CN212238595U - System for coprocessing kitchen garbage and food and beverage garbage - Google Patents

Abstract

The utility model discloses a system for co-processing kitchen waste and food and beverage waste, which comprises a kitchen waste pretreatment unit, a food and beverage waste pretreatment unit, a mixing device and a dry anaerobic fermentation device, wherein the kitchen waste pretreatment unit is provided with a kitchen waste inlet, a first leachate outlet, a first inorganic impurity outlet and a crushed kitchen waste outlet; the food waste pretreatment unit is provided with a food waste inlet, a second inorganic impurity outlet, a third inorganic impurity outlet, a second leachate outlet, a grease outlet, a wastewater outlet and a food waste slurry outlet; the mixing device is provided with a crushed kitchen waste inlet, a food and beverage waste slurry inlet and a mixed organic slurry outlet, and the food and beverage waste slurry inlet is connected with the food and beverage waste slurry outlet; the dry anaerobic fermentation device is provided with a mixed organic slurry inlet, a methane outlet and an anaerobic digestion liquid outlet, and the mixed organic slurry inlet is connected with the mixed organic slurry outlet through a scraper conveyer.

Description

System for coprocessing kitchen garbage and food and beverage garbage

Technical Field

The utility model belongs to the technical field of organic solid useless resourceization, innoxiousness and minimizing, concretely relates to system of refuse and food and beverage rubbish in coordination.

Background

The food waste is mainly food residue, namely food residues of restaurants, unit canteens and the like, and wastes of post-kitchen processing processes of fruits, vegetables, meat, grease, pastries and the like. The food residues take organic matters such as starch, dietary fiber and animal fat as main components, and have the characteristics of high water content, high oil and salt content, easy change, fermentation and smelliness, the relevance of the components of the food wastes and the dietary habits of various places is large, the water content of the food wastes is generally between 85 and 90 percent, the organic matter content of the food wastes is more than 90 percent, other sundries mainly comprise seafood shells, plastic rubbers, napkins, paper, chopsticks, broken bowls, glass bottles/cups, metal boxes and the like, and the components are very complex.

Kitchen waste is mainly perishable organic waste such as discarded fruit and vegetable and food leftovers, melon and fruit peels and the like in daily life of a family at present. In addition, the main components of the kitchen garbage are discarded organic garbage such as rotten fruits, vegetables, fishes, poultry and the like, and are also main sources of kitchen garbage, and because domestic garbage classification is in a starting stage, the kitchen garbage conveyed and treated is more complex in components and higher in impurity content than food and beverage garbage, the properties of the kitchen garbage and the food and beverage garbage are similar, but the kitchen garbage and the food and beverage garbage are mainly raw materials and are relatively low in salt content and grease content.

At present, the main treatment technologies of food waste and kitchen waste in China comprise crushing direct discharge, landfill treatment, incineration, fertilizer treatment and the like:

(1) crushing and direct discharging

The crushing and direct discharging treatment is a main method for treating a small amount of dispersed kitchen waste in European and American countries, the kitchen waste is directly crushed and crushed at a kitchen waste generating point, then the kitchen waste is discharged into an urban municipal sewer pipe network by adopting hydraulic flushing, and the kitchen waste and the urban sewage are combined and enter an urban sewage treatment plant for centralized treatment. With the development of society, the living standard of people is improved, the production amount of food waste and kitchen waste is increased day by day, the food waste and the kitchen waste are crushed and directly discharged into a sewer, the resource utilization and the reduction are not realized, and the large-scale treatment is difficult to apply. The food waste and kitchen waste contain complex components and contain fiber substances, and if the food waste and the kitchen waste are discharged into municipal pipe networks in cities, the pipe networks are easily blocked.

(2) Landfill treatment technology

Landfill is a main treatment mode for harmless treatment of domestic garbage in most countries, but because the landfill occupies a large amount of land, a large amount of expenses for land acquisition and the like are consumed, the landfill occupies a large area and has limited treatment capacity, and after the service is expired, a new landfill is still needed to be built, so that land resources are further occupied; leachate of the kitchen waste can pollute underground water and soil, odor generated by stacking the waste seriously influences air quality, irreversible secondary pollution to surrounding large-scale atmosphere and water and soil is formed, the waste is not recycled, the kitchen waste is not advocated for landfill in Europe and America, Japan and China, and a plurality of countries have been well-documented to forbid the kitchen waste from entering a landfill site for treatment.

Under the current conditions that land resources are in short supply and the attention of people to the environmental influence is higher and higher, the landfill treatment technology is obviously not suitable for the actual condition of kitchen waste treatment in China. But the method has certain feasibility as a final treatment means of inorganic impurities after the sorting treatment of the kitchen waste, so that the landfill can be used as an auxiliary treatment link for treating the food waste and the kitchen waste.

(3) Incineration treatment technology

The incineration treatment capacity is large, the capacity reduction is good, and the energy of the garbage can be realized by using the heat generated in the incineration process for power generation. However, the average water content of the kitchen waste is more than 80%, and the calorific value is about 2011kJ/kg, so that the kitchen waste is not suitable for incineration treatment.

Due to different living habits and different degrees of kitchen waste collection and classification in China, the kitchen waste in China has larger difference with foreign kitchen waste, and is characterized by high water content, low heat value, difficult direct incineration treatment, high incineration treatment investment and less application experience of directly treating the kitchen waste by incineration at home and abroad.

(4) Fertilizer treatment technology

The composting treatment of the kitchen waste mainly refers to an aerobic composting technology, wherein in the aerobic composting process, organic solids are decomposed into soluble organic matters by using extracellular enzymes secreted by aerobic microorganisms under an aerobic condition, and then the soluble organic matters permeate into cells, and the whole composting process is realized through metabolism of the microorganisms. The formed compost product is rich in humus, N, P, K and other nutrient elements, and is not only a soil conditioner, but also a high-quality fertilizer. The optimum water content required by the aerobic composting process is 50-60%, and if the water content exceeds 70%, the temperature of the compost is difficult to rise, and the decomposition speed is obviously reduced.

The defects of aerobic composting are that because of the complexity of kitchen waste in China, the pollution to harmful organic matters, grease, salt, heavy metal and the like cannot be well solved, and the harmless treatment is not thorough; the treatment process is not closed, so that secondary pollution is easily caused; the quality of the organic fertilizer is greatly restricted by the components of the kitchen waste, so that the sale is not smooth; the composting period is long, the occupied area is large, and the sanitary condition is relatively poor.

The kitchen waste in China starts late, and currently, the technology adopted by the existing municipal waste composting plant in China lags behind, and the degree of mechanization and automation is low, so that a plurality of composting products cannot reach the use standard, and the finished fertilizer becomes waste due to the sale problem.

(5) Technology for making feed

The feed treatment technology mainly adopts a physical means to heat the kitchen waste at high temperature, dry, sterilize and remove salt and the like, so that usable substances such as protein feed additives and the like can be finally generated.

There are two ways of feed processing: 1) the principle of the biological treatment for preparing the feed is that cultured strains are added into a sealed storage tank of kitchen waste, and the strains are propagated and pathogenic bacteria are killed to prepare the feed. 2) The high-temperature disinfection principle is adopted to kill virus, and the feed is processed after being crushed and can be eaten by livestock and poultry.

The relatively mature method for processing the feed by the kitchen waste comprehensively utilizes the granulation technology, the extrusion puffing technology, the drying technology and other means. The concentration of bacteria in the feed after extrusion was much lower than in the other samples. A single screw dry extrusion process can greatly reduce the concentration of potential pathogenic bacteria due to the constantly elevated temperatures used in extrusion. Some manufacturers develop matched technical equipment and put the equipment into operation.

The main problems of feed safety and homology are the problems of feed safety and homology, and the improvement of the disinfection requirement is bound to be correspondingly adjusted in the aspects of equipment, technology and the like, so that the treatment cost is increased, and in addition, the pollution to harmful organic matters, heavy metals and the like cannot be well solved and is not thoroughly harmless. Therefore, great care is taken in the selection of this technique.

Therefore, the current technology for treating kitchen waste and kitchen waste needs to be improved.

SUMMERY OF THE UTILITY MODEL

The present invention aims at solving at least one of the technical problems in the related art to a certain extent. Therefore, an object of the utility model is to provide a system of coprocessing kitchen garbage and food and beverage rubbish, this system can realize food and beverage rubbish and the garbage coprocessing of kitchen, and simple process is reasonable, the investment is low, and innoxious, resourceful, the minimizing of realization food and beverage rubbish and the garbage that remains in kitchen that can the maximize provide reference for china's organic rubbish coprocessing.

