CN202700937U - Organic waste source separation management system - Google Patents

Abstract

An organic waste source separation management system comprises an organic waste source separation system, an organic waste transport system, an organic waste automatic bagging system and an organic waste disposal system. The organic waste source separation system is connected with the organic waste transport system. The organic waste transport system is connected with the organic waste automatic bagging system. Chemical fiber filter bags are used in the organic waste automatic bagging system. Bagged organic waste and filtrate are respectively transported to the organic waste disposal system for disposal. A convenient kitchen garbage transport pipeline is provided for inhabitants in kitchens so that kitchen garbage can be transported out without going out of the kitchens and mutual composite pollution of the kitchen garbage and other household garbage is avoided. Other recyclable materials can be recycled to the maximum. Water-saving closestools and other sanitary facilities are installed in washrooms and are used for saving water and saving energy, and at the same time excrement and urine are separated from other washing water to discharge so that the washing water (grey water) and black water ( the excrement and urine) are separated from each other and are respectively transported.

Description

A source separation management system for organic waste

technical field

The utility model belongs to the field of environmental protection and energy saving, and in particular relates to an environmental protection treatment technology for saving water resources, reducing the amount of kitchen waste and feces, and utilizing them as resources. the

Background technique

Kitchen waste refers to the leftovers discarded in the daily cooking of residents, such as leftovers, leftovers, animal viscera, melon and fruit peels, rotten vegetable leaves, tea residues and other organic wastes. The current treatment methods are mainly landfill or incineration. The landfill method exists: (1) occupies a huge area of land and consumes land resources irreversibly; (2) the landfill operation produces a large amount of odor, which affects the surrounding residents; (3) the landfill gas has a deflagration hazard; (4) two Secondary pollution is serious, and landfill leachate pollutes underground water sources; (5) The recyclable substances in garbage are polluted by kitchen waste and are difficult to recycle; while garbage incineration will produce fly ash, dioxin, sulfur dioxide, carbon monoxide and other highly toxic substances consumes a lot of energy. the

The current main treatment method for feces and urine is: waste of electricity and water resources is used to flush the waste and urine from the toilet to the septic tank, dilute and hydrolyze in the septic tank, and then discharge it to the sewage treatment plant for treatment; the essence of the sewage treatment plant is to pass It consumes a large amount of electricity to separate nitrogen, phosphorus and potassium from water bodies, and convert water pollution into air pollution and sludge. However, there is currently great controversy about the storage and disposal of sludge. The by-product sewage of sewage treatment plants Mud is becoming a new source of pollution. the

Contents of the invention

The technical problem to be solved by the utility model is to solve the above-mentioned problems in the prior art, and provide an energy-saving and environment-friendly organic waste source separation management system for organic waste treatment. the

The technical scheme adopted by the utility model is: a source separation treatment system for organic waste, including an organic waste source separation system, an organic waste delivery system, an automatic organic waste bagging system, and an organic waste treatment system; The organic waste source separation system is connected to the organic waste conveying system, and the organic waste conveying system is connected to the organic waste automatic bagging system. The organic waste automatic bagging system uses chemical fiber filter bags, and the bagged Organic waste and filtrate are sent to the organic waste treatment system for treatment. the

In the above technical solution, the organic waste source separation system is composed of an organic waste input device; the organic waste input device includes a kitchen sink for discharging kitchen waste installed in the kitchen, and a water-saving toilet or water-saving toilet installed in the toilet. Squat toilets, these devices have a discharge pipe connected to the mitered pipe of the organic waste conveying system. the

In the above technical solution, the organic waste conveying system is composed of a plurality of mitered pipes, vertical pipes for vertically conveying organic waste, elbows and tees, horizontal pipes for horizontal conveying, sewage collecting horizontal pipes, and sewage collecting vertical pipes. , pressurized water supply system; each vertical pipe extends from the roof of the residential building to the outdoors, with a non-powered turbine hood or fan installed on the top, and the discharge pipes of the organic waste input devices in the kitchens and bathrooms of each household pass through the inclined pipes. The connecting pipe is connected with the vertical pipe, and the vertical pipe extends downward to the basement or overhead floor;

In the basement or overhead floor, each vertical pipe is connected to each horizontal pipe through an elbow or a tee, and each horizontal pipe is transported and collected to the sewage collection horizontal pipe, and the end of the sewage collection horizontal pipe is a sewage collection vertical pipe; in the sewage collection vertical pipe The lower end is the feed inlet of the organic waste automatic bagging system;

Each elbow is provided with a nozzle and has an interface connected to the pressure water connection pipe;

At the bottom of the horizontal pipe and the sewage collecting horizontal pipe, a nozzle is arranged at intervals, and each nozzle part has an interface connected to the pressure water connection pipe;

The spraying direction of all nozzles is consistent with the conveying direction of the pipeline;

The main pressure water pipe is connected to the pressure water pipe of the horizontal pipe through the solenoid valves, and the pressure water pipe of the horizontal pipe is connected to the interface of the horizontal pipe and the elbow nozzle through the connecting pipe. The water pipe is connected with the sewage collecting horizontal pipe and the interface of the elbow nozzle through the connecting pipe.

The water inlet end of the main pressure water pipe is connected with the water outlet end of the high-level water tank, the water inlet end of the high-level water tank is connected with the pressure water delivery pipe, and the high-level water tank is equipped with a liquid level control device. the

In the above technical solution, the automatic bagging system for organic waste is composed of a bagging bin, an automatic crushing and bagging machine, a filter bag waiting area, a first sewage pool, a ventilation system, a sewage conveying system, and a liquid level control system;

The bagging bin is a negative-pressure airtight space that is odor-proof. The sewage collection vertical pipe extends into the bagging bin from above. There is a filter bag waiting area next to the machine, a first sewage pool is set under the automatic crushing bagging machine and the filter bag waiting area, and the bagging warehouse has a door;

A fan A is installed above the bagging bin, and the exhaust pipe of the fan is connected to the vertical pipe of the organic waste conveying system;

Two water pumps are installed in the first sewage tank, water pump A is the water supply pump of the organic waste conveying system, the water outlet of water pump A is connected to the high-level water tank through the pressure water conveying pipe, and the water outlet pipe of water pump B is connected to the organic waste treatment system; A liquid level control system is installed in the first sewage tank.

In the above technical solution, the organic waste treatment system includes a solid organic waste treatment system, the solid organic waste treatment system consists of organic waste solid-liquid separation equipment, a drum type aerobic fermentation reactor, an intake and exhaust system, a circulation water system composition;

There is a second sewage pool below the solid-liquid separation equipment for organic waste, and the water pump B outlet pipe of the organic waste automatic bagging system is connected to the second sewage pool; two water pumps are installed in the second sewage pool, and the outlet of water pump E The water pipeline is connected to the waste water and waste gas treatment heat exchanger B of the organic waste treatment system; the outlet pipe of the water pump C is connected to the waste water and waste gas treatment heat exchanger D of the organic waste treatment system; the outlet pipe of the heat exchanger is connected to the sewage pool ;

The drum-type aerobic fermentation reactor has inlet and outlet ports and inlet and exhaust holes, and a coaxial water jacket is also arranged outside the drum;

The suction pipe A of the intake and exhaust system is connected to the intake pipe of the aerobic fermentation reactor through the heat exchanger A, and the exhaust pipe of the aerobic fermentation reactor is connected to the waste water and waste gas treatment system through the fan B and the waste gas output pipe;

The water inlet pipe of the water pump D is connected to the water supply pipe through the gate valve and the water inlet valve, the water outlet pipe of the water pump D is connected to the water inlet pipe of the auxiliary heat source through the gate valve, and the water outlet pipe of the auxiliary heat source is connected to the water inlet pipe of the aerobic fermentation reactor through the auxiliary heat source solenoid valve , the outlet pipe of the aerobic fermentation reactor is connected to the waste water and waste gas system through the heat exchanger A and the circulating water output pipe, and the circulating water return pipe connected to the waste water and waste gas system is connected to the water inlet pipe of the water pump D;

The auxiliary heat source is provided with a bypass branch, and the bypass branch is provided with an auxiliary heat source bypass solenoid valve;

A pressure water tank is provided between the water inlet valve and the gate valve of the water inlet pipeline of the water pump, and the pressure water tank is provided with a drain valve and a drain pipe.

