end of said U type or V-type housing is 1.5～2.5 times of liquid outlet end height; The built-in three layers of carbon fiber fine screen mesh of said first cylindrical filter; These three layers of carbon fiber fine screen mesh from top to bottom successively respectively with particle diameter for to hold back greater than the solid impurity of 10mm, 3.5～10mm, 1～3.5mm, be transported to settling tank through circle round wind energy conversion system and conveying worm then; The built-in one deck carbon fiber of said second cylindrical Rose Box fine screen mesh; This layer carbon fiber fine screen mesh with particle diameter for to hold back greater than the solid impurity of 1mm; Said steam heater has a plurality of U type steam pipes; The rubbish oil water mixture that sees through the first cylindrical Rose Box vertically rotates teeter column through a plurality of high speeds of housing bottom; Through steam heater, carry out the oil removing sterilization with steam then, the grease in the oil water mixture can be that liquid phase is exuded to said gun barrel through the second cylindrical Rose Box by solid transformation under steam high temperature;
(2) said gun barrel comprise a plurality of parallel feed passages, with the channel attached steam heater of a plurality of parallel feeds, anaerobic reactor, gravity oil removal jar, oil trap, aerobic reaction pond and membrane biological reaction pond; Wherein, the built-in membrane bioreactor in said membrane biological reaction pond by a plurality of series connection, said membrane bioreactor is made up of membrane module and filter membrane, and filter membrane is fibrous unidirectional semipermeable membrane, and the aperture of film is 0.005 micron; Material that the second cylindrical Rose Box the oozes out steam heater through said gun barrel that passes through in above-mentioned (1) is heated to 63-77 ℃ and sends into anaerobic reactor and carry out anaerobic reaction; After the material that from anaerobic reactor, comes out is sent into and is precipitated 20～40 minutes in the gravity oil removal jar; Oil skimmer through install said gravity oil removal jar upper end casts aside the grease on said gravity oil removal jar surface into oil trap, and the remaining material of said gravity oil removal jar is for use after filtering through carrying out membrane bioreactor in Aerobic Process for Treatment and the membrane biological reaction pond in the aerobic reaction pond successively again;
(3) said profit product retracting device, said profit product retracting device comprises the horizontal cylindrical elongated tubular and the lower end is the toot of tip; Wherein, said lower end be the center line of toot of tip perpendicular to the horizontal cylindrical elongated tubular, said horizontal cylindrical elongated tubular water side and lower end are that the toot middle part of tip is communicated with; Material after membrane bioreactor in the membrane biological reaction pond in above-mentioned (2) filters feeds the dissolved oil in the said horizontal cylindrical elongated tubular, oil emulsion, the dispersed oil that part is not removed; Multilayer filtrate through built-in adsorbs, condenses into oarse-grained oil film; Getting into the lower end with water (flow) direction then is the toot of tip; In the lower end is in the toot of tip; The grease of waste water partly floats, and last oil slick is that the oil skimmer of the toot middle and upper part of tip is cast aside in the oil trap by being installed in said lower end, and the waste water after the de-oiling is that the bottom of the toot of tip flows into water treatment system through said lower end.
As optimized technical scheme:
The height of the said U type in above-mentioned (1) or the inlet end of V-type housing is 2 times of liquid outlet end height.
The material that oozes out in above-mentioned (2) is heated to 68 ℃ through above-mentioned steam heater and sends into anaerobic reactor and carry out anaerobic reaction.
After the material that from anaerobic reactor, comes out in above-mentioned (2) is sent into and precipitated 30 minutes in the gravity oil removal jar, the grease on said gravity oil removal jar surface is cast aside into oil trap through the oil skimmer that install said gravity oil removal jar upper end.
This equipment has been compared following advantage with prior art:
1. crude waste needn't sorting and pulverizing, can reduce operating cost significantly.
2. needn't carry out other manpower and mechanical intervention, operating cost is very low.
3. many various solid materials not of uniform size are arranged in the rubbish, and thoroughly becoming thoroughly decomposed needs the long period, build enough a plurality of large-scale silo structures decomposed period is fully prolonged, and it is many more to consume sewage than long decomposed period, realizes with dirty pollution treatment effect.