In one aspect of the present invention, the utility model provides a system for co-processing kitchen garbage and food and beverage garbage. According to the utility model discloses an embodiment, the system includes:

the kitchen waste pretreatment unit is provided with a kitchen waste inlet, a first leachate outlet, a first inorganic impurity outlet and a crushed kitchen waste outlet;

the food waste pretreatment unit is provided with a food waste inlet, a second inorganic impurity outlet, a third inorganic impurity outlet, a second leachate outlet, a grease outlet, a wastewater outlet and a food waste slurry outlet;

the mixing device is provided with a crushed kitchen waste inlet, a food and beverage waste slurry inlet and a mixed organic slurry outlet, the crushed kitchen waste inlet is connected with the crushed kitchen waste inlet, and the food and beverage waste slurry inlet is connected with the food and beverage waste slurry outlet;

the dry anaerobic fermentation device is provided with a mixed organic slurry inlet, a methane outlet and an anaerobic digestion liquid outlet, and the mixed organic slurry inlet is connected with the mixed organic slurry outlet through a scraper conveyor.

According to the system of coprocessing kitchen garbage and food and beverage garbage of the embodiment of the utility model, through passing food and beverage garbage and kitchen garbage respectively through respective pretreatment unit, kitchen garbage can separate leachate and inorganic impurity wherein after the pretreatment, and food and beverage garbage separates inorganic impurity and grease etc. wherein after the pretreatment, then supply the broken kitchen garbage that obtains after the pretreatment of kitchen garbage and food and beverage garbage slurry after the pretreatment to the mixing arrangement and mix, supply the mixed organic slurry that obtains to the dry anaerobic fermentation device and carry out anaerobic fermentation, make organic matter in the mixed organic slurry naturally degrade under anaerobic environment, obtain marsh gas and anaerobic digestion liquid, because general food and beverage garbage moisture content is higher, and the water content of kitchen garbage is lower than the food and beverage garbage, so coprocessing anaerobic fermentation adopts dry anaerobic digestion, can avoid food and beverage rubbish moisture content too high to lead to the easy layering of anaerobism and kitchen remains rubbish solid impurity more leads to the easy scheduling problem that blocks up of anaerobic device, full play anaerobic fermentation's technological advantage, improve anaerobic device's security and produce marsh gas efficiency, and dry-type anaerobic fermentation is less than wet-type anaerobic fermentation biogas production liquid volume, can reduce the natural pond liquid and handle a difficult problem, high temperature dry-type anaerobic fermentation organic load is high, it is high to produce marsh gas rate, the income of providing whole operation project, secondary pollution problems such as material crust can be avoided in dry-type anaerobic fermentation simultaneously. Therefore, by adopting the system, the cooperative treatment of the food waste and the kitchen waste can be realized, the process is simple and reasonable, the investment is low, the harmlessness, the reclamation and the reduction of the food waste and the kitchen waste can be realized to the maximum extent, and a reference is provided for the cooperative treatment of the organic waste in China.

In addition, according to the utility model discloses the system of coprocessing kitchen garbage and food and beverage rubbish of above-mentioned embodiment can also have following additional technical characterstic:

in some embodiments of the present invention, the kitchen garbage pretreatment unit includes: a refuse storage pit having the kitchen waste inlet, the first leachate outlet, and a post-stack leachate outlet; the drum sieve is provided with a material inlet after stacking and filtering, the first inorganic impurity outlet and an organic garbage outlet, and the material inlet after stacking and filtering is connected with the material outlet after stacking and filtering; the magnetic separator is provided with an organic garbage inlet, a metal outlet and a garbage outlet after magnetic separation, and the organic garbage inlet is connected with the organic garbage outlet; the shearing type crusher is provided with a magnetic separation rear garbage inlet and a crushing rear kitchen garbage outlet, and the magnetic separation rear garbage inlet is connected with the magnetic separation rear garbage outlet. Thus, the reduction treatment of the kitchen waste can be realized.

In some embodiments of the present invention, the food waste pretreatment unit comprises: the impurity separator is provided with the food waste inlet, the second inorganic impurity outlet and a separated material outlet; a crushing and sorting pulper, wherein the crushing and sorting pulper is provided with a separated material inlet, a water inlet, a third inorganic impurity inlet and an organic slurry outlet, the separated material inlet is connected with the separated material outlet, and the water inlet is connected with the first percolate outlet and the second percolate outlet; the cooking device is provided with an organic slurry inlet and a cooked material outlet, and the organic slurry inlet is connected with the organic slurry outlet; the three-phase separator is provided with a cooked material inlet, the grease outlet, the waste water outlet and the food waste slurry outlet, the cooked material inlet is connected with the cooked material outlet, and the waste water outlet is connected with the water inlet. Therefore, the reduction treatment of the food waste can be realized.

In some embodiments of the present invention, the system further comprises: the biogas purification device is internally provided with a biological packing layer and is provided with a first biogas inlet and a desulfurized biogas outlet, and the first biogas inlet is connected with the biogas outlet; the device comprises a marsh gas purification device, wherein the marsh gas purification device is provided with a desulfurized marsh gas inlet and a vehicle fuel gas outlet, and the desulfurized marsh gas inlet is connected with the desulfurized marsh gas outlet. Therefore, resource utilization of food waste and kitchen waste can be realized.

In some embodiments of the present invention, the system further comprises: the solid-liquid separation device is provided with an anaerobic digestion liquid inlet, a biogas residue outlet and a biogas liquid outlet, and the anaerobic digestion liquid inlet is connected with the anaerobic digestion liquid outlet; the sewage treatment device is provided with a biogas slurry inlet and a standard water outlet, and the biogas slurry inlet is connected with the biogas slurry outlet. Thus, environmental pollution can be avoided.

In some embodiments of the present invention, the system further comprises: the biogas boiler is provided with a second biogas inlet, a cooling water inlet, a heat exchange flue gas outlet and a steam outlet, the second biogas inlet is connected with the biogas outlet, and the steam outlet is connected with the cooking device. Therefore, the dependence of the system on external energy sources can be reduced.

Additional aspects and advantages of the invention will be set forth in part in the description which follows and, in part, will be obvious from the description, or may be learned by practice of the invention.

Drawings

The above and/or additional aspects and advantages of the present invention will become apparent and readily appreciated from the following description of the embodiments, taken in conjunction with the accompanying drawings of which:

FIG. 1 is a schematic structural diagram of a system for co-processing kitchen waste and food waste according to an embodiment of the present invention;

FIG. 2 is a schematic structural diagram of a system for co-processing kitchen waste and food waste according to yet another embodiment of the present invention;

FIG. 3 is a schematic structural diagram of a system for co-processing kitchen waste and food waste according to another embodiment of the present invention;

FIG. 4 is a schematic structural diagram of a system for co-processing kitchen waste and food waste according to another embodiment of the present invention;

FIG. 5 is a schematic structural diagram of a system for co-processing kitchen waste and food waste according to another embodiment of the present invention;

FIG. 6 is a schematic structural diagram of a system for co-processing kitchen waste and food waste according to another embodiment of the present invention;

FIG. 7 is a flow chart of a method for cooperatively processing kitchen waste and food waste implemented by the system for cooperatively processing kitchen waste and food waste according to an embodiment of the present invention;

FIG. 8 is a schematic flow chart of a method for co-processing kitchen waste and food waste implemented by a system for co-processing kitchen waste and food waste according to yet another embodiment of the present invention;

FIG. 9 is a schematic flow chart of a method for co-processing kitchen waste and food waste implemented by a system for co-processing kitchen waste and food waste according to another embodiment of the present invention;

FIG. 10 is a schematic flow chart of a method for co-processing kitchen waste and food waste implemented by a system for co-processing kitchen waste and food waste according to another embodiment of the present invention;

FIG. 11 is a flow chart of a method for co-processing kitchen waste and food waste implemented by a system for co-processing kitchen waste and food waste according to another embodiment of the present invention;

fig. 12 is a flow chart of a method for processing kitchen waste and food waste cooperatively according to another embodiment of the present invention.

Detailed Description

Reference will now be made in detail to embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the drawings are exemplary and intended to be used for explaining the present invention, and should not be construed as limiting the present invention.

In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", "axial", "radial", "circumferential", and the like, indicate the orientation or positional relationship based on the orientation or positional relationship shown in the drawings, and are only for convenience of description and simplicity of description, and do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention.

Furthermore, the terms "first", "second" and "first" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first" or "second" may explicitly or implicitly include at least one such feature. In the description of the present invention, "a plurality" means at least two, e.g., two, three, etc., unless specifically limited otherwise.

In the present invention, unless otherwise expressly stated or limited, the terms "mounted," "connected," and "fixed" are to be construed broadly and may, for example, be fixedly connected, detachably connected, or integrally formed; can be mechanically or electrically connected; they may be directly connected or indirectly connected through intervening media, or they may be connected internally or in any other suitable relationship, unless expressly stated otherwise. The specific meaning of the above terms in the present invention can be understood according to specific situations by those skilled in the art.