In the above technical solution, the organic waste treatment system includes a waste water and waste gas treatment system, and the waste water and waste gas treatment system can be composed of liquid high-temperature anaerobic treatment equipment, a heat exchanger, and a medium-temperature aerobic biological deodorization filter tower;

The high-temperature medium water inlet of heat exchanger C is connected to the circulating water output pipe of the solid organic waste treatment system, and the high-temperature medium water outlet of heat exchanger C is connected to the circulating water return pipe; the water from the sewage tank of the solid organic waste treatment system The outlet pipeline of the water pump E is connected to the water inlet of the liquid high-temperature anaerobic treatment equipment through the heat exchanger B, the connecting pipe, the heat exchanger C, and the water inlet pipe of the liquid high-temperature treatment equipment;

The liquid high-temperature anaerobic treatment equipment has a device for conveniently adding high-temperature anaerobic strains;

The liquid high-temperature anaerobic treatment equipment is equipped with a heating device;

The liquid high-temperature anaerobic treatment equipment is equipped with an insulation layer;

The gas output port of the liquid high-temperature anaerobic treatment equipment is connected to the biogas discharge pipe, followed by a dehydration device, a desulfurization device, and a biogas collection device in sequence;

The water outlet of the liquid high-temperature anaerobic treatment equipment is connected to the water inlet of the medium-temperature aerobic biological deodorization filter tower through the outlet pipe of the liquid high-temperature treatment equipment, heat exchanger B, and the water inlet pipe of the medium-temperature aerobic biological deodorization filter tower;

The exhaust gas output pipe and suction pipe B of the solid organic waste treatment system are connected to the medium-temperature aerobic biological deodorization filter tower through the heat exchanger D, fan C, and the air inlet pipe of the medium-temperature aerobic biological deodorization filter tower;

The medium-temperature aerobic biological deodorization filter tower is provided with an exhaust port;

The mesophilic aerobic biological deodorization filter tower has a convenient device for adding photosynthetic bacteria and mesophilic aerobic bacteria;

The water outlet of the medium-temperature aerobic biological deodorization filter tower is connected with the treatment liquid pool through the overflow pipe of the medium-temperature aerobic biological deodorization filter tower.

In the above technical solution, the waste water and waste gas treatment system may also be composed of liquid high-temperature aerobic fermentation treatment equipment, a heat exchanger, and a medium-temperature aerobic biological deodorization filter tower;

The high-temperature medium water inlet of heat exchanger C is connected to the circulating water output pipe of the solid organic waste treatment system, and the high-temperature medium water outlet of heat exchanger C is connected to the circulating water return pipe; the water from the sewage tank of the solid organic waste treatment system The water outlet pipeline of the water pump E is connected to the water inlet of the liquid high-temperature aerobic treatment equipment through the heat exchanger B, the connecting pipe, the heat exchanger C, and the water inlet pipe of the liquid high-temperature treatment equipment;

The liquid high-temperature aerobic treatment equipment has a convenient device for adding high-temperature thermophilic aerobic bacteria;

The liquid high-temperature aerobic treatment equipment is equipped with an insulation layer;

The exhaust gas output pipe and suction pipe C of the solid organic waste treatment system are connected to the liquid high-temperature aerobic treatment equipment through the fan D;

The liquid high-temperature aerobic fermentation treatment equipment is connected to the medium-temperature aerobic biological deodorization filter tower through the foam outflow pipe, the water pump G, and the foam delivery pipe;

The water outlet of the liquid high-temperature aerobic treatment equipment is connected to the water inlet of the medium-temperature aerobic biological deodorization filter tower through the outlet pipe of the liquid high-temperature treatment equipment, heat exchanger B, and the water inlet pipe of the medium-temperature aerobic biological deodorization filter tower;

The exhaust gas output pipe and suction pipe B of the liquid high-temperature aerobic treatment equipment are connected to the medium-temperature aerobic biological deodorization filter tower through the heat exchanger D, the fan C, and the air inlet pipe of the medium-temperature aerobic biological deodorization filter tower;

The medium-temperature aerobic biological deodorization filter tower is provided with an exhaust port;

The mesophilic aerobic biological deodorization filter tower has a convenient device for adding photosynthetic bacteria and mesophilic aerobic bacteria;

The water outlet of the medium-temperature aerobic biological deodorization filter tower is connected with the treatment liquid pool through the overflow pipe of the medium-temperature aerobic biological deodorization filter tower.

Collect organic waste by installing kitchen sinks or other kitchen waste storage equipment in the kitchen, and installing organic waste input devices such as water-saving toilets or water-saving squatting pans in toilets; collected solids Organic waste and liquid organic waste are transported separately from other washing wastewater and other waste to achieve source separation;

The organic waste is transported to the basement or the overhead floor through the organic waste transport system, and the pressure water is used to solve the problem of anti-blocking and transport through the relay injection of the sprinkler on the elbow and the pipeline;

An automatic crushing and bagging machine is installed at the end of the pipeline transportation system to crush the solid part of the organic waste and put it into a filter bag for convenient transportation, while the liquid part of the organic waste seeps out from the filter bag to achieve preliminary solid-liquid separation. The filtered sewage is used as the water source of the pipeline transportation system, the water in the high-level water tank is supplemented by this sewage, and the excess sewage is sent to the waste water and gas treatment system for treatment;

The filter bag filled with organic waste is sent to the solid-liquid separation equipment for solid-liquid separation. After the solid-liquid separation, the bag emptying operation is carried out, and the solid organic waste poured out is sent to the drum-type high-temperature aerobic fermentation reactor for high-temperature aerobic fermentation. Treatment, after the solid organic waste is processed by high-temperature aerobic fermentation, it is odorless and has no harmful pathogenic bacteria, and is sold as agricultural organic fertilizer after aging;

Sewage separated from solid-liquid separation, sewage filtered out by the automatic bagging system for organic waste, and waste gas generated by the drum-type high-temperature aerobic fermentation reactor are sent to the waste water and waste gas treatment system for treatment. the

The wastewater and waste gas treatment system includes liquid high-temperature fermentation treatment equipment, heat exchangers, medium-temperature aerobic biological deodorization filter towers, etc. Liquid high-temperature fermentation treatment equipment can use liquid high-temperature anaerobic fermentation treatment equipment:

The sewage separated by solid-liquid separation and the sewage filtered out by the automatic bagging system of organic waste are sent to the liquid high-temperature anaerobic fermentation treatment equipment for high-temperature anaerobic fermentation, and the hot water from the drum-type high-temperature aerobic fermentation reactor is used to The sewage is heated so that the working temperature of the anaerobic reactor is greater than or equal to 53 degrees;

The liquid high-temperature anaerobic treatment equipment is equipped with a heating device. When the liquid high-temperature anaerobic reaction temperature is lower than the set temperature, the heating device is used to precisely heat the liquid; the liquid high-temperature anaerobic treatment equipment is equipped with an insulation layer; the temperature of the sewage is kept constant At the set temperature to carry out high temperature anaerobic fermentation reaction;

Liquid high-temperature anaerobic treatment equipment has a convenient device for adding high-temperature anaerobic bacteria;

The biogas generated by high-temperature anaerobic fermentation is collected and used after dehydration and desulfurization;

In the liquid high-temperature anaerobic fermentation treatment equipment, a heat exchanger is installed in the pipeline that transports the fermentation liquid to the liquid medium-temperature aerobic biological deodorization filter tower, and the heat exchanger is used to cool the high-temperature fermentation liquid to a suitable medium temperature, and exchange heat to the input The sewage to be treated in the fermentation equipment can increase the temperature of the sewage to be treated;

The sewage after the liquid high-temperature fermentation treatment is sent to the liquid medium-temperature aerobic biological deodorization filter tower for treatment, and the waste gas generated by the drum-type high-temperature aerobic fermentation reaction is mixed with fresh air, cooled to a suitable temperature by a heat exchanger, and then sent to the medium-temperature Under the liquid surface of the aerobic biological deodorization filter tower, the gas distributor provides oxygen to the fermentation liquid. The gaseous ammonia in the waste gas dissolves in the medium-temperature fermentation liquid, and the gas insoluble in water passes through layers of biological filters upwards, and is digested and eliminated by microorganisms. Discharge to the atmosphere after odor treatment;

The mesophilic aerobic biological deodorization filter tower has a convenient device for adding mesophilic aerobic bacteria and photosynthetic bacteria, and adds mesophilic aerobic bacteria and photosynthetic bacteria according to the needs of mesophilic aerobic biological reactions;

After photosynthetic microorganisms and medium-temperature aerobic fermentation, the liquid fermentation liquid has high nutrient and organic matter content, and is odorless and free of harmful pathogenic bacteria, and can be sold on-site as liquid organic fertilizer;

For long-distance transportation where high-concentration liquid organic fertilizer is required, the supernatant of the liquid organic fertilizer can be filtered through a filter, and then filtered by the membrane treatment equipment; the effluent of the membrane treatment equipment is reclaimed water, which can be used for washing and filtering Irrigation of bags and landscaping or sales of reclaimed water; the concentrated fermentation liquid left by membrane filtration can be sold as high-concentration liquid organic fertilizer for long-distance sales; the solid matter left by filter filtration is sent to solid organic waste Handling system handling.

