Tail dish resourceful treatment system
Technical Field
The utility model relates to a tail dish processing system, in particular to tail dish resourceful treatment system of integration.
Background
Vegetables are necessary for daily life. From the 'vegetable basket' proposed by the department of agriculture in 1998, central and local meat, egg, milk, aquatic product and vegetable production bases, improved variety breeding, feed processing and other service systems are established nationwide to ensure that residents eat fresh vegetables all the year round. The vegetable basket products are continuously and rapidly increased, and the situation of long-term shortage of subsidiary food supply in China is fundamentally changed. The vegetable basket project is surrounded in various places, such as Shandong, Gansu, Yunnan and the like, the supporting strength is increased, the standardization, the facility and the large-scale rapid promotion of the vegetable industry are realized, and the nationwide vegetable planting base is formed. Meanwhile, the matched refrigeration and logistics industry is developed correspondingly.
From vegetable planting bases to supermarket clean vegetables to come into the market, a large amount of defective vegetables and roots, stems, leaves and the like generated during refrigeration and clean vegetable processing become organic wastes, commonly called tail vegetables. According to statistics, the amount of the tail vegetables accounts for about 30-40% of the vegetable yield, and the effective utilization rate is low due to large yield, high water content (the average water content can reach about 95%), low effective components and lack of effective technologies. The soil is poured and buried at will, and after the soil is piled up, rotten and deteriorated, the air, the soil, the river and the underground water are polluted, the landfill site is also overloaded, a large number of mosquitoes and flies are bred, and the living environment and the body health of urban and rural residents are adversely affected. Therefore, the research on the effective utilization of the waste vegetables has important significance for relieving the pollution problem of the waste vegetables.
At present, the process of preparing the biogas by anaerobic fermentation is commonly adopted in the aspect of waste vegetable treatment. The main process comprises pretreatment, anaerobic fermentation and biochemical treatment of biogas slurry of the tailed vegetables. The anaerobic technology is complex to operate and has high technical requirements; meanwhile, the water content of the tailed vegetables is high (the average water content can reach about 95 percent), the effective dry matter is less, the unit biogas production amount is low, and meanwhile, the water content is high, the content of the contained nutrient substances is low, the biogas slurry amount is large (all seasons are produced), and sufficient soil digestion is difficult to achieve. Chinese patent CN 110272923A discloses a method and a system for recycling waste of waste tailstocks, the method comprises cleaning, removing impurities, sorting, pulping, blending materials, hydrolyzing and acidifying, anaerobic methane production and product recycling, wherein the product recycling is to reflux part of biogas slurry to a blending tank and reflux part of biogas slurry to a cstr anaerobic fermentation tank so as to improve the yield of biogas, but even after the product recycling, 50% of biogas slurry is still waiting for further treatment. Therefore, certain projects can only adopt a biochemical mode to treat the biogas slurry as 'wastewater', so that the loss of organic matters, N, P and K nutrients is caused, and meanwhile, the biochemical mode is influenced by the climatic environment and the quality of inlet water, the quality of the treated water is large in fluctuation and unstable, and secondary pollution is caused after the treated water is discharged.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem that a simple high-efficient, pollution-free, with low costs, the tail dish resourceful treatment system of high added value is provided.
In order to achieve the above object, the utility model provides a following technical scheme:
the utility model also provides a system of tail dish resourceful treatment, include: the solid-liquid separator is used for carrying out solid-liquid separation on the crushed Chinese cabbage; the collecting tank/tank is used for collecting the waste water separated by the solid-liquid separator; the first screen is used for removing particles which are harmful to the reverse osmosis membrane in the liquid in the collecting tank/tank; the liquid inlet pool/tank is used for collecting the tailed vegetable water after being screened by the screen I and the concentrated water after being treated by the reverse osmosis membrane I; VSEP for treating a liquid entering a liquid basin/tank; the clear liquid pool/tank I is used for collecting clear liquid after VSEP treatment and concentrated water after reverse osmosis membrane treatment; the first reverse osmosis membrane is used for treating liquid in the first clear liquid pool/tank; the clear liquid pool/tank II is used for collecting clear liquid treated by the reverse osmosis membrane I; the reverse osmosis membrane II is used for treating the liquid in the clear liquid pool/tank; the clean water tank is used for collecting the clean liquid treated by the reverse osmosis membrane II; a concentrated solution tank/jar having a stirrer for mixing the waste vegetable residue produced by the solid-liquid separator, the residue after the first screen, the residue after the second screen, and the concentrated water after the VSEP separation; a second screen mesh, which is used for screening the mixture fermented in the concentrated solution pool/tank according to the standard for preparing the liquid fertilizer; the liquid fertilizer matrix pool/tank is used for collecting liquid sieved by the screen II; a mixing tank/tank having a stirrer for mixing the liquid in the liquid fertilizer matrix tank/tank and the nutrient solution in the nutrient solution tank/tank to make a specific liquid fertilizer; and the nutrient solution pool/tank is used for providing nutrient solution required for preparing the specific liquid fertilizer.
Compared with the prior art, the beneficial effects of the utility model are that:
(1) the water and residue of the tailed vegetable do not fall to the ground.
(2) The waste vegetable water is treated by a full physical method (membrane separation), no chemicals are added, and no secondary pollution is caused.