4. economic benefit is high.
Description of drawings
Fig. 1 is the sketch map of changing food waste water-oil separating integrated equipment for wastewater treatment of the present invention.
The specific embodiment
Below in conjunction with the specific embodiment, further set forth the present invention.
Embodiment 1:
A kind of changing food waste water-oil separating integrated equipment for wastewater treatment comprises electronic display controller, it is characterized in that: comprise that also the rubbish material that is connected with electronic display controller respectively stores split device, gun barrel and profit product retracting device; Wherein, Said electronic display controller, rubbish material store split device, gun barrel and the mutual collaborative work of profit product retracting device four parts; Said electronic display controller is used for charging and the discharging that real-time monitoring rubbish material stores split device, gun barrel and profit product retracting device, and is done in such a manner the integrated processing procedure of changing food waste water-oil separating:
(1) said rubbish material stores split device and comprises U type or V-type housing, two seal cover boards; Be built in the first cylindrical Rose Box of housing inlet, a plurality of high speeds that are built in housing bottom vertically rotate teeter column, be built in the steam heater of housing liquid outlet, be built in the housing liquid outlet and at the second cylindrical Rose Box on steam heater top; Wherein, the height of the inlet end of said U type or V-type housing is 2 times of liquid outlet end height; The built-in three layers of carbon fiber fine screen mesh of said first cylindrical filter; These three layers of carbon fiber fine screen mesh from top to bottom successively respectively with particle diameter for to hold back greater than the solid impurity of 10mm, 3.5～10mm, 1～3.5mm, be transported to settling tank through circle round wind energy conversion system and conveying worm then; The built-in one deck carbon fiber of said second cylindrical Rose Box fine screen mesh; This layer carbon fiber fine screen mesh with particle diameter for to hold back greater than the solid impurity of 1mm; Said steam heater has a plurality of U type steam pipes; The rubbish oil water mixture that sees through the first cylindrical Rose Box vertically rotates teeter column through a plurality of high speeds of housing bottom; Through steam heater, carry out the oil removing sterilization with steam then, the grease in the oil water mixture can be that liquid phase is exuded to said gun barrel through the second cylindrical Rose Box by solid transformation under steam high temperature;
(2) said gun barrel comprise a plurality of parallel feed passages, with the channel attached steam heater of a plurality of parallel feeds, anaerobic reactor, gravity oil removal jar, oil trap, aerobic reaction pond and membrane biological reaction pond; Wherein, the built-in membrane bioreactor in said membrane biological reaction pond by a plurality of series connection, said membrane bioreactor is made up of membrane module and filter membrane, and filter membrane is fibrous unidirectional semipermeable membrane, and the aperture of film is 0.005 micron; Material that the second cylindrical Rose Box the oozes out steam heater through said gun barrel that passes through in above-mentioned (1) is heated to 63-77 ℃ and sends into anaerobic reactor and carry out anaerobic reaction; After the material that from anaerobic reactor, comes out is sent into and is precipitated 20～40 minutes in the gravity oil removal jar; Oil skimmer through install said gravity oil removal jar upper end casts aside the grease on said gravity oil removal jar surface into oil trap, and the remaining material of said gravity oil removal jar is for use after filtering through carrying out membrane bioreactor in Aerobic Process for Treatment and the membrane biological reaction pond in the aerobic reaction pond successively again;
(3) said profit product retracting device, said profit product retracting device comprises the horizontal cylindrical elongated tubular and the lower end is the toot of tip; Wherein, said lower end be the center line of toot of tip perpendicular to the horizontal cylindrical elongated tubular, said horizontal cylindrical elongated tubular water side and lower end are that the toot middle part of tip is communicated with; Material after membrane bioreactor in the membrane biological reaction pond in above-mentioned (2) filters feeds the dissolved oil in the said horizontal cylindrical elongated tubular, oil emulsion, the dispersed oil that part is not removed; Multilayer filtrate through built-in adsorbs, condenses into oarse-grained oil film; Getting into the lower end with water (flow) direction then is the toot of tip; In the lower end is in the toot of tip; The grease of waste water partly floats, and last oil slick is that the oil skimmer of the toot middle and upper part of tip is cast aside in the oil trap by being installed in said lower end, and the waste water after the de-oiling is that the bottom of the toot of tip flows into water treatment system through said lower end.