In the above technical solution, the liquid high-temperature fermentation treatment equipment of the waste water and waste gas treatment system can also use liquid high-temperature aerobic fermentation treatment equipment:

The sewage separated by solid-liquid separation and the sewage filtered out by the automatic bagging system of organic waste are sent to the liquid high-temperature aerobic fermentation treatment equipment for high-temperature aerobic fermentation, and the hot water from the drum-type high-temperature aerobic fermentation reactor is used to The sewage is heated so that the working temperature of the aerobic reactor is greater than or equal to 55 degrees;

The liquid high-temperature aerobic treatment equipment is equipped with an insulation layer, so that the sewage can undergo high-temperature aerobic fermentation reaction at a relatively constant temperature;

The liquid high-temperature aerobic treatment equipment has a convenient device for adding high-temperature thermophilic aerobic bacteria;

The oxygen required for liquid high-temperature aerobic fermentation is mixed with the waste gas and fresh air produced by the drum-type high-temperature aerobic fermentation reactor, and then aerated into the high-temperature fermentation liquid, so that the liquid high-temperature aerobic reaction can be carried out at a high speed;

The foam generated in the liquid high-temperature aerobic fermentation treatment equipment is sent to the spray system of the medium-temperature aerobic biological deodorization filter tower to spray on the filter layer, and is provided to the biological filter material as a nutrient solution;

In the liquid high-temperature aerobic fermentation treatment equipment, a heat exchanger is installed in the pipeline that transports the fermentation liquid to the liquid medium-temperature aerobic biological deodorization filter tower, and the heat exchanger is used to cool the high-temperature fermentation liquid to a suitable medium temperature, and exchange heat into the fermentation The sewage to be treated in the equipment can increase the temperature of the sewage to be treated;

The sewage treated by liquid high-temperature aerobic fermentation is sent to the liquid medium-temperature aerobic biological deodorization filter tower for treatment, while the waste gas and fresh air produced by liquid high-temperature aerobic fermentation are cooled to a suitable temperature by a heat exchanger and then sent to the medium-temperature aerobic Under the liquid surface of the biological deodorization filter tower, oxygen is provided to the fermentation liquid through the air distributor, the gaseous ammonia in the waste gas is dissolved in the medium temperature fermentation liquid, and the gas insoluble in water passes through the layers of biological filter layers, and is digested and deodorized by microorganisms back to the atmosphere;

The mesophilic aerobic biological deodorization filter tower has a convenient device for adding mesophilic aerobic bacteria and photosynthetic bacteria, and adds photosynthetic bacteria and mesophilic aerobic bacteria according to the needs of mesophilic aerobic biological reactions;

After photosynthetic microorganisms and medium-temperature aerobic fermentation, the liquid fermentation liquid has high nutrient and organic matter content, and is odorless and free of harmful pathogenic bacteria, and can be sold on-site as liquid organic fertilizer;

For long-distance transportation where high-concentration liquid organic fertilizer is required, the supernatant of the liquid organic fertilizer can be filtered through a filter, and then filtered by the membrane treatment equipment; the effluent of the membrane treatment equipment is reclaimed water, which can be used for washing and filtering Irrigation of bags and landscaping or sales of reclaimed water; the concentrated fermentation liquid left by membrane filtration can be sold as high-concentration liquid organic fertilizer for long-distance sales; the solid matter left by filter filtration is sent to solid organic waste Handling system handling.

The beneficial effects of the utility model are: providing residents with a convenient food waste transportation pipeline in the kitchen, so that the food waste can be transported outside the kitchen, eliminating the trouble of residents bagging the food waste and discarding it outside, and avoiding Kitchen waste and other domestic waste are mixed and polluted, so that other recyclable materials can be recycled to the maximum extent; water-saving toilets and other sanitation facilities are installed in toilets, so that the transportation of feces and urine can be compared with other washing products while saving water and energy. The water is discharged separately, so that the washing water (referred to as gray water) is separated from the black water (feces and urine) and transported separately. The gray water can be sold as reclaimed water after simple treatment, while the black water and solid organic waste are processed by organic waste. The treatment system turns waste into treasure after treatment, and organic waste is utilized as a resource, contributing to the sustainable development of the economy. the

Description of drawings:

Fig. 1 is the schematic diagram when the utility model adopts liquid high-temperature anaerobic fermentation processing equipment;

Fig. 2 is the schematic diagram when the utility model adopts liquid high-temperature aerobic fermentation treatment equipment;

Fig. 3 is a schematic diagram of the organic waste source separation system and the organic waste conveying system of the utility model;

Fig. 4 is the schematic diagram of the utility model organic waste automatic bagging system;

Fig. 5 is the schematic diagram of the utility model organic waste solid processing system;

Fig. 6 is the schematic diagram of the wastewater and waste gas treatment system of the utility model adopting liquid high-temperature anaerobic fermentation treatment;

Fig. 7 is a schematic diagram of a wastewater and waste gas treatment system using liquid high-temperature aerobic fermentation treatment according to the present invention.

Number in the picture:

1 Organic waste source separation system, 2 Organic waste conveying system, 3 Organic waste automatic bagging system, 4 Organic waste treatment system, 41 Solid organic waste treatment system, 42 Waste water and waste gas from liquid high-temperature anaerobic fermentation reaction Treatment system, 43 waste water and gas treatment system using liquid high-temperature aerobic fermentation reaction, 101 organic waste input device, 201 unpowered air cap, 202 vertical pipe, 203 elbow, 204 horizontal pipe, 205 sewage collection horizontal pipe, 206 sewage collection Vertical pipe, 207 water pump A, 208 main pressure water pipe, 209 solenoid valve, 210 horizontal pipe pressure water pipe, 211 horizontal pipe pressure water connection pipe, 212 sewage collection horizontal pipe pressure water pipe, 213 sewage collection horizontal pipe pressure water connection pipe, 214 oblique Takeover, 215 high water tank, 216 pressure water delivery pipe, 301 exhaust pipe, 302 fan A, 303 bagging warehouse, 304 automatic crushing bagging machine, 305 water pump B, 306 sewage pipe, 307 first sewage pool, 308 door, 4101 second sewage tank, 4102 water pump C, 4103 sewage circulation return pipe, 4104 centrifugal solid-liquid separation equipment, 4105 water supply pipe, 4106 circulating water return pipe, 4107 water inlet valve, 4108 drain valve, 4109 pressure water tank, 4110 gate valve, 4111 water pump inlet pipe, 4112 water pump D, 4113 auxiliary heat source gate valve, 4114 auxiliary heat source, 4115 auxiliary heat source solenoid valve, 4116 auxiliary heat source bypass solenoid valve, 4117 aerobic fermentation reactor inlet pipe, 4118 aerobic fermentation reactor exhaust pipe , 4119 fan B, 4120 exhaust gas output pipe, 4121 suction pipe A, 4122 aerobic fermentation reactor outlet pipe, 4123 heat exchanger A, 4124 circulating water output pipe, 4125 sewage circulation outlet pipe, 4126 sewage output pipe, 4127 drainage Pipe, 4128 water pump E, 4129 aerobic fermentation reactor inlet pipe, 4130 drum type high temperature aerobic fermentation reactor, 4201 liquid high temperature treatment equipment outlet pipe, 4202 medium temperature aerobic biological deodorization filter tower inlet pipe, 4203 heat exchanger B , 4204 connecting pipe, 4205 heat exchanger C, 4206 liquid high temperature treatment equipment inlet pipe, 4207 electric heater, 4208 liquid high temperature anaerobic treatment equipment, 4209 medium temperature aerobic biological deodorization filter tower, 4210 exhaust port, 4211 suction pipe B, 4212 heat exchanger D, 4213 fan C, 4214 medium temperature aerobic biological deodorization filter tower inlet pipe, 4215 water pump F, 4216 treatment liquid delivery pipe, 4217 treatment liquid pool, 4218 medium temperature aerobic biological deodorization filter tower overflow Pipe, 4219 filter, 4220 membrane treatment equipment, 4221 concentrated fermentation liquid output pipe, 4222 medium water output pipe, 4223 biogas discharge pipe, 4224 dehydration device, 4225 desulfurization device, 4226 biogas collection device, 4301 suction pipe C, 4302 fan D, 4303 liquid high temperature aerobic fermentation treatment equipment, 4304 liquid high temperature aerobic fermentation treatment equipment exhaust pipe, 4305 foam delivery Tube, 4306 Water pump G, 4307 Foam outflow tube. the

Detailed ways:

The source separation management system of organic waste is composed of organic waste source separation system 1, organic waste conveying system 2, organic waste automatic bagging system 3, and organic waste treatment system 4. The organic waste source separation system 1 is connected to the organic waste conveying system 2 , and the organic waste conveying system 2 is connected to the organic waste automatic bagging system 3 . The organic waste bagged in the organic waste automatic bagging system 3 and the filtered liquid are transported to the organic waste treatment system 4 for processing.

The organic waste source separation system 1 is composed of an organic waste input device 101 installed in each household. the

The input device of organic waste includes kitchen sinks for discharging kitchen waste and other storage equipment for kitchen waste, and high-pressure water-saving toilets without traps or water-saving squatting toilets installed in toilets. The discharge pipe of the organic waste input device 101 is connected to the miter pipe 214 of the organic waste conveying system 2 .