In the present application, unless expressly stated or limited otherwise, the first feature may be directly on or directly under the second feature or indirectly via intermediate members. Also, a first feature "on," "over," and "above" a second feature may be directly or diagonally above the second feature, or may simply indicate that the first feature is at a higher level than the second feature. A first feature being "under," "below," and "beneath" a second feature may be directly under or obliquely under the first feature, or may simply mean that the first feature is at a lesser elevation than the second feature.

In one aspect of the present invention, the utility model provides a system for co-processing kitchen garbage and food and beverage garbage. According to the utility model discloses an embodiment, refer to 1, this system includes: a kitchen waste pretreatment unit 100, a food waste pretreatment unit 200, a mixing device 300 and a dry anaerobic fermentation device 400.

According to the embodiment of the utility model provides a surplus rubbish pretreatment unit in kitchen 100 has surplus rubbish in kitchen entry 101, first filtration liquid export 102, first inorganic impurity export 103 and broken kitchen surplus rubbish export 104, and is suitable for and carries out the preliminary treatment to surplus rubbish in kitchen to obtain first filtration liquid, first inorganic impurity and broken kitchen surplus rubbish.

According to an embodiment of the present invention, referring to fig. 2, the kitchen garbage pretreatment unit 100 includes a garbage storage pit 11, a drum sieve 12, a magnetic separator 13, and a shear crusher 14.

According to the embodiment of the present invention, referring to fig. 2, the garbage storage pit 11 has a kitchen garbage inlet 101, a first leachate outlet 102 and a filtered material outlet 113. Specifically, kitchen garbage gets into between unloading after the measurement is weighed, unloads into rubbish pit 11, and kitchen garbage piles up in rubbish pit, then adopts grab bucket material loading to plate feeder, and the plate feeder lower part is equipped with the collecting tank, and kitchen garbage leachate can be collected to this collecting tank, collects the first leachate in the collecting tank and flows to the leachate collecting tank by oneself, and the material of piling up in the hopper after straining is carried by plate feeder and is got into the band conveyer, reentrant rotary screen 12 of follow-up workshop section behind even cloth.

According to the utility model discloses a specific embodiment, refer to fig. 2, trommel 12 has and piles after straining material entry 121, first inorganic impurity export 103 and organic rubbish export 123, pile after straining material entry 121 and pile after straining material export 113 and link to each other, and be suitable for the heap after straining that obtains to the aforesaid and sieve, the thing of oversize is bold plastics, paper and billet etc. be first inorganic impurity promptly, this first inorganic impurity sends to the system of burning and burns, and the thing of undersize that obtains gets into in follow-up magnet separator 13 for organic rubbish. Specifically, the drum sieve is provided with a 80mm single-stage sieve, and a bag breaking cutter structure is arranged in the drum sieve 12, so that the high bag breaking efficiency is achieved, and the loss of organic matters on the sieve caused by bag breakage can be effectively avoided.

According to the utility model discloses a specific embodiment, referring to fig. 2, magnet separator 13 has rubbish export 133 after organic rubbish entry 131, metal export 132 and the magnetic separation, and organic rubbish entry 131 links to each other with organic rubbish export 123, and is suitable for the organic rubbish that obtains in trommel screen 12 to carry out the magnetic separation, so that isolate the metal in the organic rubbish, rubbish supply to subsequent shear type breaker 14 after the remaining magnetic separation is handled.

According to the utility model discloses a specific embodiment, refer to fig. 2, shear type breaker 14 has rubbish entry 141 after the magnetic separation and the surplus rubbish export 104 in broken kitchen, and rubbish entry 141 links to each other with rubbish export 133 after the magnetic separation, and is suitable for the rubbish after the magnetic separation that obtains above-mentioned to cut the breakage, obtains the surplus rubbish in broken kitchen. Specifically, the shear type crusher 14 mainly depends on the principle of 'shearing and cutting' to complete the process of crushing kitchen garbage, the motor drives the speed reducer to transmit torque to the moving knife of the crusher through the knife roll shaft, the knife hook of the moving knife hooks the material to be torn downwards, the blades of the pair rollers cut the material like scissors, the crushing ratio is large, the discharge granularity is large, and the crushing effect on the tough material is good. And the shear type crusher 14 is different according to the design size of the blade, and the particle size of the crushed material can be different, so that the multistage crushing can be set as required to achieve the ideal particle size of the material.

According to the embodiment of the utility model, referring to fig. 1, food waste pretreatment unit 200 has food waste entry 201, second leachate export 207, second inorganic impurity export 202, third inorganic impurity export 203, grease export 204, waste water export 205 and food waste slurry export 206, and is suitable for and carries out the preliminary treatment to food waste to obtain second inorganic impurity, third inorganic impurity, second leachate, grease, waste water and food waste slurry.

According to an embodiment of the present invention, referring to fig. 3, the food waste pretreatment unit 200 includes an impurity separator 21, a crushing and sorting pulper 22, a cooking device 23 and a three-phase separator 24.

According to the specific embodiment of the utility model, referring to fig. 3, impurity separator 21 has food waste entry 201, second inorganic impurity export 202, second leachate export 207 and after-separation material export 213, and is suitable for separating food waste to obtain the second inorganic impurity, second leachate and the after-separation material that contain plastics, metal, glass of great particle diameter. Specifically, food and beverage rubbish gets into the factory through collecting and measures the back, with food and beverage rubbish through impurity separator, comes out the great plastics of particle diameter, metal, glass etc. impurity separation, and remaining after-separating material is supplied with to connecing in the hopper, and liquid in the after-separating material simultaneously is through connecing hopper bottom drainage spiral to drip second filtration liquid, flows into the filtration liquid collecting pit and keeps in. The area of the receiving hopper is sealed as much as possible to prevent the odor from overflowing, and the generated odor is led out by the induced draft fan and is sent to the deodorization system. Meanwhile, the impurity separator is arranged in front of the material receiving hopper, large substances in the food waste are removed in the front section, the blocking problem of the pretreatment unit conveying and crushing equipment is effectively avoided, and the impurity separator device is of a spiral structure and is free of winding, blocking and hanging. It should be noted that, a person skilled in the art can select an impurity separator with a specific structure according to actual needs, as long as effective separation of large materials such as glass bottles, trays, dishes, plastics and other impurities can be realized, and brittle impurities are not broken in the separation process (sand removal difficulty in subsequent processes is reduced, and abrasion of a conveying system is reduced). And connect the hopper to install in the discharge pit, it is more to unload the interior odor volume of producing of room, and the design adopts the infrared quick canvas rolling slats door of twice, prevents to unload to the greatest extent that interior odor is excessive. And a deodorizing pipeline collection air port and a plant liquid spraying system are arranged in the discharging room, so that the air freshness of the discharging area is ensured. The top of the receiving hopper adopts a sealing design, and the cover plate of the discharging opening is interlocked with the infrared quick rolling shutter door between the discharging. The top of the receiving hopper is provided with an exhaust port, and odor is collected under negative pressure and then sent to a deodorization system to prevent the odor from overflowing. The screw conveyor at the bottom of the receiving hopper adopts a double-screw design, so that smooth conveying of materials is guaranteed. The contact part of the screw conveyer and the material is made of 304 stainless steel, so that the corrosion resistance of the equipment is ensured.

According to the specific embodiment of the utility model, refer to fig. 3, broken separating pulping machine 22 has after-separation material entry 221, water entry 222, third inorganic impurity entry 203 and organic thick liquids export 223, after-separation material entry 221 links to each other with after-separation material export 213, water entry 222 links to each other with first filtration liquid export 102 and second filtration liquid export 207, and be suitable for carrying out the slurrying after the broken separation of above-mentioned after-separation material and first filtration liquid and second filtration liquid that obtains, so that separate the third inorganic impurity such as metal in the after-separation material, plastics, bamboo wood chopsticks, bone, and the organic thick liquids that obtains are supplied to in subsequent cooking device 23. The crushing and sorting pulping machine adopts totally enclosed mechanical continuous operation, can efficiently remove light substances and fragile and non-fragile substances, and can effectively solve the problem that food and beverage garbage is difficult to treat due to high viscosity and more impurities. The crushing and sorting pulping machine integrates material crushing, pulping and impurity sorting, and has the advantages of high automation degree, compact structure and complete functions. Equipment and material contact part all adopt stainless steel, and corrosion resistance is strong, and the quartering hammer adopts alloy material, and intensity is high, and the wearability is good to this application supplies with the broken pulping machine of selecting separately in the first filtration liquid that obtains of above-mentioned kitchen garbage pretreatment and the second filtration liquid that obtains behind the food and beverage rubbish pretreatment, has not only saved the supply of external running water, realizes the utilization of the resourceful utilization of filtration liquid moreover.