Embodiment 2:
A kind of changing food waste water-oil separating integrated equipment for wastewater treatment comprises electronic display controller, it is characterized in that: comprise that also the rubbish material that is connected with electronic display controller respectively stores split device, gun barrel and profit product retracting device; Wherein, Said electronic display controller, rubbish material store split device, gun barrel and the mutual collaborative work of profit product retracting device four parts; Said electronic display controller is used for charging and the discharging that real-time monitoring rubbish material stores split device, gun barrel and profit product retracting device, and is done in such a manner the integrated processing procedure of changing food waste water-oil separating:
(1) said rubbish material stores split device and comprises U type or V-type housing, two seal cover boards; Be built in the first cylindrical Rose Box of housing inlet, a plurality of high speeds that are built in housing bottom vertically rotate teeter column, be built in the steam heater of housing liquid outlet, be built in the housing liquid outlet and at the second cylindrical Rose Box on steam heater top; Wherein, the height of the inlet end of said U type or V-type housing is 1.5～2.5 times of liquid outlet end height; The built-in three layers of carbon fiber fine screen mesh of said first cylindrical filter; These three layers of carbon fiber fine screen mesh from top to bottom successively respectively with particle diameter for to hold back greater than the solid impurity of 10mm, 3.5～10mm, 1～3.5mm, be transported to settling tank through circle round wind energy conversion system and conveying worm then; The built-in one deck carbon fiber of said second cylindrical Rose Box fine screen mesh; This layer carbon fiber fine screen mesh with particle diameter for to hold back greater than the solid impurity of 1mm; Said steam heater has a plurality of U type steam pipes; The rubbish oil water mixture that sees through the first cylindrical Rose Box vertically rotates teeter column through a plurality of high speeds of housing bottom; Through steam heater, carry out the oil removing sterilization with steam then, the grease in the oil water mixture can be that liquid phase is exuded to said gun barrel through the second cylindrical Rose Box by solid transformation under steam high temperature;
(2) said gun barrel comprise a plurality of parallel feed passages, with the channel attached steam heater of a plurality of parallel feeds, anaerobic reactor, gravity oil removal jar, oil trap, aerobic reaction pond and membrane biological reaction pond; Wherein, the built-in membrane bioreactor in said membrane biological reaction pond by a plurality of series connection, said membrane bioreactor is made up of membrane module and filter membrane, and filter membrane is fibrous unidirectional semipermeable membrane, and the aperture of film is 0.005 micron; Material that the second cylindrical Rose Box the oozes out steam heater through said gun barrel that passes through in above-mentioned (1) is heated to 68 ℃ and sends into anaerobic reactor and carry out anaerobic reaction; After the material that from anaerobic reactor, comes out is sent into and is precipitated 20～40 minutes in the gravity oil removal jar; Oil skimmer through install said gravity oil removal jar upper end casts aside the grease on said gravity oil removal jar surface into oil trap, and the remaining material of said gravity oil removal jar is for use after filtering through carrying out membrane bioreactor in Aerobic Process for Treatment and the membrane biological reaction pond in the aerobic reaction pond successively again;
(3) said profit product retracting device, said profit product retracting device comprises the horizontal cylindrical elongated tubular and the lower end is the toot of tip; Wherein, said lower end be the center line of toot of tip perpendicular to the horizontal cylindrical elongated tubular, said horizontal cylindrical elongated tubular water side and lower end are that the toot middle part of tip is communicated with; Material after membrane bioreactor in the membrane biological reaction pond in above-mentioned (2) filters feeds the dissolved oil in the said horizontal cylindrical elongated tubular, oil emulsion, the dispersed oil that part is not removed; Multilayer filtrate through built-in adsorbs, condenses into oarse-grained oil film; Getting into the lower end with water (flow) direction then is the toot of tip; In the lower end is in the toot of tip; The grease of waste water partly floats, and last oil slick is that the oil skimmer of the toot middle and upper part of tip is cast aside in the oil trap by being installed in said lower end, and the waste water after the de-oiling is that the bottom of the toot of tip flows into water treatment system through said lower end.