The organic waste conveying system 2 is composed of a plurality of mitered pipes, a vertical pipe responsible for the vertical conveyance of organic waste, an elbow, a horizontal pipe responsible for the horizontal conveyance, a sewage collection horizontal pipe, a sewage collection vertical pipe, and a pressure water supply system. the

The standpipe 202 protrudes from the roof of the residential building to the outdoors, and the top of the standpipe 202 is equipped with an unpowered wind cap 201. The discharge pipes of the organic waste input devices 101 in the kitchens and toilets of each household pass through the mitered pipe 214 and the standpipe 202. connect. Standpipe 202 extends down to a basement or raised level. the

In the basement or overhead floor, there are the following ways to connect the vertical pipe: the vertical pipe 202 is connected to the horizontal pipe 204 through the elbow 203 or through a tee, and then connected to the horizontal pipe 205 of the sewage collection, and the horizontal pipe 205 of the sewage collection is connected to the horizontal pipe 205 of the sewage collection The vertical pipe 206 is connected; the vertical pipe 202 is connected with the sewage collection horizontal pipe 205 through an elbow or a tee, and the sewage collection horizontal pipe 205 is connected with the sewage collection vertical pipe 206; or the vertical pipe 202 is directly connected with the sewage collection vertical pipe 206. The lower end of the sewage collection vertical pipe 206 is the feeding port of the automatic crushing and bagging machine 304 of the organic waste automatic bag changing system 3 . the

The corner of each elbow is provided with a spray head, and is connected with a pressure water connecting pipe. the

There is a shower nozzle at intervals at the bottom of the horizontal pipe 204 and the sewage collection horizontal pipe 205 pipeline, and each nozzle position has an interface to be connected with the pressure water connecting pipe. The distance between the nozzles is set to ensure that the water flow generated by the pressure water in the pipeline forms a relay flow. the

A first sewage tank 307 is provided in the organic waste automatic bag changing system 3 . A water pump A 207 is arranged at the first sewage tank 307, and the water outlet of the water pump A 207 is connected with the high-level water tank 215 through the pressure water delivery pipe 216, and the high-level water tank is equipped with a liquid level control device. The water outlet of the elevated water tank 215 is connected with the main pressure water pipe 208 . the

The main pressure water pipe 208 is connected with the horizontal pipe pressure water pipe 210 through the solenoid valve 209 . The horizontal pipe pressure water pipe 210 is connected with the interface of the nozzle part of the elbow 203 , and the horizontal pipe pressure water pipe 210 is connected with the interface of the horizontal pipe 204 nozzle part through the horizontal pipe pressure water connecting pipe 211 . the

The main pressure water pipe 208 is connected with the pressure water pipe 212 of the sewage collecting horizontal pipe. The pressure water pipe 212 of the sewage collecting horizontal pipe is connected with the interface of the nozzle part of the elbow, and the pressure water pipe 212 of the sewage collecting horizontal pipe is connected with the interface of the nozzle part of the sewage collecting horizontal pipe 212 through the pressure water connecting pipe 213 of the sewage collecting horizontal pipe. the

The organic waste automatic bagging system 3 is composed of a bagging bin, an automatic crushing bagging machine, a filter bag waiting area, a sewage tank, a ventilation system, a sewage conveying system, and a control system. the

The bagging bin 303 is an odor-proof closed space, and the sewage collection vertical pipe 206 stretches into the bagging bin 303 from above. Below the discharge port of the sewage vertical pipe 206, the feed port of the automatic crushing and bagging machine 304 is arranged, and a filter bag waiting area is arranged beside the automatic crushing and bagging machine 304. The automatic crushing and bagging machine 304 and the filter bag A first sewage pool 307 is arranged below the waiting area. The bagging bin 303 is provided with a door 308 . A fan A302 is installed above the bagging bin, and the exhaust pipe 301 of the fan A302 is connected with the vertical pipe 202. the

Two water pumps are arranged in the first sewage pool 307 . Water pump A 207 is the water supply pump of the organic waste delivery system 2. The water pump B 305 is connected with the organic waste treatment system through the sewage pipe 306. the

A liquid level control system is installed in the first sewage tank 307. the

The organic waste treatment system 4 is composed of a solid organic waste treatment system 41 and a waste water and waste gas treatment system. the

The solid organic waste treatment system 41 is composed of solid-liquid separation equipment, a drum-type high-temperature aerobic fermentation reactor, an intake and exhaust system, and a circulating water system. the

The solid organic waste treatment system 41 is equipped with a centrifugal solid-liquid separation device 4104, and a second sewage pool 4101 is provided below it, and the sewage pipe 306 from the organic waste automatic bagging system and the sewage circulation from the waste water and gas treatment system The return pipe 4103 is connected to the second sewage tank 4101, and the second sewage tank 4101 is provided with a water pump C 4102 and a water pump E4128, and the water outlet of the water pump C4102 is connected with a sewage circulation outlet pipe 4125 to be connected with the waste water and gas treatment system; the water outlet of the water pump E4128 A sewage output pipe 4126 is connected to the waste water and gas treatment system. the

The drum-type aerobic fermentation reactor 4130 has inlet and outlet ports and inlet and exhaust holes, and a coaxial water jacket is also provided outside the drum. the

The suction pipe A 4121 of the intake and exhaust system is connected to the air inlet of the drum type aerobic fermentation reactor 4130 through the heat exchanger A 4123, the air inlet pipe 4129 of the aerobic fermentation reactor 4130, and the exhaust pipe of the drum type aerobic fermentation reactor 4130 The stomata are connected to the wastewater and waste gas treatment system through the exhaust pipe 4118 of the aerobic fermentation reactor, the fan B 4119, and the waste gas output pipe 4120. the

The water inlet pipe 4111 of water pump D 4112 links to each other with water supply pipe 4105 by gate valve 4110, water inlet valve 4107. The outlet pipe of the water pump D 4112 is connected to the water inlet pipe of the auxiliary heat source 4114 through the auxiliary heat source gate valve 4113, and the outlet pipe of the auxiliary heat source 4114 is connected to the aerobic fermentation reactor water inlet pipe 4117 through the auxiliary heat source electromagnetic valve 4115. The outlet pipe 4122 of the aerobic fermentation reactor is connected to the waste water and waste gas treatment system through the heat exchanger A 4123 and the circulating water output pipe 4124; the circulating water return pipe 4106 connected to the waste water and waste gas treatment system is connected to the water inlet pipe 4111 of the water pump D 4112. the

The auxiliary heat source 4114 is provided with a bypass branch, and the auxiliary heat source bypass solenoid valve 4116 is arranged on the bypass branch. the

A pressure water tank 4109 is arranged between the water inlet valve 4107 and the gate valve 4110 of the water inlet pipeline of the water pump D 4112. The pressure water tank 4109 is provided with a drain valve 4108 and a drain pipe 4127 . the

According to the difference of liquid high-temperature fermentation treatment equipment used in sewage high-temperature treatment, the waste water and waste gas treatment system is divided into two implementation modes: waste water and waste gas treatment system using liquid high-temperature anaerobic treatment 42, waste water and waste gas treatment system using liquid high-temperature aerobic treatment 43 . the

The wastewater and waste gas treatment system 42 using liquid high-temperature anaerobic treatment is composed of liquid high-temperature anaerobic treatment equipment, heat exchangers, medium-temperature aerobic biological deodorization filter towers, water pumps, filters, and membrane treatment equipment. the

The high-temperature medium water inlet of the heat exchanger C 4205 is connected to the circulating water output pipe 4124 of the solid organic waste treatment system 41, and the high-temperature medium water outlet is connected to the circulating water return pipe 4106. the

The sewage circulation outlet pipe 4125 of the solid organic waste treatment system 41 is connected to the low-temperature medium water inlet of the heat exchanger D 4212, and the low-temperature medium water outlet of the heat exchanger D 4212 is connected to the sewage circulation return pipe 4103. the

The sewage output pipe 4126 of the solid organic waste treatment system 41 is connected to the water inlet of the liquid high-temperature anaerobic treatment equipment 4208 through the heat exchanger B 4203, the connecting pipe 4204, the heat exchanger C 4205, the water inlet pipe 4206 of the liquid high-temperature anaerobic treatment equipment, and the liquid The water outlet of the high-temperature anaerobic treatment equipment 4208 is connected to the water inlet of the medium-temperature aerobic biological deodorization filter tower 4209 through the outlet pipe 4201 of the liquid high-temperature treatment equipment, the heat exchanger B 4203, the water inlet pipe 4202 of the medium-temperature aerobic biological deodorization filter tower. the

The liquid high-temperature anaerobic treatment equipment 4208 is provided with a device for conveniently adding high-temperature anaerobic bacteria parent, has a thermal insulation layer and is provided with an auxiliary heater 4207 . the