According to the specific embodiment of the present invention, referring to fig. 3, the cooking device 23 has an organic slurry inlet 231 and a cooked material outlet 232, the organic slurry inlet 231 is connected to the organic slurry outlet 223, and is suitable for cooking the organic slurry obtained above, so as to obtain the cooked material. Specifically, the grease content of the food waste is high, if the food waste is not separated, the food waste enters a subsequent dry anaerobic fermentation device, the long-chain fatty acid poisoning of anaerobic bacteria can be caused, so that the treatment effect of anaerobic digestion is influenced, and most of grease in the food waste must be separated. The grease in the food waste mainly exists in the forms of floating oil, dispersed oil, emulsified oil, solid internal oil and the like. The floatable oil drops have larger particle size and can be separated in an upward floating manner by standing, and the effect of the dispersed oil, the emulsified oil and the oil in the solid is poorer by utilizing a common gravity separation method, and the boiling device is arranged to heat the organic slurry in the boiling device to 65-70 ℃, so that most of the oil contained in the organic slurry can be converted into the floatable oil, and the separation of the follow-up oil is facilitated.

According to the specific embodiment of the utility model, referring to fig. 3, three-phase separator 24 has the back of cooking material entry 241, grease export 204, waste water export 205 and food and beverage rubbish thick liquids export 206, the back of cooking material entry 241 links to each other with the back of cooking material export 232, waste water export 205 links to each other with water entry 222, and is suitable for the back of cooking material that obtains to the aforesaid and carries out the three-phase separation, so that the separation obtains grease, waste water and food and beverage rubbish thick liquids, and return a part of the waste water after the separation to broken sorting pulper 22 and participate in the slurrying. Specifically, the grease in the cooked material is separated by utilizing the high-speed centrifugal principle of a three-phase separator, the grease is stored and sold out periodically, and meanwhile, the grease content requirement before the organic slurry enters a subsequent dry anaerobic fermentation device 400 is ensured. And a part of the separated waste water returns to the crushing and sorting pulping machine 22 to participate in pulping, and the rest waste water is mixed with the solid materials separated in the three-phase separator 24 to prepare the pulp, so that the food waste pulp is obtained.

According to the embodiment of the utility model, refer to fig. 1, mixing arrangement 300 has broken kitchen garbage entry 301, food and beverage rubbish thick liquids entry 302 and mixed organic thick liquids export 303, broken kitchen garbage entry 301 links to each other with broken kitchen garbage entry 104, food and beverage rubbish thick liquids entry 302 links to each other with food and beverage rubbish thick liquids export 206, and be suitable for the food and beverage rubbish thick liquids that the broken kitchen garbage that obtains of the above-mentioned kitchen garbage preprocessing unit 100 and the above-mentioned food and beverage rubbish preprocessing unit 200 obtained to mix, obtain mixed organic thick liquids. Preferably, the mass ratio of the crushed kitchen waste to the food waste slurry is not less than 1.53. The inventor finds that if the mass ratio of the kitchen waste after the crushing treatment to the food waste slurry is lower than 1.53, the reaction condition of dry anaerobic fermentation cannot be met, and only semi-dry anaerobic fermentation or even wet anaerobic fermentation can be carried out, so that dry anaerobic cooperative treatment of the kitchen waste and the food waste cannot be realized, and by controlling the mass ratio of the kitchen waste after the crushing treatment to the food waste slurry to be not lower than 1.53, the feeding condition can be ensured to meet the reaction condition of the dry anaerobic fermentation, the problems that the food waste is easy to stratify due to overhigh water content and the anaerobic device is easy to block due to more solid impurities in the kitchen waste can be avoided, the process advantages of the dry anaerobic fermentation can be fully exerted, and the safety and the biogas production efficiency of the anaerobic device can be improved.

According to the embodiment of the present invention, the dry anaerobic fermentation device 400 has the mixed organic slurry inlet 401, the biogas outlet 402 and the anaerobic digestion liquid outlet 403, the mixed organic slurry inlet 401 is connected with the mixed organic slurry outlet 303 through the scraper conveyor 41, and the mixed organic slurry obtained in the mixing device 300 is supplied to the dry anaerobic fermentation device 400 by the scraper conveyor 41 for anaerobic fermentation, so as to obtain biogas and anaerobic digestion liquid. The inventor finds that organic slurry obtained by mixing broken kitchen waste obtained by pretreating kitchen waste and restaurant waste slurry obtained by pretreating restaurant waste is supplied to a dry anaerobic fermentation device for anaerobic fermentation, so that organic matters in the mixed organic slurry are naturally degraded in an anaerobic environment to obtain biogas and anaerobic digestion liquid, the dry anaerobic digestion is adopted in cooperation with anaerobic fermentation because the water content of common restaurant waste is higher and the water content of the kitchen waste is lower than that of the restaurant waste, the problems that the restaurant waste is easy to stratify due to overhigh water content of the restaurant waste and the anaerobic device is easy to block due to more solid impurities in the kitchen waste can be solved, the technological advantages of the anaerobic fermentation are fully played, the safety and biogas production efficiency of the anaerobic device are improved, the biogas production amount of biogas liquid is less in the dry anaerobic fermentation than that in the wet anaerobic fermentation, and the biogas liquid treatment problem can be reduced, the high-temperature dry anaerobic fermentation has high organic load and high biogas production rate, provides the benefit of the whole operation project, and simultaneously can avoid the secondary pollution problems of material incrustation and the like by dry anaerobic fermentation.

Specifically, the solid content of mixed organic slurry obtained by mixing the food waste slurry obtained by pretreating food waste and the broken kitchen waste obtained by pretreating kitchen waste is greater than 20 wt%, and blockage faults easily occur by adopting a screw pump, a slurry pump and the like.

After the mixed organic slurry obtained by mixing the food waste slurry obtained by pretreating food waste and the crushed kitchen waste obtained by pretreating kitchen waste is sent into a dry anaerobic fermentation device through a plate conveyor, biodegradation is carried out in a closed environment, organic matter is biodegraded and methane is generated in the dry anaerobic fermentation device in about 20 days, and the remainder after anaerobic fermentation is anaerobic digestion liquid. And the dry anaerobic fermentation tank is of a reinforced concrete structure, and is constructed in civil engineering on site. The fermentation device is internally provided with a stirrer, so that the materials in the fermentation device are uniformly stirred. Meanwhile, the fermentation temperature is controlled to be 50-60 ℃, the fermentation temperature is preferably 55 ℃, the dry anaerobic fermentation device adopts a coil pipe heating mode, and meanwhile, the heat preservation measure is adopted on the outer wall, so that the heat loss is reduced. Meanwhile, an online instrument is arranged in the dry anaerobic fermentation device, parameters such as material height, temperature, pH, methane pressure and the like in the dry anaerobic fermentation device are monitored in real time, and the stable operation of the anaerobic fermentation device is ensured.

According to the system of coprocessing kitchen garbage and food and beverage garbage of the embodiment of the utility model, through passing food and beverage garbage and kitchen garbage respectively through respective pretreatment unit, kitchen garbage can separate leachate and inorganic impurity wherein after the pretreatment, and food and beverage garbage separates inorganic impurity and grease etc. wherein after the pretreatment, then supply the broken kitchen garbage that obtains after the pretreatment of kitchen garbage and food and beverage garbage slurry after the pretreatment to the mixing arrangement and mix, supply the mixed organic slurry that obtains to the dry anaerobic fermentation device and carry out anaerobic fermentation, make organic matter in the mixed organic slurry naturally degrade under anaerobic environment, obtain marsh gas and anaerobic digestion liquid, because general food and beverage garbage moisture content is higher, and the water content of kitchen garbage is lower than the food and beverage garbage, so coprocessing anaerobic fermentation adopts dry anaerobic digestion, can avoid food and beverage rubbish moisture content too high to lead to the easy layering of anaerobism and kitchen remains rubbish solid impurity more leads to the easy scheduling problem that blocks up of anaerobic device, full play anaerobic fermentation's technological advantage, improve anaerobic device's security and produce marsh gas efficiency, and dry-type anaerobic fermentation is less than wet-type anaerobic fermentation biogas production liquid volume, can reduce the natural pond liquid and handle a difficult problem, high temperature dry-type anaerobic fermentation organic load is high, it is high to produce marsh gas rate, the income of providing whole operation project, secondary pollution problems such as material crust can be avoided in dry-type anaerobic fermentation simultaneously. Therefore, by adopting the system, the cooperative treatment of the food waste and the kitchen waste can be realized, the process is simple and reasonable, the investment is low, the harmlessness, the reclamation and the reduction of the food waste and the kitchen waste can be realized to the maximum extent, and a reference is provided for the cooperative treatment of the organic waste in China.

Further, referring to fig. 4, the system for cooperatively treating kitchen waste and food waste further includes a biogas purification device 500 and a biogas purification device 600.