Embodiment 3:
A kind of changing food waste water-oil separating integrated equipment for wastewater treatment comprises electronic display controller, it is characterized in that: comprise that also the rubbish material that is connected with electronic display controller respectively stores split device, gun barrel and profit product retracting device; Wherein, Said electronic display controller, rubbish material store split device, gun barrel and the mutual collaborative work of profit product retracting device four parts; Said electronic display controller is used for charging and the discharging that real-time monitoring rubbish material stores split device, gun barrel and profit product retracting device, and is done in such a manner the integrated processing procedure of changing food waste water-oil separating:
(1) said rubbish material stores split device and comprises U type or V-type housing, two seal cover boards; Be built in the first cylindrical Rose Box of housing inlet, a plurality of high speeds that are built in housing bottom vertically rotate teeter column, be built in the steam heater of housing liquid outlet, be built in the housing liquid outlet and at the second cylindrical Rose Box on steam heater top; Wherein, the height of the inlet end of said U type or V-type housing is 1.5～2.5 times of liquid outlet end height; The built-in three layers of carbon fiber fine screen mesh of said first cylindrical filter; These three layers of carbon fiber fine screen mesh from top to bottom successively respectively with particle diameter for to hold back greater than the solid impurity of 10mm, 3.5～10mm, 1～3.5mm, be transported to settling tank through circle round wind energy conversion system and conveying worm then; The built-in one deck carbon fiber of said second cylindrical Rose Box fine screen mesh; This layer carbon fiber fine screen mesh with particle diameter for to hold back greater than the solid impurity of 1mm; Said steam heater has a plurality of U type steam pipes; The rubbish oil water mixture that sees through the first cylindrical Rose Box vertically rotates teeter column through a plurality of high speeds of housing bottom; Through steam heater, carry out the oil removing sterilization with steam then, the grease in the oil water mixture can be that liquid phase is exuded to said gun barrel through the second cylindrical Rose Box by solid transformation under steam high temperature;
(2) said gun barrel comprise a plurality of parallel feed passages, with the channel attached steam heater of a plurality of parallel feeds, anaerobic reactor, gravity oil removal jar, oil trap, aerobic reaction pond and membrane biological reaction pond; Wherein, the built-in membrane bioreactor in said membrane biological reaction pond by a plurality of series connection, said membrane bioreactor is made up of membrane module and filter membrane, and filter membrane is fibrous unidirectional semipermeable membrane, and the aperture of film is 0.005 micron; Material that the second cylindrical Rose Box the oozes out steam heater through said gun barrel that passes through in above-mentioned (1) is heated to 63-77 ℃ and sends into anaerobic reactor and carry out anaerobic reaction; After the material that from anaerobic reactor, comes out is sent into and is precipitated 30 minutes in the gravity oil removal jar; Oil skimmer through install said gravity oil removal jar upper end casts aside the grease on said gravity oil removal jar surface into oil trap, and the remaining material of said gravity oil removal jar is for use after filtering through carrying out membrane bioreactor in Aerobic Process for Treatment and the membrane biological reaction pond in the aerobic reaction pond successively again;
(3) said profit product retracting device, said profit product retracting device comprises the horizontal cylindrical elongated tubular and the lower end is the toot of tip; Wherein, said lower end be the center line of toot of tip perpendicular to the horizontal cylindrical elongated tubular, said horizontal cylindrical elongated tubular water side and lower end are that the toot middle part of tip is communicated with; Material after membrane bioreactor in the membrane biological reaction pond in above-mentioned (2) filters feeds the dissolved oil in the said horizontal cylindrical elongated tubular, oil emulsion, the dispersed oil that part is not removed; Multilayer filtrate through built-in adsorbs, condenses into oarse-grained oil film; Getting into the lower end with water (flow) direction then is the toot of tip; In the lower end is in the toot of tip; The grease of waste water partly floats, and last oil slick is that the oil skimmer of the toot middle and upper part of tip is cast aside in the oil trap by being installed in said lower end, and the waste water after the de-oiling is that the bottom of the toot of tip flows into water treatment system through said lower end.