The gas output port of the liquid high-temperature anaerobic treatment equipment 4208 is connected to the biogas discharge pipe 4223 , followed by a dehydration device 4224 , a desulfurization device 4225 , and a biogas collection device 4226 in sequence. the

The waste gas output pipe 4120 and suction pipe B 4211 of the solid organic waste treatment system 41 are connected to the medium-temperature aerobic biological deodorization filter tower 4209 through the heat exchanger D4212 and the fan C 4213 through the medium-temperature aerobic biological deodorization filter tower inlet pipe 4214 . the

The medium-temperature aerobic biological deodorization filter tower is provided with an exhaust port 4210 . the

The mesophilic aerobic biological deodorization filter tower has a convenient device for adding photosynthetic bacteria and mesophilic aerobic bacteria. the

The medium-temperature aerobic biological deodorization filter tower is equipped with an insulation layer. the

The water outlet of the medium-temperature aerobic biological deodorization filter tower 4209 is connected to the treatment liquid pool 4217 through the medium-temperature aerobic biological deodorization filter tower overflow pipe 4218, the water inlet pipe of the water pump F 4215 is connected to the treatment liquid pool 4217, and the outlet of the water pump F 4215 The water port is connected to the membrane treatment equipment 4220 through the treatment liquid delivery pipe 4216 and the filter 4219 . the

The membrane treatment equipment 4220 has a concentrated fermentation broth output pipe 4221 and a middle water outflow pipe 4222 . the

The wastewater and waste gas treatment system 43 using high-temperature aerobic fermentation treatment is composed of liquid high-temperature aerobic fermentation treatment equipment, heat exchangers, medium-temperature aerobic biological deodorization filter towers, water pumps, filters, and membrane treatment equipment. the

The high-temperature medium water inlet of the heat exchanger C4205 is connected to the circulating water output pipe 4124 of the solid organic waste treatment system 41 , and the high-temperature medium water outlet is connected to the circulating water return pipe 4106 . the

The sewage circulation outlet pipe 4125 of the solid organic waste treatment system 41 is connected to the low-temperature medium water inlet of the heat exchanger D 4212, and the low-temperature medium water outlet of the heat exchanger D 4212 is connected to the sewage circulation return pipe 4103. the

The sewage treatment output pipe 4126 of the solid organic waste treatment system 41 is connected to the water inlet of the liquid high-temperature aerobic treatment equipment 4303 through the heat exchanger B 4203, the connecting pipe 4204, the heat exchanger C 4205, the water inlet pipe 4206 of the liquid high-temperature treatment equipment, The water outlet of liquid high-temperature aerobic treatment equipment 4303 is connected to the water inlet of medium-temperature aerobic biological deodorization filter tower 4209 through liquid high-temperature treatment equipment outlet pipe 4201, heat exchanger B 4203, medium temperature aerobic biological deodorization filter tower inlet pipe 4202. the

The exhaust gas output pipe 4120 and the suction pipe C 4301 of the solid organic waste treatment system 41 are connected to the liquid high-temperature aerobic treatment equipment 4303 through the fan D 4302. the

The liquid high-temperature aerobic treatment equipment 4303 is equipped with a device for conveniently adding photosynthetic strains and mesophilic aerobic bacteria mothers, and has an insulating layer. the

The liquid high-temperature aerobic fermentation treatment equipment 4303 is connected to the medium-temperature aerobic biological deodorization filter tower 4209 through the foam outflow pipe 4307, the water pump G 4306, and the foam delivery pipe 4305. the

The gas outlet of the liquid high-temperature aerobic fermentation treatment equipment 4303 is connected to the exhaust pipe 4304 of the liquid high-temperature aerobic fermentation treatment equipment and the suction pipe B 4211 through the heat exchanger D 4212, fan C 4213, and the air intake pipe of the medium-temperature aerobic biological deodorization filter tower 4214 is connected with medium-temperature aerobic biological deodorization filter tower 4209. the

The medium-temperature aerobic biological deodorization filter tower is provided with an exhaust port 4210 . the

The mesophilic aerobic biological deodorization filter tower has a convenient device for adding photosynthetic bacteria and mesophilic aerobic bacteria. the

The medium-temperature aerobic biological deodorization filter tower is equipped with an insulation layer. the

The water outlet of the medium-temperature aerobic biological deodorization filter tower 4209 is connected to the treatment liquid pool 4217 through the medium-temperature aerobic biological deodorization filter tower overflow pipe 4218, the water inlet pipe of the water pump F 4215 is connected to the treatment liquid pool 4217, and the outlet of the water pump F 4215 The water port is connected to the membrane treatment equipment 4220 through the treatment liquid delivery pipe 4216 and the filter 4219 . the

The membrane treatment equipment 4220 has a concentrated fermentation broth output pipe 4221 and a middle water outflow pipe 4222 . the

Specific implementation mode one:

The organic waste enters the vertical pipe 202 through the organic waste source separation system 1 through the organic waste input device 101 installed in each household and the miter pipe 214 of the organic waste delivery system 2 . the

After the organic waste enters a certain vertical pipe 202, the electromagnetic valve 209 on the horizontal pipe pressure water pipe 210 connected with this vertical pipe 202 is energized and connected. Under the action of pressure water, the organic waste reaches the automatic crushing and bagging machine 304 of the organic waste automatic bagging system 3 through the vertical pipe 202, the elbow 203, the horizontal pipe 204, the sewage collection horizontal pipe 205, and the sewage collection vertical pipe 206 feed port. the

The solid part of the organic waste is crushed by the automatic crushing and bagging machine 304 and loaded into a chemical fiber filter bag. After the filter bag is full, it is moved to the filter bag waiting area. the

The liquid part filtered from the automatic crushing and bagging machine 304 and the filter bag waiting area flows into the first sewage pool 307 . Part of the sewage enters the high-level water tank 215 through the pressure water delivery pipe 216 under the action of the water pump A 207, and is supplied to the organic waste delivery system 2 for use. The high water tank is equipped with a liquid level control device. the

When the water level of the high level water tank is lower than the set low value, the liquid level control system of the first sewage tank will start the water pump A 207 to send the sewage into the high level water tank 215 through the pressure water delivery pipe 216, when the water level of the high level water tank reaches the set high level When the value is reached, the level control system of the first sewage tank will turn off the water pump A 207. When the liquid level of the first sewage tank was higher than the set value, the liquid level control system of the first sewage tank would start the water pump B 305 to transport the sewage to the second sewage tank 4101 of the solid organic waste treatment system 41 through the sewage pipe 306 At the same time, the liquid level control device ensures that the liquid level of the first sewage tank 307 is not lower than a lower limit liquid level, and the lower limit liquid level ensures the supply of water to the organic waste conveying system 2 . the

The bad smell of 303 in the bagging bin is extracted by blower fan A 302, and is discharged by standpipe 202 through exhaust pipe 301. the

The solid organic waste packed into the filter bag is transported to the solid organic waste treatment system 41 of the organic waste treatment system 4 . The solid organic waste is sent to the centrifugal solid-liquid separation equipment 4104 together with the filter bag, and the solid-liquid separation is carried out under the action of centrifugal force. After the separation, the bag emptying operation is carried out, and the dehydrated solid organic waste is poured out from the filter bag And send the drum type high-temperature aerobic fermentation reactor 4130 to carry out high-temperature aerobic fermentation treatment. the

The sewage separated by the centrifugal solid-liquid separation equipment 4104 enters the second sewage pool 4101, the sewage from the organic waste automatic bagging system 3 enters the second sewage pool 4101 through the sewage pipe 306, and the sewage from the waste water and gas treatment system 42 passes through the second sewage pool 4101. The sewage circulation return pipe 4103 enters the second sewage pool 4101 . The sewage in the second sewage pool 4101 flows into the sewage circulation outlet pipe 4125 through the water pump C4102, and returns to the second sewage pool 4101 from the sewage circulation return pipe 4103 through the heat exchanger D4212. The sewage in the second sewage pool 4101 is sent to the waste water waste gas treatment system 42 that adopts liquid high-temperature anaerobic treatment through the water pump E 4128 through the sewage output pipe 4126 for treatment. the

After the solid organic waste is fermented by the drum-type high-temperature aerobic fermentation reactor 4130, it is odorless and has no harmful pathogenic bacteria. After aging, it can be sold as agricultural organic fertilizer. the

The oxygen required for solid high-temperature aerobic fermentation reaction is supplemented by air inhaled from the atmosphere. After the air passes through the suction pipe A4121 and is heated by the heat exchanger A4123, it enters the drum-type high-temperature well through the air inlet pipe 4129 of the aerobic fermentation reactor. Oxygen Fermentation Reactor 4130. The exhaust gas produced by the high-temperature aerobic fermentation reaction is extracted from the drum-type high-temperature aerobic fermentation reactor 4130 by the fan B 4119 through the exhaust pipe 4118 of the aerobic fermentation reactor, and sent to the waste water treated by liquid high-temperature anaerobic treatment through the exhaust gas output pipe 4120 Exhaust gas treatment system 42 treats. the

