The resource Anhydrous ecological toilet of one provenance divergence type
Technical field
The invention belongs to hygienic device, be specifically related to the resource Anhydrous ecological toilet of a provenance divergence type.
Background technology
Anhydrous or the water-saving ecological type lavatory of being popular on market at present can be divided into four classes.1) the circulating water flushing type bio-toilet that urine is processed separately, it is by custom-designed separator, urine to be collected separately, automatically adds special agent to remove after peculiar smell, is back to toilet flushing; After ight soil is dry, can be made into agricultural fertilizer.Its advantage is to make dung recovery, but in use needs a small amount of supplementing water, and daily management requires higher, and the outer National Games of ight soil produce secondary pollution.2) the circulating water flushing type bio-toilet of fecaluria mixed processing, it is to adopt aerobe facture or embrane method etc., utilizes the metabolism of microorganism, dejection degradation is CO the most at last
2and H
2o, the water producing in process is reuse toilet flushing after treatment, also can enter environment.Its advantage is that fecaluria is handled together, and can reuse flush the toilet, but still needs regular moisturizing and regularly remove contamination, and pollutant levels can progressively increase with the operation in lavatory, causes its intractability large, and the cost that moves is for a long time too high, treatment effect is generally undesirable.3) exempt from water microorganism compost type bio-toilet, it can be divided into anaerobic type and aerobic type two classes, adopts anaerobic fermentation or aerobic composting process, and ight soil is finally processed into fertilizer or soil conditioner.Its advantage is without residue, anhydrous, but its deficiency is that the processing time is long, stink is dense, sanitary condition is poor, take up room large.4) exempt from Biodegradation type bio-toilet, as Chinese patent literature CN201409867Y, it adopts the special microorganism fungus kind of cultivating to process ight soil, larger molecular organics is degraded to the small organic molecules such as sugar, aliphatic acid and amino acid, the ight soil minimizing time is short, efficiency is high, and on market, popularization is hotter at present, but this type lavatory is subject to the restriction of fecaluria ratio, as too high in urine ratio, affect growth activity and the efficient degradation of flora; Its bacterial classification need regularly replace in addition and cost is high.
Summary of the invention
The object of the present invention is to provide a kind of resource Anhydrous ecological toilet with the source divergence type of completely anhydrous, resource, the feature such as maintenance is simple, operating cost is low, non-secondary pollution.
The technical scheme that realizes the object of the invention is: the resource Anhydrous ecological toilet of source divergence type, comprises source separation system and dry bioreactor; Described source separation system comprises: closet, be positioned at the conveyer belt that closet below turns forward, the urine collecting box that is positioned at conveyer belt below, the urine fixed nitrogen being communicated with urine collecting box and carry phosphorus device; Described dry bioreactor comprises the reative cell of three settings, in the first reative cell, be provided with agitating device, the second reative cell and the 3rd reative cell are positioned at the both sides of the first reative cell, in the second reative cell and the 3rd reative cell, be equipped with vertical spiral, the bottom of the second reative cell and the 3rd reative cell is communicated with by an auger conveyor horizontal and that be positioned at below, described conveyer belt rear end, and it is corresponding with described conveyer belt rear end that described auger conveyor is provided with opening; The top of the second reative cell and the 3rd reative cell is equipped with opening and is communicated with the first reative cell; The first reative cell bottom is provided with opening and is communicated with the bottom of the second reative cell; The second reative cell is provided with discharging opening.
The present invention also comprises with described urine fixed nitrogen and carries the urine clean unit that phosphorus device is connected.
The online gathering-device of the built-in urokinase of described urine collecting box, this device comprises tubular shell, in housing, be provided with heat exchange coil, and fill resin cation, the configuration of amount of resin be (100-1000) by one week amount of urine and amount of resin: 1 ratio setting, and the import of heat exchange coil and export and connect and compose small-sized cooling system with Small Refrigerating Equipment respectively, the two ends of housing are provided with urine filling mouth and urine outlet, housing is provided with the temperature online probe that is inserted into enclosure interior, and housing outer wall is enclosed with heat-insulation layer.
Described urine fixed nitrogen is carried phosphorus device and is comprised fixed nitrogen reactive tank, fixed nitrogen stillpot, the adsorption tank that zeolite powder is housed and the overflow launder at interval successively, between groove and groove, be provided with the intercommunicating pore of dislocation up and down, fixed nitrogen reactive tank is provided with automatic medicine feeder, and being provided with the urine import being connected with the urine outlet of the online gathering-device of urokinase, overflow launder is provided with urine outlet.