Claims (4)
1. a changing food waste water-oil separating integrated equipment for wastewater treatment comprises electronic display controller, it is characterized in that: comprise that also the rubbish material that is connected with electronic display controller respectively stores split device, gun barrel and profit product retracting device; Wherein, Said electronic display controller, rubbish material store split device, gun barrel and the mutual collaborative work of profit product retracting device four parts; Said electronic display controller is used for charging and the discharging that real-time monitoring rubbish material stores split device, gun barrel and profit product retracting device; And be done in such a manner the integrated processing procedure of changing food waste water-oil separating: (1) said rubbish material stores split device and comprises U type or V-type housing, two seal cover boards; Be built in the first cylindrical Rose Box of housing inlet, a plurality of high speeds that are built in housing bottom vertically rotate teeter column, be built in the steam heater of housing liquid outlet, be built in the housing liquid outlet and at the second cylindrical Rose Box on steam heater top; Wherein, the height of the inlet end of said U type or V-type housing is 1.5～2.5 times of liquid outlet end height; The built-in three layers of carbon fiber fine screen mesh of the said first cylindrical Rose Box; These three layers of carbon fiber fine screen mesh from top to bottom successively respectively with particle diameter for to hold back greater than the solid impurity of 10mm, 3.5～10mm, 1～3.5mm, be transported to settling tank through circle round wind energy conversion system and conveying worm then; The built-in one deck carbon fiber of said second cylindrical Rose Box fine screen mesh; This layer carbon fiber fine screen mesh with particle diameter for to hold back greater than the solid impurity of 1mm; Said steam heater has a plurality of U type steam pipes; The rubbish oil water mixture that sees through the first cylindrical Rose Box vertically rotates teeter column through a plurality of high speeds of housing bottom; Through steam heater, carry out the oil removing sterilization with steam then, the grease in the oil water mixture can be that liquid phase is exuded to said gun barrel through the second cylindrical Rose Box by solid transformation under steam high temperature; (2) said gun barrel comprise a plurality of parallel feed passages, with the channel attached steam heater of a plurality of parallel feeds, anaerobic reactor, gravity oil removal jar, oil trap, aerobic reaction pond and membrane biological reaction pond; Wherein, the built-in membrane bioreactor in said membrane biological reaction pond by a plurality of series connection, said membrane bioreactor is made up of membrane module and filter membrane, and filter membrane is fibrous unidirectional semipermeable membrane, and the aperture of film is 0.005 micron; Material that the second cylindrical Rose Box the oozes out steam heater through said gun barrel that passes through in above-mentioned (1) is heated to 63-77 ℃ and sends into anaerobic reactor and carry out anaerobic reaction; After the material that from anaerobic reactor, comes out is sent into and is precipitated 20～40 minutes in the gravity oil removal jar; Oil skimmer through install said gravity oil removal jar upper end casts aside the grease on said gravity oil removal jar surface into oil trap, and the remaining material of said gravity oil removal jar is for use after filtering through carrying out membrane bioreactor in Aerobic Process for Treatment and the membrane biological reaction pond in the aerobic reaction pond successively again; (3) said profit product retracting device, said profit product retracting device comprises the horizontal cylindrical elongated tubular and the lower end is the toot of tip; Wherein, said lower end be the center line of toot of tip perpendicular to the horizontal cylindrical elongated tubular, said horizontal cylindrical elongated tubular water side and lower end are that the toot middle part of tip is communicated with; Material after membrane bioreactor in the membrane biological reaction pond in above-mentioned (2) filters feeds the dissolved oil in the said horizontal cylindrical elongated tubular, oil emulsion, the dispersed oil that part is not removed; Multilayer filtrate through built-in adsorbs, condenses into oarse-grained oil film; Getting into the lower end with water (flow) direction then is the toot of tip; In the lower end is in the toot of tip; The grease of waste water partly floats, and last oil slick is that the oil skimmer of the toot middle and upper part of tip is cast aside in the oil trap by being installed in said lower end, and the waste water after the de-oiling is that the bottom of the toot of tip flows into water treatment system through said lower end.