The hot water required by the drum-type high-temperature aerobic fermentation reactor 4130 is initially provided by the auxiliary heat source 4114 . The water pump D4112 absorbs water from the water inlet pipe 4111, and the outlet water of the water pump D4112 enters the auxiliary heat source 4114 through the auxiliary heat source gate valve 4113, and enters the drum-type high-temperature aerobic fermentation reactor 4130 through the auxiliary heat source solenoid valve 4115 and the aerobic fermentation reactor water inlet pipe 4117 after heating water jacket. The outlet water of the water jacket enters the heat exchanger A 4123 through the outlet pipe 4122 of the aerobic fermentation reactor, heats the air, and then sends it through the outlet pipe 4124 of the circulating water to the wastewater and waste gas treatment system 42 using liquid high-temperature anaerobic treatment. The circulating water returned from the waste water and gas treatment system 42 using liquid high-temperature anaerobic treatment flows into the water inlet pipe 4111 through the circulating water return pipe 4106 . the

The water in the water pump water inlet pipe 4111 is initially provided by the water supply pipe 4105, and then provided by the outside through the water inlet valve 4107 and the gate valve 4110. After the pipeline of the circulating water system is filled with water, close the gate valve 4110 and fill the pressure water tank 4109 with water. After the pressure water tank is filled with water to meet the requirements, close the water inlet valve 4107 and open the gate valve 4110 to automatically replenish water from the pressure water tank to the circulating water system. After the water in the circulating water system is heated and expanded, the excess water is discharged from the drain pipe 4127 through the drain valve 4108 . the

When the heat generated by the high-temperature aerobic fermentation reaction can meet the needs of the entire system, the auxiliary heat source bypass solenoid valve 4116 is turned on, and the auxiliary heat source solenoid valve 4115 is turned off. the

The circulating water sent from the solid organic waste treatment system 41 to the waste water and waste gas treatment system 42 using liquid high-temperature anaerobic treatment through the circulating water output pipe 4124 is returned to the solid organic waste treatment by the circulating water return pipe 4106 after passing through the heat exchanger C4205 System 41. the

The sewage sent in by the sewage output pipe 4126 of the solid organic waste treatment system 41 is first heated by the heat exchanger B4203, and then enters the heat exchanger C4205 through the connecting pipe 4204 for heating, and is then heated by the liquid high-temperature treatment equipment after two stages of heating. The water pipe 4206 flows into the liquid high-temperature anaerobic treatment equipment 4208 for high-temperature anaerobic treatment, which kills pathogenic bacteria while biologically digesting the sewage. the

When the liquid high-temperature anaerobic reaction temperature is lower than the set temperature, start the electric heater 4207 to heat the liquid high-temperature anaerobic treatment equipment. the

The liquid high-temperature anaerobic treatment equipment 4209 is equipped with a convenient device for adding high-temperature anaerobic bacteria mothers, and adds high-temperature anaerobic bacteria mothers according to the needs of high-temperature anaerobic reactions. the

The liquid high-temperature anaerobic treatment equipment is equipped with an insulation layer. the

The effluent after liquid high-temperature anaerobic treatment enters the heat exchanger B4203 through the outlet pipe 4201 of the liquid high-temperature treatment equipment, and after heat exchange and cooling with the sewage flowing into the system for treatment, it enters through the water inlet pipe 4202 of the medium-temperature aerobic biological deodorization filter tower Medium temperature aerobic biological deodorization filter tower 4209. the

The biogas generated by the high-temperature anaerobic fermentation reaction in the liquid high-temperature anaerobic treatment equipment 4208 flows out from the biogas discharge pipe 4223, and is collected and used by the biogas collection device 4226 after being treated by the dehydration device 4224 and the desulfurization device 4225. the

The sewage entering the mesophilic aerobic biological deodorization filter tower 4209 is subjected to mesophilic aerobic fermentation and digestion treatment in the mesophilic aerobic biological deodorization filter tower 4209. the

The waste gas produced by solid high-temperature aerobic fermentation reaction passes through the waste gas output pipe 4120, the fresh air passes through the suction pipe B4211, passes through the heat exchanger D 4212, the fan C 4213, and the air inlet pipe 4214 of the medium-temperature aerobic biological deodorization filter tower to the medium-temperature aerobic biological deodorization. Odor filter tower 4209 Fermentation tank under the liquid surface is sprayed and aerated through the aeration head, the gaseous ammonia in the waste gas dissolves in the medium-temperature fermentation liquid, and the gas insoluble in water passes through layers of biological filters, and is digested and deodorized by microorganisms. Exhaust port 4210 vents to atmosphere. the

Mesophilic aerobic biological deodorization filter tower 4209 has a convenient device for adding mesophilic aerobic bacteria and photosynthetic bacteria. According to the needs of mesophilic aerobic biological reactions, mesophilic aerobic bacteria and photosynthetic bacteria are added. the

After the mesophilic aerobic fermentation and digestion treatment is carried out in the mesophilic aerobic biological deodorization filter tower 4209, the treated fermented liquid flows into the treatment liquid pool 4217 through the overflow pipe 4218 of the mesophilic aerobic biological deodorization filter tower. The liquid fermented liquid has high nutrient and organic matter content, is odorless, and has no harmful pathogenic bacteria, and can be sold on the spot as a liquid organic fertilizer. the

For long-distance transportation that requires high-concentration liquid organic fertilizers, the supernatant of the treatment liquid in the treatment liquid pool 4217 is sent to the membrane treatment equipment 4220 for processing through the water pump F 4215, the treatment liquid delivery pipe 4216, and the filter 4219. The effluent of the membrane treatment equipment flows out from the reclaimed water outflow pipe 4222, which can be used to wash the filter bag and the site, while the concentrated fermented liquid left after being filtered flows out from the concentrated fermented liquid outflow pipe 4221, which has high nutrient and organic matter content. And it is odorless and has no harmful pathogenic bacteria, and can be sold as a liquid organic fertilizer. The solid matter left by the filter 4219 is sent to the solid organic waste treatment system 41 for treatment. the

Specific implementation mode two:

Organic waste enters the vertical pipe 202 through the organic waste source separation system 1 through the organic waste input device 101 installed by each household and the miter pipe 214 of the organic waste delivery system 2 .

After the organic waste enters the vertical pipe 202, the solenoid valve 209 on the horizontal pipe pressure water pipe 210 connected to the vertical pipe 202 is energized and connected. Under the action of pressure water, the organic waste reaches the automatic crushing and bagging machine 304 of the organic waste automatic bagging system 3 through the vertical pipe 202, the elbow 203, the horizontal pipe 204, the sewage collection horizontal pipe 205, and the sewage collection vertical pipe 206 feed port. the

The solid part of the organic waste is crushed by the automatic crushing and bagging machine 304 and loaded into a chemical fiber filter bag. After the filter bag is full, it is moved to the filter bag waiting area. the

The liquid part filtered from the automatic crushing and bagging machine 304 and the filter bag waiting area flows into the first sewage pool 307 . Part of the sewage enters the high-level water tank 215 through the pressure water delivery pipe 216 under the action of the water pump A 207, and is supplied to the organic waste delivery system 2 for use. The high water tank is equipped with a liquid level control device. the

When the water level of the high level water tank is lower than the set low value, the liquid level control system of the first sewage tank will start the water pump A 207 to send the sewage into the high level water tank 215 through the pressure water delivery pipe 216, when the water level of the high level water tank reaches the set high level When the value is reached, the level control system of the first sewage tank will turn off the water pump A 207. When the liquid level of the first sewage tank was higher than the set value, the liquid level control system of the first sewage tank would start the water pump B 305 to transport the sewage to the second sewage tank 4101 of the solid organic waste treatment system 41 through the sewage pipe, The liquid level control system also ensures that the liquid level of the first sewage tank 307 is not lower than a lower limit liquid level, and the lower limit liquid level ensures that the organic waste conveying system 2 can be supplied with water. the

The foul smell in the bagging bin is extracted by blower fan A 302, and is discharged through the vertical pipe 202 through the exhaust pipe 301. the

The solid organic waste packed into the filter bag is transported to the solid organic waste treatment system 41 of the organic waste treatment system 4 . The solid organic waste is sent to the centrifugal solid-liquid separation equipment 4104 together with the filter bag, and the solid-liquid separation is carried out under the action of centrifugal force. After the separation, the bag emptying operation is carried out, and the dehydrated solid organic waste is poured out from the filter bag And send the drum type high-temperature aerobic fermentation reactor 4130 to carry out high-temperature aerobic fermentation treatment. the