The bottom of described conveyer belt rear end is provided with scrapes closet.
Feature of the present invention is to utilize conveyer belt that ight soil is automatically separated with urine, utilize the online gathering-device of urine collecting box and urokinase to collect urokinase, utilize urine fixed nitrogen to carry phosphorus device and extract and collect nitrogen and the phosphorus in urine, utilize urine clean unit that remaining urine is further processed to the requirement that reaches integrated wastewater discharge standard one-level, directly discharge.Utilize dry bioreactor ight soil to be mixed with auxiliary material fully simultaneously and form the oxygen of holding concurrently, aerobic biotic environment produces aerobic compost, reaches the object of minimizing, innoxious, resource.
The present invention is owing to adopting said structure, overcome the deficiency of existing ecotypical toilet, can realize ight soil urine source separation, real-time online and collect that urokinase raw material, the real-time fixed nitrogen of urine are carried phosphorus, ight soil is produced biological organic fertilizer, there is completely anhydrous, resource, maintenance is simple, operating cost is low, non-secondary pollution, without number of users restriction, odorless, the advantage such as sanitary condition is good, treatment effect is good, occupy little space.
Below in conjunction with accompanying drawing, technical scheme of the present invention is described further.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Fig. 2 is the right view of Fig. 1.
Fig. 3 is the structural representation of dry bioreactor in the present invention.
Fig. 4 is the structural representation of the online gathering-device of urokinase in the present invention
Fig. 5 is the structural representation that in the present invention, urine fixed nitrogen is carried phosphorus device
Fig. 6 is the structure diagram of urinating clean unit in the present invention
The specific embodiment
Referring to Fig. 1-Fig. 3, the resource Anhydrous ecological toilet of source divergence type, comprises source separation system and dry bioreactor, described source separation system comprises: closet 6, be positioned at the conveyer belt 1 that closet 6 belows turn forward, the urine collecting box 3 that is positioned at conveyer belt 1 below, the urine fixed nitrogen that is communicated with urine collecting box 3 carries phosphorus device 4, conveyer belt 1 slope design is 1-10o, and it is connected with motor deceleration device 2, and the bottom of conveyer belt 1 rear end is provided with scrapes closet 11, described dry bioreactor comprises the reative cell 8 of three settings, 18, 19, in the first reative cell 18, be provided with agitating device 9, the second reative cell 19 and the 3rd reative cell 8 are positioned at the both sides of the first reative cell 18, in the second reative cell 19 and the 3rd reative cell 8, be equipped with vertical spiral 12, spiral 12 is connected with the motor 16 that is located at dry bioreactor top, agitating device 9 in the first reative cell 18 is connected with the spiral 12 in the second reative cell 19 by belt 20, the lower end of the second reative cell 19 is provided with circulation feed back pipe 15, at auger conveyor 5 horizontal by between circulation feed back pipe 15 and the bottom of the 3rd reative cell 8 and that be positioned at below described conveyer belt 1 rear end, be communicated with, the helical axis of auger conveyor 5 is connected with motor 13 by the belt pulley 17 of establishing thereon, it is corresponding with conveyer belt 1 rear end that auger conveyor 5 is provided with funnel 14, the top of the second reative cell 19 and the 3rd reative cell 8 is respectively equipped with opening 21,22 and is communicated with the first reative cell 18, the first reative cell 18 bottoms are provided with opening 23 and are communicated with the bottom of the second reative cell 19, the second reative cell 19 is provided with discharging opening 7, position towards closet 11 on bioreactor is provided with the sensor 10 of controlling conveyer belt 1 motion.
The online gathering-device 31 of the built-in urokinase of described urine collecting box 3, this device 31 as shown in Figure 4, comprise tubular shell 3103, in housing 3103, be provided with heat exchange coil 3106, and fill resin cation 3105, the configuration of amount of resin is (100-1000) by one week amount of urine and amount of resin: 1 ratio setting, import 3110 and the outlet 3102 of heat exchange coil 3106 connect and compose small-sized cooling system with Small Refrigerating Equipment respectively, the two ends of housing 3103 are provided with urine filling mouth 3101 and urine outlet 3108, housing 3103 is provided with and is inserted into the temperature online probe 3109 of enclosure interior and for being fixed on the fixing feet 3107 on urine collecting box 3, housing 3103 outer walls are enclosed with heat-insulation layer 3104.