According to the embodiment of the present invention, a bio-packing layer (not shown) is disposed in the biogas purification apparatus 500, and the biogas purification apparatus 500 has a first biogas inlet 501 and a desulfurized biogas outlet 502, the first biogas inlet 501 is connected to the biogas outlet 402, and is adapted to purify a part of the biogas obtained in the dry anaerobic fermentation apparatus 400, so as to facilitate the purification of the biogasObtaining the desulfurized biogas. Specifically, the biogas purification device comprises a biological desulfurization tower and a dry-method desulfurization device which are sequentially connected, biogas generated by the dry-type anaerobic fermentation device is firstly sent to the biological desulfurization tower, and a biological filler layer with high porosity, high buffering capacity and high water holding capacity is filled in the biological desulfurization tower, so that microorganisms with desulfurization characteristics can be attached to and grow on the biological desulfurization tower. And nutrient solution is arranged in the biological desulfurization tower for cyclic spraying, and microorganisms and nutrient elements rich in the nutrient solution are utilized to culture desulfurization floras, so that H in the biogas₂S is oxidized to S and further oxidized to S₂O₃ ^2-、SO₄ ^2-And the products are obtained, thereby achieving the removal of H₂Purpose of S, and biological desulfurizing tower can be used for removing H from marsh gas₂The S concentration is reduced from 2500ppm to 200ppm, and the biogas treated by the biological desulfurization tower is subjected to dry desulfurization by a dry desulfurization device, wherein the dry desulfurization is realized by filling a desulfurizer with a certain height in desulfurization equipment, the biogas passing through the biological desulfurization tower passes through the desulfurizer from bottom to top, and H passes through the desulfurizer from bottom to top₂S is removed to realize the desulfurization process, wherein the desulfurizer takes ferric oxide as a main active catalytic component, and is added with a plurality of catalyst promoters and carriers to remove H under the catalysis at normal temperature and normal pressure₂S, the desulfurization rate can reach more than 90 percent, and H in the biogas after biological desulfurization can be removed₂S is further reduced to below 7.5 ppm. It should be noted that, those skilled in the art can select the bio-filler layer and the desulfurization flora according to actual needs, as long as the above desulfurization function is achieved. The dry desulfurization continuous regeneration process has the characteristics of high sulfur capacity, small bed resistance, convenient operation, continuous regeneration, simple regeneration process and the like. The desulfurization regeneration process principle is as follows:

and (3) desulfurization: fe₂O₃·H₂O+3H₂S＝Fe₂S₃·H₂O+3H₂O

Regeneration: 2Fe₂S₃·H₂O+3O₂＝2Fe₂O₃·H₂O+6S

By combining the two reaction formulas, the desulfurization regeneration reaction formula is as follows: h₂S+1/2O₂＝S+H₂O (reaction conditions are Fe)₂O₃·H₂O). . It should be noted that, those skilled in the art can select the bio-filler layer and the desulfurization flora according to actual needs, as long as the above desulfurization function is achieved.

According to the utility model discloses an embodiment, marsh gas purification device 600 has desulfurization back marsh gas entry 601 and vehicle gas export 602, and desulfurization back marsh gas entry 601 links to each other with desulfurization back marsh gas export 502, and is suitable for the desulfurization back marsh gas that obtains to the aforesaid and carries out purification treatment to obtain vehicle gas. Specifically, the biogas purification device 600 is a membrane purification device, the obtained desulfurized biogas is firstly pretreated to remove particles, moisture, oil substances and the like in the biogas, and when the biogas enters the membrane purification device, the biogas reaches the air inlet requirement (the pressure is 2-3 Kpa, the temperature is less than 55 ℃; CH₄55 to 65 volume percent; CO 2₂35 to 45 volume percent; h₂S＜7.5mg/Nm³；H₂O50-100% RH; note: the standard reference condition of gas volume in the standard is 101.325kPa, 20 ℃) and then is supplied to membrane purification equipment, a membrane component carries out coarse decarburization and fine decarburization on methane, CH is finally generated after membrane purification₄The natural gas product with the purity higher than 97 percent can remove water in the methane by the membrane component, and finally the dew point of the biological gas can completely meet the dew point requirement of the vehicle gas. The waste gas separated by membrane purification can be directly discharged, and CO can also be discharged₂And (3) recycling, enabling the biogas with the purity higher than 97% to enter a CNG compressor system, raising the pressure to 25MPa through a compressor to reach the pressure standard of the vehicle fuel gas, adding the biogas into a skid-mounted vehicle through a gas filling column, and selling or transporting the biogas to peripheral gas filling stations for use. The membrane module is the core of the whole membrane purification equipment, and the carbon dioxide reaches the design output requirement after passing through the second-stage hollow fiber membrane module. The outer exhaust gas of the system is discharged in the first-stage membrane group to become exhaust gas. After passing through the secondary membrane group, the exhaust gas of the secondary membrane group returns to the pressure stabilizing buffer tank through backflow to complete closed circulation. The working principle of the hollow fiber membrane is that different gas molecules are separated through different permeation rates of different gases in the high polymer material hollow fiber membrane. Wherein the penetration rate isThe gas having a high permeation rate is called "fast gas", and the gas having a low permeation rate is called "slow gas". The fast gas is permeated fast, most of the fast gas is concentrated at one end of the gas inlet, and a small part of the fast gas penetrates to one end of the gas outlet; the "slow gas" penetrates slowly so that most of it penetrates the membrane module to the exhaust port end and a small portion is concentrated at the intake port end. The water, hydrogen sulfide, carbon dioxide and oxygen in the biogas are all 'fast gas', while the nitrogen and methane are 'slow gas'. Therefore, the selective permeation adsorption characteristic of the membrane module determines that the membrane method methane purification can remove a large amount of carbon dioxide and can remove part of hydrogen sulfide and oxygen impurities.

Further, referring to fig. 5, the system for cooperatively processing kitchen waste and food waste further includes: a solid-liquid separation device 700 and a sewage treatment device 800.

According to the embodiment of the utility model, solid-liquid separation device 700 has anaerobic digestion liquid entry 701, natural pond sediment export 702 and natural pond liquid export 703, and anaerobic digestion liquid entry 701 links to each other with anaerobic digestion liquid export 403, and is suitable for the anaerobic digestion liquid that obtains in the above-mentioned dry-type anaerobic fermentation device 400 to carry out solid-liquid separation, obtains natural pond sediment and natural pond liquid. Specifically, the solid-liquid separation device 700 is a two-phase horizontal screw centrifuge, the anaerobic digestion liquid generated by the dry anaerobic fermentation device 400 is pumped to the two-phase horizontal screw centrifuge, the two-phase horizontal screw centrifuge utilizes the density difference of the two phases of solid and liquid, under the action of the centrifuge, the sedimentation speed of solid phase particles is accelerated to realize solid-liquid separation, the separation process is that the anaerobic digestion liquid added with a flocculating agent (for example, PAM or ferric salt) is sent to a mixing cavity in a rotary drum of the two-phase horizontal screw centrifuge through an inlet pipeline, due to the high-speed rotation and friction resistance of the rotor, the anaerobic digestion liquid is accelerated in the rotor and forms a cylindrical liquid ring layer, under the action of centrifugal force, the solid particles with larger specific gravity are settled to the inner wall of the rotary drum to form a mud layer, then the solid phase is pushed to a conical end by utilizing the relative speed difference of a screw and the rotary drum, the mud residue is dehydrated, and supernatant is discharged from the large end of the rotary drum to realize solid-liquid separation, biogas residues containing 80% of water generated by the solid-liquid separation are sent to an incineration plant to be incinerated, and the generated biogas slurry is pumped to a subsequent sewage treatment device 800 to be treated.

According to the utility model discloses an embodiment, sewage treatment plant 800 has natural pond liquid entry 801 and water outlet 802 up to standard, and natural pond liquid entry 801 links to each other with natural pond liquid export 703, and is suitable for and purifies natural pond liquid, realizes the discharge to reach standard of waste water. It should be noted that, those skilled in the art can select specific operations in the purification process according to actual needs, as long as the standard discharge of biogas slurry can be achieved, and details are not described herein.

Further, referring to fig. 6, the system for cooperatively processing kitchen waste and food waste further includes: the biogas boiler 900 is provided with a second biogas inlet 901, a cooling water inlet 902, a heat exchange flue gas outlet 903 and a steam outlet 904, the second biogas inlet 901 is connected with the biogas outlet 402, the steam outlet 904 is connected with the cooking device 23, and the biogas boiler 900 is suitable for burning another part of the biogas obtained by the dry anaerobic fermentation device 400 and then exchanging heat with the cooling water to obtain heat exchange flue gas and steam, and supplying the steam to the cooking device 23 to be used as a heat source for heating the organic slurry.

For the convenience of understanding, the following describes a method for implementing the cooperative treatment of kitchen waste and food waste by using the above system. According to an embodiment of the present invention, referring to fig. 7, the method includes:

s100: feeding the kitchen waste into a kitchen waste pretreatment unit for pretreatment

In the step, the kitchen waste is supplied to a kitchen waste pretreatment unit for pretreatment so as to obtain a first leachate, a first inorganic impurity and crushed kitchen waste.