(3) More than 90 percent of the plant nutrient elements of nitrogen, phosphorus and potassium in the tailvegetable water are returned to the water soluble fertilizer, the leaf fertilizer or the suspended fertilizer again.
(4) A large amount of water contained in a large amount of waste water is directly separated into clear water which can be directly discharged, recycled and even drunk through membrane separation; meanwhile, organic matters, nitrogen, phosphorus and potassium plant nutrient elements in the waste vegetable water are concentrated, so that the utilization value is improved.
(5) The process has simple and effective steps, high automation degree and low cost.
Drawings
Fig. 1 is a schematic view of the use flow of the tail vegetable recycling system of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
The utility model provides a tail dish resourceful treatment system, include: the solid-liquid separator is used for carrying out solid-liquid separation on the crushed Chinese cabbage; the collecting tank/tank is connected with the solid-liquid separator and is used for collecting the waste water separated by the solid-liquid separator; the screen I is connected with the collection tank/tank and is used for removing particles which are harmful to the reverse osmosis membrane in the liquid in the collection tank/tank; the liquid inlet pool/tank is connected with the screen I and the reverse osmosis membrane I and is used for collecting the tailwater screened by the screen I and the concentrated water treated by the reverse osmosis membrane I; VSEP (high frequency vibrating membrane filtration) connected to the intake basin/tank for treating the liquid in the intake basin/tank; the clear liquid pool/tank I is connected with the VSEP and is used for collecting clear liquid treated by the VSEP and concentrated water treated by the reverse osmosis membrane II; the first reverse osmosis membrane is connected with the first clear liquid pool/tank and is used for treating liquid in the first clear liquid pool/tank; the clear liquid pool/tank II is connected with the reverse osmosis membrane I and is used for collecting clear liquid treated by the reverse osmosis membrane I; the second reverse osmosis membrane is connected with the second clear liquid pool/tank and is used for treating liquid in the second clear liquid pool/tank; the clean water tank is connected with the second reverse osmosis membrane and is used for collecting the clean liquid treated by the second reverse osmosis membrane; the concentrated solution pool/tank is provided with a stirrer, is connected with the solid-liquid separator, the screen I, the VSEP and the screen II and is used for mixing the waste vegetable residue generated by the solid-liquid separator, the filter residue obtained after the screen I is screened, the filter residue obtained after the screen II is screened and concentrated water obtained after the VSEP is separated; the screen II is connected with the concentrated solution pool/tank and is used for screening the fermented mixture in the concentrated solution pool/tank according to the standard for preparing liquid fertilizer; the liquid fertilizer matrix pool/tank is connected with the second screen mesh and is used for collecting liquid screened by the second screen mesh; a mixing tank/tank having a stirrer connected to the liquid fertilizer matrix tank and the nutrient solution tank/tank for mixing the liquid in the liquid fertilizer matrix tank/tank and the nutrient solution in the nutrient solution tank/tank to make a specific liquid fertilizer; and the nutrient solution pool/tank is used for providing nutrient solution required for preparing the specific liquid fertilizer.
The use method of the system comprises the following steps:
crushing the collected and transported tail vegetables, performing solid-liquid separation on the crushed tail vegetables through a solid-liquid separator to obtain tail vegetable water and tail vegetable residues, feeding the separated tail vegetable water into a collecting pool/tank, and using the tail vegetable residues for later use;
removing particles which are harmful to a reverse osmosis membrane from the waste water in the collecting tank/tank by using a first screen, and feeding the screened liquid into a liquid inlet tank/tank;
clear liquid obtained after the liquid in the liquid inlet pool/tank is processed by VSEP (high frequency vibration membrane filtration technology) enters a clear liquid pool/tank I, and concentrated liquid enters a concentrated liquid pool/tank I;
clear liquid obtained after the liquid in the clear liquid pool/tank I is treated by the reverse osmosis membrane I enters a clear liquid pool/tank II, and concentrated liquid is returned to the clear liquid pool/tank II;
clear liquid obtained after the liquid in the clear liquid pool/tank II is treated by the reverse osmosis membrane II enters the clear water pool/tank, and concentrated liquid is returned to the clear liquid pool/tank I;
and the tailing residues generated by solid-liquid separation are metered and sent into the concentrated solution pool/tank, and a stirrer is arranged in the concentrated solution pool/tank at the same time, so that the concentrated solution and the fed tailing residues are stirred and uniformly mixed and then are effectively fermented. The mixing ratio is determined according to the standard of making liquid fertilizer, and the proportion of the ingredients can be adjusted by adjusting the conveying speed of each material.
The fermented concentrated solution and the mixture of the waste residues can pass through a screen mesh II with a corresponding aperture according to the standard for preparing the liquid fertilizer, the liquid after screening enters a liquid fertilizer matrix pool/tank, and is mixed into a corresponding specific liquid fertilizer (a water-soluble fertilizer, a leaf fertilizer or a suspended fertilizer) in a mixing pool/tank according to the proportion of the requirement for producing the corresponding liquid fertilizer (the water-soluble fertilizer, the leaf fertilizer or the suspended fertilizer) to the corresponding nutrient solution added from the nutrient solution pool/tank, and the mixing pool/tank is provided with a stirrer so as to be fully and uniformly mixed. If the filter residue can not be fully degraded in the screening process, the filter residue flows back to the concentrated solution pool/tank again for next degradation.