2. changing food waste water-oil separating integrated equipment for wastewater treatment according to claim 1 is characterized in that: the height of the said U type in above-mentioned (1) or the inlet end of V-type housing is 2 times of liquid outlet end height.
3. changing food waste water-oil separating integrated equipment for wastewater treatment according to claim 1 and 2 is characterized in that: the material that oozes out in above-mentioned (2) is heated to 68 ℃ through above-mentioned steam heater and sends into anaerobic reactor and carry out anaerobic reaction.
4. changing food waste water-oil separating integrated equipment for wastewater treatment according to claim 1 and 2; It is characterized in that: after the material that from anaerobic reactor, comes out in above-mentioned (2) is sent into and precipitated 30 minutes in the gravity oil removal jar, the grease on said gravity oil removal jar surface is cast aside into oil trap through the oil skimmer that install said gravity oil removal jar upper end.
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| CN2011101150765A CN102240659B (en) | 2011-05-05 | 2011-05-05 | Equipment for integrally treating oil-water separation of kitchen garbage |
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| CN2011101150765A CN102240659B (en) | 2011-05-05 | 2011-05-05 | Equipment for integrally treating oil-water separation of kitchen garbage |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102642968A (en) * | 2012-04-26 | 2012-08-22 | 卢瑞琳 | Oil-water-solid separation device for kitchen wastes |
| CN102688623A (en) * | 2012-06-14 | 2012-09-26 | 长沙中联重科环卫机械有限公司 | Material heating device |
| CN103343054A (en) * | 2013-07-08 | 2013-10-09 | 湖南联博机械股份有限公司 | Whole-process monitoring waste cooking oil recovery system |
| CN103538832B (en) * | 2013-10-31 | 2015-04-15 | 无锡同春新能源科技有限公司 | Swill barrel with wind power generation as power supply |
| CN104496057A (en) * | 2014-12-26 | 2015-04-08 | 合肥创想能源环境科技有限公司 | Cleaning device system for tableware in catering industry |
| CN105505557B (en) * | 2015-11-25 | 2019-06-14 | 中国科学院广州能源研究所 | A kind of device of continuous extraction and separation kitchen garbage grease |
| CN107135374A (en) * | 2017-05-02 | 2017-09-05 | 广州聚澜健康产业研究院有限公司 | A kind of kitchen waste processing equipment monitoring management system |
| CN106915875A (en) * | 2017-05-16 | 2017-07-04 | 张阳康 | A kind of municipal sewage system |
| CN112879652B (en) * | 2021-01-08 | 2023-05-09 | 上海东海压力容器制造股份有限公司 | Centralized treatment system equipment for treating waste by waste based on living and sludge garbage |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP4501142B2 (en) * | 2005-12-28 | 2010-07-14 | 有限会社 だるま設備設計 | Oil-water separator |
| CN101367086B (en) * | 2007-07-25 | 2011-02-09 | 练其辉 | Processing method capable of quite recycling solid garbage |
| JP5503203B2 (en) * | 2008-12-16 | 2014-05-28 | 株式会社木村技研 | Oil-water separator and kitchen system |
| CN101480541B (en) * | 2009-01-12 | 2011-01-05 | 北京青龙河经济技术开发有限公司 | Solid-liquid separator suitable for kitchen waste |
| CN101524700B (en) * | 2009-04-28 | 2012-01-25 | 王绍康 | Treating technical method for food wastes and treating equipment |
| CN102039303B (en) * | 2010-11-12 | 2012-07-04 | 河南省澳斯迪环保机械有限责任公司 | Municipal solid waste comprehensive treatment and recycling device |
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