According to an embodiment of the present invention, referring to fig. 8, step S100 is performed according to the following steps:

s110: supplying kitchen garbage to garbage storage pit for stacking and filtering

In the step, the kitchen waste is supplied to a waste storage pit for heap filtration so as to obtain a first leachate and a heap-filtered material. Specifically, kitchen garbage gets into between unloading after the measurement is weighed, unloads into rubbish pit 11, and kitchen garbage piles up in rubbish pit, then adopts grab bucket material loading to plate feeder, and the plate feeder lower part is equipped with the collecting tank, and kitchen garbage leachate can be collected to this collecting tank, collects the leachate in the collecting tank and flows to the leachate collecting tank by oneself, and the material of piling up in the hopper is carried by plate feeder and is got into the belt conveyor, reentrant rotary screen 12 of follow-up workshop section behind the even cloth.

S120: feeding the piled and filtered materials into a drum screen for screening

In this step, the material after the filtering is supplied to a drum screen for screening, the oversize products are large plastic, paper, wood blocks and the like, which are the first inorganic impurities, the first inorganic impurities are sent to an incineration system for incineration, and the obtained undersize products are organic garbage and enter a subsequent magnetic separator 13. Specifically, the drum sieve is provided with a 80mm single-stage sieve, and a bag breaking cutter structure is arranged in the drum sieve 12, so that the high bag breaking efficiency is achieved, and the loss of organic matters on the sieve caused by bag breakage can be effectively avoided.

S130: organic garbage is supplied to a magnetic separator for magnetic separation

In this step, the organic waste obtained above is supplied to a magnetic separator for magnetic separation so as to separate metals from the organic waste, and the remaining magnetic separated waste is supplied to a subsequent shear crusher 14 for treatment.

S140: feeding the magnetically separated garbage to a shearing type crusher for shearing and crushing

In the step, the obtained magnetically separated garbage is supplied to a shear type crusher for shearing and crushing so as to obtain the crushed kitchen garbage. Specifically, the shear type crusher 14 mainly depends on the principle of 'shearing and cutting' to complete the process of crushing kitchen garbage, the motor drives the speed reducer to transmit torque to the moving knife of the crusher through the knife roll shaft, the knife hook of the moving knife hooks the material to be torn downwards, the blades of the pair rollers cut the material like scissors, the crushing ratio is large, the discharge granularity is large, and the crushing effect on the tough material is good. And the shear type crusher 14 is different according to the design size of the blade, and the particle size of the crushed material can be different, so that the multistage crushing can be set as required to achieve the ideal particle size of the material.

S200: food waste is supplied to a food waste pretreatment unit for pretreatment

In the step, the food waste is supplied to the food waste pretreatment unit for pretreatment so as to obtain second inorganic impurities, third inorganic impurities, second leachate, grease, wastewater and food waste slurry.

According to an embodiment of the present invention, referring to fig. 9, step S200 is performed according to the following steps:

s210: food waste is supplied to an impurity separator for separation

In the step, the food waste is supplied to an impurity separator for separation so as to obtain second inorganic impurities containing plastics, metals, glass and the like with larger grain sizes, second leachate and separated materials. Specifically, food and beverage rubbish gets into the factory through collecting and measures the back, with food and beverage rubbish through impurity separator, comes out the great plastics of particle diameter, metal, glass etc. impurity separation, and remaining after-separating material is supplied with to connecing in the hopper, and liquid in the after-separating material simultaneously is through connecing hopper bottom drainage spiral to drip second filtration liquid, flows into the filtration liquid collecting pit and keeps in. The area of the receiving hopper is sealed as much as possible to prevent the odor from overflowing, and the generated odor is led out by the induced draft fan and is sent to the deodorization system. Meanwhile, the impurity separator is arranged in front of the material receiving hopper, large substances in the food waste are removed in the front section, the blocking problem of the pretreatment unit conveying and crushing equipment is effectively avoided, and the impurity separator device is of a spiral structure and is free of winding, blocking and hanging. It should be noted that, a person skilled in the art can select an impurity separator with a specific structure according to actual needs, as long as effective separation of large materials such as glass bottles, trays, dishes, plastics and other impurities can be realized, and brittle impurities are not broken in the separation process (sand removal difficulty in subsequent processes is reduced, and abrasion of a conveying system is reduced). And connect the hopper to install in the discharge pit, it is more to unload the interior odor volume of producing of room, and the design adopts the infrared quick canvas rolling slats door of twice, prevents to unload to the greatest extent that interior odor is excessive. And a deodorizing pipeline collection air port and a plant liquid spraying system are arranged in the discharging room, so that the air freshness of the discharging area is ensured. The top of the receiving hopper adopts a sealing design, and the cover plate of the discharging opening is interlocked with the infrared quick rolling shutter door between the discharging. The top of the receiving hopper is provided with an exhaust port, and odor is collected under negative pressure and then sent to a deodorization system to prevent the odor from overflowing. The screw conveyor at the bottom of the receiving hopper adopts a double-screw design, so that smooth conveying of materials is guaranteed. The contact part of the screw conveyer and the material is made of 304 stainless steel, so that the corrosion resistance of the equipment is ensured.

S220: the separated material, the first percolate and the second percolate are supplied to a crushing and sorting pulping machine to be crushed and sorted and then pulped

In this step, the separated material obtained as described above, the first leachate and the second leachate are supplied to a crushing and sorting pulper to be crushed and sorted and then pulped, so that the third inorganic impurities such as metal, plastic, bamboo, chopsticks, bones and the like in the separated material are separated, and the obtained organic slurry is supplied to the subsequent cooking device 23. The crushing and sorting pulping machine adopts totally enclosed mechanical continuous operation, can efficiently remove light substances and fragile and non-fragile substances, and can effectively solve the problem that food and beverage garbage is difficult to treat due to high viscosity and more impurities. The crushing and sorting pulping machine integrates material crushing, pulping and impurity sorting, and has the advantages of high automation degree, compact structure and complete functions. Equipment and material contact part all adopt stainless steel, and corrosion resistance is strong, and the quartering hammer adopts alloy material, and intensity is high, and the wearability is good to this application supplies with the broken pulping machine of selecting separately in the first filtration liquid that obtains of above-mentioned kitchen garbage pretreatment and the second filtration liquid that obtains behind the food and beverage rubbish pretreatment, has not only saved the supply of external running water, realizes the utilization of the resourceful utilization of filtration liquid moreover.

S230: feeding the organic slurry to a cooking device for cooking

In this step, the organic slurry is supplied to a cooking device and cooked to obtain a cooked material. Specifically, the grease content of the food waste is high, if the food waste is not separated, the food waste enters a subsequent dry anaerobic fermentation device, the long-chain fatty acid poisoning of anaerobic bacteria can be caused, so that the treatment effect of anaerobic digestion is influenced, and most of grease in the food waste must be separated. The grease in the food waste mainly exists in the forms of floating oil, dispersed oil, emulsified oil, solid internal oil and the like. The floatable oil drops have larger particle size and can be separated in an upward floating manner by standing, and the effect of the dispersed oil, the emulsified oil and the oil in the solid is poorer by utilizing a common gravity separation method, and the boiling device is arranged to heat the organic slurry in the boiling device to 65-70 ℃, so that most of the oil contained in the organic slurry can be converted into the floatable oil, and the separation of the follow-up oil is facilitated.

S240: the cooked material is supplied to a three-phase separator for separation, and the waste water is supplied to step S220

In this step, the cooked material obtained above is supplied to a three-phase separator to perform three-phase separation so as to separate oil, wastewater and food waste slurry, and the separated wastewater is returned to the crushing and sorting pulping machine 22 of step S220 to participate in pulping. Specifically, the grease in the cooked material is separated by utilizing the high-speed centrifugal principle of a three-phase separator, the grease is stored and sold out periodically, and meanwhile, the grease content requirement before the organic slurry enters a subsequent dry anaerobic fermentation device 400 is ensured. And a part of the separated waste water returns to the crushing and sorting pulping machine 22 to participate in pulping, and the rest waste water is mixed with the solid materials separated in the three-phase separator 24 to prepare the pulp, so that the food waste pulp is obtained.

S300: feeding the crushed kitchen garbage and the food and beverage garbage slurry to a mixing device for mixing

In this step, the crushed kitchen waste obtained by the kitchen waste pretreatment unit 100 in the step S100 and the food waste slurry obtained by the food waste pretreatment unit 200 in the step S200 are supplied to the mixing device 300 and mixed to obtain a mixed organic slurry. Preferably, the mass ratio of the crushed kitchen waste to the food waste slurry is not less than 1.53. The inventor finds that if the mass ratio of the kitchen waste after the crushing treatment to the food waste slurry is lower than 1.53, the reaction condition of dry anaerobic fermentation cannot be met, and only semi-dry anaerobic fermentation or even wet anaerobic fermentation can be carried out, so that dry anaerobic cooperative treatment of the kitchen waste and the food waste cannot be realized, and by controlling the mass ratio of the kitchen waste after the crushing treatment to the food waste slurry to be not lower than 1.53, the feeding condition can be ensured to meet the reaction condition of the dry anaerobic fermentation, the problems that the food waste is easy to stratify due to overhigh water content and the anaerobic device is easy to block due to more solid impurities in the kitchen waste can be avoided, the process advantages of the dry anaerobic fermentation can be fully exerted, and the safety and the biogas production efficiency of the anaerobic device can be improved.