The sewage separated by the centrifugal solid-liquid separation equipment 4104 enters the second sewage pool 4101, the sewage from the organic waste automatic bagging system 3 enters the second sewage pool 4101 through the sewage pipe 306, and the sewage from the waste water and gas treatment system 43 passes through the second sewage pool 4101. The sewage circulation return pipe 4103 enters the second sewage pool 4101 . The sewage in the second sewage pool 4101 flows into the sewage circulation outlet pipe 4125 through the water pump C4102, and returns to the second sewage pool 4101 from the sewage circulation return pipe 4103 through the heat exchanger D4212. The sewage in the second sewage pool 4101 is sent to the waste water waste gas treatment system 43 that adopts liquid high-temperature aerobic treatment through the water pump E 4128 through the sewage output pipe 4126 for processing. the

After the solid organic waste is fermented by the drum-type high-temperature aerobic fermentation reactor 4130, it is odorless and has no harmful pathogenic bacteria. After aging, it can be sold as agricultural organic fertilizer. the

The oxygen required for the solid high-temperature aerobic fermentation reaction is supplemented by air sucked from the atmosphere. The air passes through the suction pipe A4121 and is heated by the heat exchanger A4123, and then enters the drum-type high-temperature aerobic fermentation reactor 4130 through the air inlet pipe 4129 of the aerobic fermentation reactor. The exhaust gas produced by the high-temperature aerobic fermentation reaction is extracted from the drum-type high-temperature aerobic fermentation reactor 4130 by the fan B 4119 through the exhaust pipe 4118 of the aerobic fermentation reactor, and sent to the waste gas that is treated with liquid high-temperature aerobic fermentation through the exhaust gas output pipe 4120. Wastewater and waste gas treatment system 43 for treatment. the

The hot water required by the drum-type high-temperature aerobic fermentation reactor 4130 is initially provided by the auxiliary heat source 4114 . The water pump D4112 absorbs water from the water pump inlet pipe 4111, and the outlet water of the water pump D4112 enters the auxiliary heat source 4114 through the auxiliary heat source gate valve 4113, and enters the drum type high-temperature aerobic fermentation reactor through the auxiliary heat source solenoid valve 4115 and the aerobic fermentation reactor water inlet pipe 4117 after heating 4130's water jacket. The outlet water of the water jacket enters the heat exchanger A4123 through the outlet pipe 4122 of the aerobic fermentation reactor, heats the air, and then sends it through the outlet pipe 4124 of the circulating water to the wastewater and waste gas treatment system 43 using liquid high-temperature aerobic treatment. The circulating water returned from the wastewater waste gas treatment system 43 that adopts liquid high-temperature aerobic fermentation treatment flows into the water inlet pipe 4111 through the circulating water return pipe 4106. the

The water in the water pump water inlet pipe 4111 is initially provided by the water supply pipe 4105, and then provided by the outside through the water inlet valve 4107 and the gate valve 4110. After the pipeline of the circulating water system is filled with water, close the gate valve 4110 and fill the pressure water tank 4109 with water. After the pressure water tank is filled with water to meet the requirements, close the water inlet valve 4107 and open the gate valve 4110 to automatically replenish water from the pressure water tank to the circulating water system. After the water in the circulating water system is heated and expanded, the excess water is discharged from the drain pipe 4127 through the drain valve 4108 . the

When the heat generated by the high-temperature aerobic fermentation reaction can meet the needs of the entire system, the auxiliary heat source bypass solenoid valve 4116 is turned on, and the auxiliary heat source solenoid valve 4115 is turned off. the

The circulating water sent from the solid organic waste treatment system 41 through the circulating water output pipe 4124 to the waste water and waste gas treatment system 43 that adopts liquid high-temperature aerobic fermentation treatment is returned to the solid organic waste by the circulating water return pipe 4106 after passing through the heat exchanger C4205 Processing system 41 . the

The sewage sent in by the sewage output pipe 4126 of the solid organic waste treatment system 41 is first heated by the heat exchanger B4203, and then enters the heat exchanger C4205 through the connecting pipe 4204 for heating, and is then heated by the liquid high-temperature treatment equipment after two stages of heating. The water pipe 4206 flows into the liquid high-temperature aerobic fermentation treatment equipment 4303 for high-temperature aerobic fermentation treatment, and kills pathogenic bacteria while biologically digesting the sewage. the

The waste gas generated by the solid high-temperature aerobic fermentation reaction passes through the waste gas output pipe 4120, and the fresh air enters the liquid high-temperature aerobic fermentation treatment equipment 4303 through the suction pipe C 4301 through the fan D 4302 to aerate the high-temperature sewage. Under the joint action of species and oxygen, the sewage undergoes high-temperature aerobic reaction. the

The liquid high-temperature aerobic treatment equipment 4303 is equipped with a device for conveniently adding thermophilic aerobic bacteria mothers, and adding thermophilic aerobic bacteria mothers according to the needs of high-temperature aerobic reactions. the

The liquid high-temperature aerobic treatment equipment is equipped with an insulation layer. the

The effluent treated by liquid high-temperature aerobic fermentation enters the heat exchanger B4203 through the outlet pipe 4201 of the liquid high-temperature treatment equipment, and after heat exchange and cooling with the sewage flowing into the system for treatment, it passes through the water inlet pipe 4202 of the medium-temperature aerobic biological deodorization filter tower Enter the medium temperature aerobic biological deodorization filter tower 4209. the

The sewage entering the mesophilic aerobic biological deodorization filter tower 4209 is subjected to mesophilic aerobic fermentation and digestion treatment in the mesophilic aerobic biological deodorization filter tower 4209. the

The foam produced by the liquid high-temperature aerobic fermentation reaction is sent to the liquid medium-temperature aerobic biological deodorization filter tower 4209 to spray the filter layer through the foam outflow pipe 4307, the water pump G 4306, and the foam delivery pipe 4305. the

The exhaust gas produced by the liquid high-temperature aerobic fermentation reaction passes through the exhaust pipe 4304 of the liquid high-temperature aerobic fermentation treatment equipment, the fresh air passes through the suction pipe B 4211, passes through the heat exchanger D 4212, and the fan C 4213 enters through the medium-temperature aerobic biological deodorization filter tower The trachea 4214 aerates through the aeration head under the liquid surface of the medium-temperature aerobic biological deodorization filter tower 4209 fermentation tank, the gaseous ammonia in the waste gas dissolves in the medium-temperature fermentation liquid, and the insoluble gas part passes through the layers of biological filters upwards, After being digested and deodorized by microorganisms, it is discharged to the atmosphere through the exhaust port 4210. the

Mesophilic aerobic biological deodorization filter tower 4211 has a convenient device for adding mesophilic aerobic bacteria and photosynthetic bacteria. According to the needs of mesophilic aerobic biological reactions, mesophilic aerobic bacteria and photosynthetic bacteria are added. the

After the mesophilic aerobic fermentation and digestion treatment is carried out in the mesophilic aerobic biological deodorization filter tower 4209, the treated fermented liquid flows into the treatment liquid pool 4217 through the overflow pipe 4218 of the mesophilic aerobic biological deodorization filter tower. The liquid fermented liquid has high nutrient and organic matter content, is odorless, and has no harmful pathogenic bacteria, and can be sold on the spot as a liquid organic fertilizer. the

For long-distance transportation that requires high-concentration liquid organic fertilizers, the supernatant of the treatment liquid in the treatment liquid pool 4217 is sent to the membrane treatment equipment 4220 for processing through the water pump F 4215, the treatment liquid delivery pipe 4216, and the filter 4219. The effluent of the membrane treatment equipment flows out from the reclaimed water outflow pipe 4222, which can be used to wash the filter bag and the site, while the concentrated fermented liquid left after being filtered flows out from the concentrated fermented liquid outflow pipe 4221, which has high nutrient and organic matter content. And it is odorless and has no harmful pathogenic bacteria, and can be sold as a liquid organic fertilizer. The solid matter left by the filter 4219 is sent to the solid organic waste treatment system 41 for treatment. the

Claims (7)

1. the source separation governing system of an organic waste is characterized in that: comprise organic waste source separation system, organic waste induction system, organic waste automatic bagging system, organic refuse treating system; Described organic waste source separation system is connected with the organic waste induction system, described organic waste induction system is connected with organic waste automatic bagging system, described organic waste automatic bagging system uses the chemical fibre filter bag, the organic waste that is bagging and filter liquor are transported to respectively organic refuse treating system and are processed.

2. the source separation governing system of organic waste according to claim 1 is characterized in that: described organic waste source separation system is comprised of the organic waste input unit; The organic waste input unit is included in the nappy of washing of the discharging rubbish from cooking of installing in the kitchen, in the lavatory economical toilet or water-saving squatting pan is installed, and the discharge pipe of these equipment is connected with the inclined pipe of organic waste induction system.