Described urine fixed nitrogen is carried phosphorus device 4 as shown in Figure 5, comprise fixed nitrogen reactive tank 44, fixed nitrogen stillpot 45, the adsorption tank 46 that zeolite powder 47 is housed and the overflow launder 410 at interval successively, between groove and groove, be provided with the intercommunicating pore 49 of dislocation up and down, fixed nitrogen reactive tank 44 is provided with magnesia, sodium carbonate (or sodium acid carbonate, calcium carbonate) automatic medicine feeder 42,43, and be provided with the urine import 41 being connected with the urine outlet 3108 of the online gathering-device 31 of urokinase, overflow launder 410 is provided with urine outlet 48, and fixed nitrogen is carried phosphorus device 4 inner spaces and is set to 0.01-1m3.
The present invention also comprises the urine outlet 48 urine clean units 24 that are connected of carrying phosphorus device 4 with described urine fixed nitrogen, urine clean unit 24 as shown in Figure 6, by be provided with deflection plate 2402 anaerobic reaction groove 2403, be provided with micro-aerator 2408 and haydite 2405 micro-aeration biochemical groove 2404 and overflow chamber 2406 in series, anaerobic reaction groove 2403 and overflow chamber 2406 are respectively equipped with import 2401 and outlet 2407.
Operation principle of the present invention:
People enters behind lavatory, by human body sensor 10, start conveyer belt 1, urine flow to urine collecting box 3 certainly by the gradient, the online gathering-device 31 of the built-in urokinase of urine collecting box 3, urine flow when space that resin forms, the attached resins that combine in of raw material level protein such as its urokinase, by manually carrying out resin replacement by the cycle of 1-15 days, the resin of collection is sent into the extraction that urokinase specialized factory carries out urokinase etc.The heat exchange coil 3106 being connected with small-sized cooling system is for absorbing the heat of urine, and its temperature is detected and controlled by temperature online probe 3109.Urine is after resin is collected urokinase raw material, flow into urine fixed nitrogen and carry phosphorus device 4, when urine flow, the fashionable 0.01%-1% that magnesia, sodium carbonate mixing is pressed in to liquid measure by Automatic Dosing unit 42,43 adds, and forms magnesium ammonium phosphate and precipitates and collect as high-quality slow-release fertilizer.The discharge after urine clean unit 24 is processed of the remaining urine of Retained, because anaerobic reaction groove 2403 is arranged to baffling form, add micro-aeration biochemical groove 2404, can form in inside the environment of double oxygen, aerobic cycle alternation, reach the requirement of integrated wastewater discharge standard one-level, can directly discharge.
Ight soil drops on conveyer belt 1, conveyer belt 1 is the counter motion from flow path direction to urine, closet 11 is scraped in the lower end of conveyer belt, by pressing close to be less than the iron plate of 1 millimeter or stainless steel substrates, plastic sheet etc. with conveyer belt, is fixed on and on conveyer belt support, completes just slag, the just removing of stain on conveyer belt.Because Action of Gravity Field and scrape closet 11 work, the funnel 14 that ight soil falls on dry auger conveyor 5 enters dry bioreactor, in dry bioreactor, be equipped with by sawdust, rice bran, the auxiliary material that bamboo charcoal powder (wooden carbon dust) etc. form, auxiliary material falls into auger conveyor 5 by the circulation feed back pipe 15 of the second reative cell 19 bottoms, by auger conveyor 5, push the 3rd reative cell 8, spiral 12 in the second and the 3rd reative cell is upwards carried auxiliary material, through opening 21, 22 send in the first reative cell 18, the agitating device 9 of the first reative cell 18 constantly stirs auxiliary material, the auxiliary material again opening 23 through the first reative cell 18 bottoms enters the bottom of the second reative cell 19, so just form inner vertical circulation and the circulation of upper and lower region, ight soil is mixed with auxiliary material fully and form the oxygen of holding concurrently, aerobic biotic environment produces aerobic compost, reach minimizing, innoxious, the object of resource, the volume setting of pressing 0.01-1m3 of dry bioreactor.
During being stirred in lavatory and being used of dry type bioreactor inside, start operation 1 minute, and when long-time nobody uses in lavatory, the stirring of dry type bioreactor inside started once every 90 minutes, the fortune time is 30 seconds each time; The auger conveyor 5 of dry type bioreactor bottom and conveyer belt 1 interlock.