S400: feeding the mixed organic slurry to a dry anaerobic fermentation device for anaerobic fermentation treatment

In this step, the mixed organic slurry obtained as described above is supplied to the dry anaerobic fermentation apparatus 400 to be subjected to anaerobic fermentation treatment, so that biogas and anaerobic digestion liquid are obtained. The inventor finds that organic slurry obtained by mixing broken kitchen waste obtained by pretreating kitchen waste and solid residues obtained by pretreating food waste is supplied to a dry anaerobic fermentation device for anaerobic fermentation, so that organic matters in the mixed organic slurry are naturally degraded in an anaerobic environment to obtain methane and anaerobic digestion liquid, the dry anaerobic digestion is adopted in cooperation with the anaerobic fermentation because the water content of common food waste is higher and the water content of the kitchen waste is lower than that of the food waste, the problems that the food waste is easy to stratify due to overhigh water content of the food waste and the anaerobic device is easy to block due to more solid impurities in the food waste can be solved, the technological advantages of the anaerobic fermentation are fully played, the safety and the methane production efficiency of the anaerobic device are improved, the biogas liquid yield is less in dry anaerobic fermentation compared with wet anaerobic fermentation, the biogas liquid treatment problem can be reduced, and the organic load of high-temperature anaerobic dry fermentation is high, the biogas production rate is high, the income of the whole operation project is provided, and meanwhile, the dry anaerobic fermentation can avoid the secondary pollution problems such as material crusting and the like.

Specifically, the solid content of mixed organic slurry obtained by mixing the food waste slurry obtained by pretreating food waste and the broken kitchen waste obtained by pretreating kitchen waste is greater than 20 wt%, and blockage faults easily occur by adopting a screw pump, a slurry pump and the like.

After the mixed organic slurry obtained by mixing the food waste slurry obtained by pretreating food waste and the crushed kitchen waste obtained by pretreating kitchen waste is sent into a dry anaerobic fermentation device through a plate conveyor, biodegradation is carried out in a closed environment, organic matter is biodegraded and methane is generated in the dry anaerobic fermentation device in about 20 days, and the remainder after anaerobic fermentation is anaerobic digestion liquid. And the dry anaerobic fermentation tank is of a reinforced concrete structure, and is constructed in civil engineering on site. The fermentation device is internally provided with a stirrer, so that the materials in the fermentation device are uniformly stirred. Meanwhile, the fermentation temperature is controlled to be 50-60 ℃, the fermentation temperature is preferably 55 ℃, the dry anaerobic fermentation device adopts a coil pipe heating mode, and meanwhile, the heat preservation measure is adopted on the outer wall, so that the heat loss is reduced. Meanwhile, an online instrument is arranged in the dry anaerobic fermentation device, parameters such as material height, temperature, pH, methane pressure and the like in the dry anaerobic fermentation device are monitored in real time, and the stable operation of the anaerobic fermentation device is ensured.

According to the embodiment of the utility model, food and beverage rubbish and food and beverage rubbish coprocessing method, through with food and beverage rubbish and food and beverage rubbish respectively through respective pretreatment unit, food and beverage rubbish can separate filtration liquid and inorganic impurity wherein after the pretreatment, and food and beverage rubbish separates inorganic impurity and grease etc. wherein after the pretreatment, then supply the broken food and beverage rubbish thick liquids that obtains after the pretreatment of food and beverage rubbish to the mixing arrangement and mix, supply the organic thick liquids that obtains to dry anaerobic fermentation device and carry out anaerobic fermentation, make organic matter in the organic thick liquids of mixing degrade naturally under anaerobic environment, obtain marsh gas and anaerobic digestion liquid, because general food and beverage rubbish moisture content is higher, and food and beverage rubbish moisture content is low relatively, so the dry anaerobic digestion is adopted in the coprocessing anaerobic fermentation, can avoid food and beverage rubbish moisture content too high to lead to the easy layering of anaerobism and kitchen remains rubbish solid impurity more leads to the easy scheduling problem that blocks up of anaerobic device, full play anaerobic fermentation's technological advantage, improve anaerobic device's security and produce marsh gas efficiency, and dry-type anaerobic fermentation is less than wet-type anaerobic fermentation biogas production liquid volume, can reduce the natural pond liquid and handle a difficult problem, high temperature dry-type anaerobic fermentation organic load is high, it is high to produce marsh gas rate, the income of providing whole operation project, secondary pollution problems such as material crust can be avoided in dry-type anaerobic fermentation simultaneously. Therefore, by adopting the method, the cooperative treatment of the food waste and the kitchen waste can be realized, the process is simple and reasonable, the investment is low, the harmlessness, the reclamation and the reduction of the food waste and the kitchen waste can be realized to the maximum extent, and a reference is provided for the cooperative treatment of the organic waste in China.

Further, referring to fig. 10, the method for co-processing kitchen garbage and food and beverage garbage further includes

S500: a part of the biogas is supplied to a biogas purification device containing a biological packing layer

In this step, a part of the biogas obtained in the above step S400 is supplied to a biogas purification apparatus containing a bio-filler layer and purified to obtain a desulfurized biogas. Specifically, the biogas purification device comprises a biological desulfurization tower and a dry-method desulfurization device which are sequentially connected, biogas generated by the dry-type anaerobic fermentation device is firstly sent to the biological desulfurization tower, and a biological filler layer with high porosity, high buffering capacity and high water holding capacity is filled in the biological desulfurization tower, so that microorganisms with desulfurization characteristics can be attached to and grow on the biological desulfurization tower. And nutrient solution is arranged in the biological desulfurization tower for cyclic spraying, and microorganisms and nutrient elements rich in the nutrient solution are utilized to culture desulfurization floras, so that H in the biogas₂S is oxidized to S and further oxidized to S₂O₃ ^2-、SO₄ ^2-And the products are obtained, thereby achieving the removal of H₂Purpose of S, and biological desulfurizing tower can be used for removing H from marsh gas₂The S concentration is reduced from 2500ppm to 200ppm, and the biogas treated by the biological desulfurization tower is subjected to dry desulfurization by a dry desulfurization device, wherein the dry desulfurization is realized by filling a desulfurizer with a certain height in desulfurization equipment, the biogas passing through the biological desulfurization tower passes through the desulfurizer from bottom to top, and H passes through the desulfurizer from bottom to top₂S is removed to realize the desulfurization process, wherein the desulfurizer takes ferric oxide as a main active catalytic component, and is added with a plurality of catalyst promoters and carriers to remove H under the catalysis at normal temperature and normal pressure₂S, the desulfurization rate can reach more than 90 percent, and H in the biogas after biological desulfurization can be removed₂S is further reduced to below 7.5 ppm. It should be noted that, those skilled in the art can select the bio-filler layer and the desulfurization flora according to actual needs, as long as the above desulfurization function is achieved. The dry desulfurization continuous regeneration process has the characteristics of high sulfur capacity, small bed resistance, convenient operation, continuous regeneration, simple regeneration process and the like. The desulfurization regeneration process principle is as follows:

and (3) desulfurization: fe₂O₃·H₂O+3H₂S＝Fe₂S₃·H₂O+3H₂O

Regeneration: 2Fe₂S₃·H₂O+3O₂＝2Fe₂O₃·H₂O+6S

By combining the two reaction formulas, the desulfurization regeneration reaction formula is as follows: h₂S+1/2O₂＝S+H₂O (reaction conditions are Fe)₂O₃·H₂O). It should be noted that, those skilled in the art can select the bio-filler layer and the desulfurization flora according to actual needs, as long as the above desulfurization function is achieved.