3. the source separation governing system of organic waste according to claim 1 is characterized in that: described organic waste induction system by vertical tube, elbow and the threeway of many inclined pipes, vertical transport organic waste, be responsible for the transverse tube of horizontal feed and collect dirty transverse tube, the dirty vertical tube of collection, press water water system forming; Each vertical tube stretches out the open air by the roof of residential building, the top is equipped with unpowered turbine blast cap or blower fan, the delivery pipe of the organic waste input unit of the kitchen of every family and toilet is connected with vertical tube by inclined pipe, and vertical tube extends downward basement or Stilt layer; At basement or Stilt layer, each vertical tube is connected with each transverse tube by elbow or by threeway, and each transverse tube is carried to the dirty transverse tube of collection and compiled, and the end that collects dirty transverse tube is the dirty vertical tube of collection, the charging aperture in the lower end that integrates dirty vertical tube as organic waste automatic bagging system; Each elbow is provided with shower nozzle, and the interface that links to each other with the press water tube connector is arranged; Bottom in transverse tube and the dirty transverse tube pipeline of collection just arranges a shower nozzle every a segment distance, and all there is the interface that links to each other with the press water tube connector at each shower nozzle position; The water spraying direction of all shower nozzles is consistent with the throughput direction of pipeline; The principal pressure water pipe links to each other with the transverse tube penstocks through each magnetic valve, and the transverse tube penstocks link to each other with the interface of transverse tube with elbow shower nozzle position by tube connector; The principal pressure water pipe links to each other with the dirty transverse tube penstocks of collection, collects dirty transverse tube penstocks and links to each other by the interface of tube connector with the dirty transverse tube of collection and elbow shower nozzle position; The water inlet end of principal pressure water pipe links to each other with the elevated tank water side, and the water inlet end of elevated tank links to each other with the press water carrier pipe, and elevated tank is equipped with fluid level control device.

4. the source separation governing system of organic waste according to claim 1 is characterized in that: described organic waste automatic bagging system is comprised of pack storehouse, automatic pulverizing sack filling machine, filter bag as ready district, the first cesspool, exhausting system, sewage transport system, fluid level control device; The pack storehouse be one every smelly negative pressure confined space, collecting dirty vertical tube stretches in the pack storehouse from the top, collecting dirty vertical tube discharging opening is connected with the charging aperture of automatic pulverizing sack filling machine, be provided with filter bag as ready district on the next door of automatic pulverizing sack filling machine, the below in automatic pulverizing sack filling machine and filter bag as ready district is provided with the first cesspool, and the pack storehouse offers door; Blower fan A is equipped with in the top in pack storehouse, and the exhaust duct of blower fan is connected with the vertical tube of organic waste induction system; Be provided with two water pumps in the first cesspool, water pump A is the water supply pump of organic waste induction system, and the delivery port of water pump A links to each other with elevated tank by the press water carrier pipe, and the outlet pipe of water pump B links to each other with organic refuse treating system; At the first cesspool tank level control system is housed.

5. the source separation governing system of organic waste according to claim 1, it is characterized in that: described organic refuse treating system comprises the solid organic castoff treatment system, and the solid organic castoff treatment system is comprised of organic waste solid-liquid separating equipment, drum-type aerobic fermentation reactor, air inlet system and exhaust system, circulation; The below of organic waste solid-liquid separating equipment is provided with the second cesspool, and the water pump B outlet pipe of organic waste automatic bagging system links to each other with the second cesspool; Be provided with two water pumps at the second cesspool, the outlet pipeline of water pump E links to each other with the pollutant treatment heat exchanger B of organic refuse treating system; The outlet pipeline of water pump C links to each other with the pollutant treatment heat exchanger D of organic refuse treating system; The outlet pipe of heat exchanger links to each other with cesspool; Drum-type aerobic fermentation reactor has charging and discharging mouth and inlet and outlet hole, also is provided with coaxial water jacket in the outside of cylinder in addition; The air intake duct A of air inlet system and exhaust system links to each other with aerobic fermentation reactor air inlet pipe through heat exchanger A, and aerobic fermentation reactor blast pipe links to each other with the pollutant treatment system through blower fan B, exhaust output tube; The water inlet pipe of water pump D links to each other with feed pipe by gate valve, water intaking valve, the outlet pipe of water pump D links to each other with the water inlet pipe of auxiliary thermal source through gate valve, the outlet pipe of auxiliary thermal source links to each other with aerobic fermentation reactor water inlet pipe through the auxiliary thermal source magnetic valve, aerobic fermentation reactor outlet pipe links to each other with the waste water and gas system through heat exchanger A, recirculated water efferent duct, and the recirculated water return pipe that links to each other with the waste water and gas system links to each other with the water inlet pipe of water pump D; Auxiliary thermal source is provided with the bypass branch road, is provided with the auxiliary thermal source bypass solenoid valve on the bypass branch road; Water intaking valve and the intervalve of the inlet pipeline of water pump are provided with pressure water tank, and pressure water tank is provided with draining valve and drainpipe.

6. the source separation governing system of organic waste according to claim 1, it is characterized in that: described organic refuse treating system comprises the pollutant treatment system, and the pollutant treatment system is comprised of liquid high temperature anaerobic treatment facility, heat exchanger, middle temperature aerobe deodorizing filter tower; The high-temperature medium water inlet of heat exchanger C links to each other with the recirculated water efferent duct of solid organic castoff treatment system, and the high-temperature medium delivery port of heat exchanger C links to each other with the recirculated water return pipe; The outlet pipeline that comes from the water pump E of solid organic castoff treatment system cesspool links to each other with liquid high temperature anaerobic treatment facility water inlet through heat exchanger B, communicating pipe, heat exchanger C, liquid high-temperature processing device water inlet pipe; Liquid high temperature anaerobic treatment facility has the convenient device that adds the high temperature anaerobic bacterial classification; Liquid high temperature anaerobic treatment facility is provided with heater; Liquid high temperature anaerobic treatment facility is provided with heat-insulation layer; The gas delivery port of liquid high temperature anaerobic treatment facility links to each other with the biogas discharge pipe, is connected to successively thereafter dewater unit, desulfurizer, sludge gas collecting device; The delivery port of liquid high temperature anaerobic treatment facility links to each other with the water inlet of middle temperature aerobe deodorizing filter tower through liquid high-temperature processing device outlet pipe, heat exchanger B, middle temperature aerobe deodorizing filter tower water inlet pipe; The exhaust output tube of solid organic castoff treatment system links to each other with middle temperature aerobe deodorizing filter tower by heat exchanger D, blower fan C, middle temperature aerobe deodorizing filter tower air inlet pipe with air intake duct B; Middle temperature aerobe deodorizing filter tower is provided with exhaust outlet; Middle temperature aerobe deodorizing filter tower has the convenient device that adds photosynthetic starter and have a liking for warm aerobic starter; The delivery port of middle temperature aerobe deodorizing filter tower links to each other with the processing liquid pool by middle temperature aerobe deodorizing filter tower overflow pipe.

7. the source separation governing system of organic waste according to claim 1, it is characterized in that: described organic refuse treating system comprises the pollutant treatment system, and the pollutant treatment system is comprised of liquid high-temperature aerobic fermentation treatment facility, heat exchanger, middle temperature aerobe deodorizing filter tower; The high-temperature medium water inlet of heat exchanger C links to each other with the recirculated water efferent duct of solid organic castoff treatment system, and the high-temperature medium delivery port of heat exchanger C links to each other with the recirculated water return pipe; The outlet pipeline that comes from the water pump E of solid organic castoff treatment system cesspool links to each other with liquid high-temperature aerobic treatment facility water inlet through heat exchanger B, communicating pipe, heat exchanger C, liquid high-temperature processing device water inlet pipe; Liquid high-temperature aerobic treatment facility has the convenient device that adds the thermophilic aerobic starter of high temperature; Liquid high-temperature aerobic treatment facility is provided with heat-insulation layer; The exhaust output tube of solid organic castoff treatment system links to each other with liquid high-temperature aerobic treatment facility by blower fan D with air intake duct C; Liquid high-temperature aerobic fermentation treatment facility links to each other with middle temperature aerobe deodorizing filter tower by foam effuser, water pump G, foam pipeline; The delivery port of liquid high-temperature aerobic treatment facility links to each other with the water inlet of middle temperature aerobe deodorizing filter tower through liquid high-temperature processing device outlet pipe, heat exchanger B, middle temperature aerobe deodorizing filter tower water inlet pipe; The exhaust output tube of liquid high-temperature aerobic treatment facility links to each other with middle temperature aerobe deodorizing filter tower by heat exchanger D, blower fan C, middle temperature aerobe deodorizing filter tower air inlet pipe with air intake duct B; Middle temperature aerobe deodorizing filter tower is provided with exhaust outlet; Middle temperature aerobe deodorizing filter tower has the convenient device that adds photosynthetic starter and have a liking for warm aerobic starter; The delivery port of middle temperature aerobe deodorizing filter tower links to each other with the processing liquid pool by middle temperature aerobe deodorizing filter tower overflow pipe.

Images