S600: supplying the desulfurized biogas to a biogas purification device

In this step, the desulfurized biogas obtained in the above step S500 is supplied to a biogas purification apparatus for purification treatment, so as to obtain a vehicle gas. Specifically, the biogas purification device 600 is a membrane purification device, the obtained desulfurized biogas is firstly pretreated to remove particles, moisture, oil substances and the like in the biogas, and when the biogas enters the membrane purification device, the biogas reaches the air inlet requirement (the pressure is 2-3 Kpa, the temperature is less than 55 ℃; CH₄55 to 65 volume percent; CO 2₂35 to 45 volume percent; h₂S＜7.5mg/Nm³；H₂O50-100% RH; note: the standard reference condition of gas volume in the standard is 101.325kPa, 20 ℃) and then is supplied to membrane purification equipment, a membrane component carries out coarse decarburization and fine decarburization on methane, CH is finally generated after membrane purification₄The natural gas product with the purity higher than 97 percent can remove water in the methane by the membrane component, and finally the dew point of the biological gas can completely meet the dew point requirement of the vehicle gas. Membrane purificationThe separated waste gas can be directly discharged or CO can be discharged₂And (3) recycling, enabling the biogas with the purity higher than 97% to enter a CNG compressor system, raising the pressure to 25MPa through a compressor to reach the pressure standard of the vehicle fuel gas, adding the biogas into a skid-mounted vehicle through a gas filling column, and selling or transporting the biogas to peripheral gas filling stations for use. The membrane module is the core of the whole membrane purification equipment, and the carbon dioxide reaches the design output requirement after passing through the second-stage hollow fiber membrane module. The outer exhaust gas of the system is discharged in the first-stage membrane group to become exhaust gas. After passing through the secondary membrane group, the exhaust gas of the secondary membrane group returns to the pressure stabilizing buffer tank through backflow to complete closed circulation. The working principle of the hollow fiber membrane is that different gas molecules are separated through different permeation rates of different gases in the high polymer material hollow fiber membrane. Among them, a gas having a high permeation rate is referred to as "fast gas", and a gas having a low permeation rate is referred to as "slow gas". The fast gas is permeated fast, most of the fast gas is concentrated at one end of the gas inlet, and a small part of the fast gas penetrates to one end of the gas outlet; the "slow gas" penetrates slowly so that most of it penetrates the membrane module to the exhaust port end and a small portion is concentrated at the intake port end. The water, hydrogen sulfide, carbon dioxide and oxygen in the biogas are all 'fast gas', while the nitrogen and methane are 'slow gas'. Therefore, the selective permeation adsorption characteristic of the membrane module determines that the membrane method methane purification can remove a large amount of carbon dioxide and can remove part of hydrogen sulfide and oxygen impurities.

Further, referring to fig. 11, the method for cooperatively treating kitchen waste and food waste further includes:

s700: feeding the anaerobic digestion solution into a solid-liquid separation device for solid-liquid separation

In this step, the anaerobic digestion solution obtained in the above step S400 is supplied to a solid-liquid separation apparatus to be subjected to solid-liquid separation, so that biogas residues and biogas slurry are obtained. Specifically, the solid-liquid separation device 700 is a two-phase horizontal screw centrifuge, the anaerobic digestion liquid generated by the dry anaerobic fermentation device 400 is pumped to the two-phase horizontal screw centrifuge, the two-phase horizontal screw centrifuge utilizes the density difference of the two phases of solid and liquid, under the action of the centrifuge, the sedimentation speed of solid phase particles is accelerated to realize solid-liquid separation, the separation process is that the anaerobic digestion liquid added with a flocculating agent (for example, PAM or ferric salt) is sent to a mixing cavity in a rotary drum of the two-phase horizontal screw centrifuge through an inlet pipeline, due to the high-speed rotation and friction resistance of the rotor, the anaerobic digestion liquid is accelerated in the rotor and forms a cylindrical liquid ring layer, under the action of centrifugal force, the solid particles with larger specific gravity are settled to the inner wall of the rotary drum to form a mud layer, then the solid phase is pushed to a conical end by utilizing the relative speed difference of a screw and the rotary drum, the mud residue is dehydrated, and discharging the supernatant from the large end of the rotary drum to realize solid-liquid separation, sending the biogas residues with water content of 80% generated by the solid-liquid separation to an incineration plant for incineration, and pumping the generated biogas slurry to a subsequent step S800 for treatment.

S800: supply biogas slurry to a sewage treatment device

In the step, the biogas slurry is supplied to a sewage treatment device for purification, so that the wastewater is discharged after reaching the standard. It should be noted that, those skilled in the art can select specific operations in the purification process according to actual needs, as long as the standard discharge of biogas slurry can be achieved, and details are not described herein.

Further, referring to fig. 12, the method for cooperatively treating kitchen waste and food waste further includes:

s900: another part of the biogas is supplied to the biogas boiler to be combusted and then exchanges heat with cooling water, and the steam is supplied to step S240

In this step, another part of the biogas obtained from the total dry anaerobic fermentation device of the step S400 is supplied to a biogas boiler to be combusted and then exchanges heat with cooling water, so as to obtain heat exchange flue gas and steam, and the steam is supplied to the cooking device 23 of the step S230 to be used as a heat source for heating the organic slurry.

In the description herein, references to the description of the term "one embodiment," "some embodiments," "an example," "a specific example," or "some examples," etc., mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above are not necessarily intended to refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, various embodiments or examples and features of different embodiments or examples described in this specification can be combined and combined by one skilled in the art without contradiction.

Although embodiments of the present invention have been shown and described, it is understood that the above embodiments are exemplary and should not be construed as limiting the present invention, and that variations, modifications, substitutions and alterations can be made to the above embodiments by those of ordinary skill in the art without departing from the scope of the present invention.

Claims (6)

1. A system for co-processing kitchen waste and food and beverage waste, comprising:

the kitchen waste pretreatment unit is provided with a kitchen waste inlet, a first leachate outlet, a first inorganic impurity outlet and a crushed kitchen waste outlet;

the food waste pretreatment unit is provided with a food waste inlet, a second inorganic impurity outlet, a third inorganic impurity outlet, a second leachate outlet, a grease outlet, a wastewater outlet and a food waste slurry outlet;

the mixing device is provided with a crushed kitchen waste inlet, a food and beverage waste slurry inlet and a mixed organic slurry outlet, the crushed kitchen waste inlet is connected with the crushed kitchen waste inlet, and the food and beverage waste slurry inlet is connected with the food and beverage waste slurry outlet;

the dry anaerobic fermentation device is provided with a mixed organic slurry inlet, a methane outlet and an anaerobic digestion liquid outlet, and the mixed organic slurry inlet is connected with the mixed organic slurry outlet through a scraper conveyor.

2. The system for co-processing kitchen waste and food waste according to claim 1, wherein said kitchen waste pre-processing unit comprises:

a refuse storage pit having the kitchen waste inlet, the first leachate outlet, and a post-stack leachate outlet; the drum sieve is provided with a material inlet after stacking and filtering, the first inorganic impurity outlet and an organic garbage outlet, and the material inlet after stacking and filtering is connected with the material outlet after stacking and filtering;

the magnetic separator is provided with an organic garbage inlet, a metal outlet and a garbage outlet after magnetic separation, and the organic garbage inlet is connected with the organic garbage outlet;

the shearing type crusher is provided with a magnetic separation rear garbage inlet and a crushing rear kitchen garbage outlet, and the magnetic separation rear garbage inlet is connected with the magnetic separation rear garbage outlet.

3. The system for co-processing kitchen waste and food waste according to claim 1 or 2, wherein the food waste pre-processing unit comprises:

the impurity separator is provided with the food waste inlet, the second inorganic impurity outlet, a second percolate outlet and a separated material outlet;

a crushing and sorting pulper, wherein the crushing and sorting pulper is provided with a separated material inlet, a water inlet, a third inorganic impurity inlet and an organic slurry outlet, the separated material inlet is connected with the separated material outlet, and the water inlet is connected with the first percolate outlet and the second percolate outlet;

the cooking device is provided with an organic slurry inlet and a cooked material outlet, and the organic slurry inlet is connected with the organic slurry outlet;

the three-phase separator is provided with a cooked material inlet, the grease outlet, the waste water outlet and the food waste slurry outlet, the cooked material inlet is connected with the cooked material outlet, and the waste water outlet is connected with the water inlet.

4. The system for co-processing kitchen waste and food and beverage waste according to claim 1, further comprising:

the biogas purification device is internally provided with a biological packing layer and is provided with a first biogas inlet and a desulfurized biogas outlet, and the first biogas inlet is connected with the biogas outlet;

the device comprises a marsh gas purification device, wherein the marsh gas purification device is provided with a desulfurized marsh gas inlet and a vehicle fuel gas outlet, and the desulfurized marsh gas inlet is connected with the desulfurized marsh gas outlet.

5. The system for co-processing kitchen waste and food and beverage waste according to claim 1, further comprising:

the solid-liquid separation device is provided with an anaerobic digestion liquid inlet, a biogas residue outlet and a biogas liquid outlet, and the anaerobic digestion liquid inlet is connected with the anaerobic digestion liquid outlet;

the sewage treatment device is provided with a biogas slurry inlet and a standard water outlet, and the biogas slurry inlet is connected with the biogas slurry outlet.

6. The system for co-processing kitchen waste and food and beverage waste according to claim 3, further comprising:

the biogas boiler is provided with a second biogas inlet, a cooling water inlet, a heat exchange flue gas outlet and a steam outlet, the second biogas inlet is connected with the biogas outlet, and the steam outlet is connected with the cooking device.

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