CN105621840A - Pressure-difference-type green ecological septic tank and use method thereof - Google Patents
Pressure-difference-type green ecological septic tank and use method thereof Download PDFInfo
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- CN105621840A CN105621840A CN201610115056.0A CN201610115056A CN105621840A CN 105621840 A CN105621840 A CN 105621840A CN 201610115056 A CN201610115056 A CN 201610115056A CN 105621840 A CN105621840 A CN 105621840A
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- 238000000034 method Methods 0.000 title claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 84
- 230000009467 reduction Effects 0.000 claims description 68
- 238000005352 clarification Methods 0.000 claims description 58
- 239000007788 liquid Substances 0.000 claims description 55
- 230000000630 rising effect Effects 0.000 claims description 12
- 238000005192 partition Methods 0.000 claims description 10
- 239000002893 slag Substances 0.000 claims description 4
- 238000007689 inspection Methods 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 238000000855 fermentation Methods 0.000 abstract description 9
- 230000004151 fermentation Effects 0.000 abstract description 9
- 238000000354 decomposition reaction Methods 0.000 abstract 14
- 244000052616 bacterial pathogen Species 0.000 abstract 1
- 230000029087 digestion Effects 0.000 description 9
- 210000003608 fece Anatomy 0.000 description 7
- 239000007789 gas Substances 0.000 description 6
- 239000010871 livestock manure Substances 0.000 description 6
- 239000010865 sewage Substances 0.000 description 6
- 239000002689 soil Substances 0.000 description 5
- 102000002322 Egg Proteins Human genes 0.000 description 4
- 108010000912 Egg Proteins Proteins 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 210000004681 ovum Anatomy 0.000 description 4
- 230000003071 parasitic effect Effects 0.000 description 4
- 244000052769 pathogen Species 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 230000007812 deficiency Effects 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 230000001717 pathogenic effect Effects 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 238000005191 phase separation Methods 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 241000256113 Culicidae Species 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 241000255925 Diptera Species 0.000 description 1
- 241000305071 Enterobacterales Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000004176 ammonification Methods 0.000 description 1
- 239000005557 antagonist Substances 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
- C02F11/04—Anaerobic treatment; Production of methane by such processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/002—Apparatus and plants for the biological treatment of water, waste water or sewage comprising an initial buffer container
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Molecular Biology (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
Abstract
Provided are a pressure-difference-type green ecological septic tank and a use method thereof. The septic tank comprises a separated primary decomposition chamber, a separated advanced decomposition chamber and a separated clarifying chamber; the separated primary decomposition chamber comprises a primary decomposition front chamber and a primary decomposition rear chamber which are connected with each other through a pressure difference control water via pipe; the separated advanced decomposition chamber comprises an advanced decomposition front chamber and an advanced decomposition rear chamber, the advanced decomposition rear chamber is connected with the primary decomposition rear chamber through an overflow-type water via pipe, and the advanced decomposition front chamber is connected with the advanced decomposition rear chamber through a pressure difference control water via pipe; the separated clarifying chamber comprises a clarifying front chamber and a clarifying rear chamber, the clarifying front chamber is connected with the advanced decomposition front chamber through an overflow-type water via pipe, the clarifying rear chamber is connected with the clarifying front chamber through a pressure difference control water via pipe, and the clarifying rear chamber is provided with a water outlet pipe. According to the septic tank, grading decomposition and fermentation treatment can be automatically conducted, pathogenic bacteria are killed to the maximum extent, and greenization of the ecological environment is guaranteed.
Description
Technical field
The invention belongs to technical field of buildings, particularly relate to a kind of pressure reduction formula green ecological septic tank and using method thereof.
Background technology
Septic tank is process ight soil and the equipment of in addition filtering-depositing, is by sanitary sewage lattice precipitation, and mud carries out the small-sized process structures of anaerobic digestion. Its principle is that cured article decomposes at the bottom of pond, and the aquation object on upper strata, enters pipeline and flow away, prevent line clogging, has sufficient time hydrolysis to solidification object rubbish such as () ight soil.
The application of tradition septic tank has had more than 100 year history, technological line is the pattern that sewage contacts with mud, the sludge digestion degraded of deposition produces the digestion gas such as biogas, carbonic acid gas, hydrogen sulfide, mud is produced disturbance by the Float upward function of digestion gas, the perturbation action of mud can be allowed mud more abundant with mixing of biological flora by digestion gas, contributes to digestion degraded. But bottom mud rises with digestion gas, after bubble is overflowed, mud precipitates downwards again, and these rise and the mud of precipitation pollutes sewage again.
Three phase separation septic tank technology is on the basis of tradition septic tank, remain the advantage of muddy water mixing in septic tank, add the technology of " sewage, mud, digestion gas " three phase separation, in the water side of septic tank, three-phase separating device is set, mud, the digestion gas of water side are separated with sewage treatment process, avoid air supporting phenomenon to the interference of sewage disposal.
The ultimate principle of septic tank is that the principle such as the precipitating action utilizing the proportion of parasitic ovum to be greater than excrement urine mixed solution and produce and the fermentation of ight soil closing anaerobic, liquefaction, ammonification, biological antagonist removes and kills parasitic ovum and germ, mosquitos and flies multiplies in control, thus reaches the object of decontamination of human excreta. Three-grid septic tank is made up of three ponds being connected, middle by manure through pipe UNICOM, anaerobically fermenting, middle level is mainly utilized to cross excrement and parasitic ovum proportion is greater than general mixed solution proportion and is easy to the principle of precipitation, ight soil decomposes through the fermentation of more than 30 days in pond, middle level excrement liquid flow to 3 ponds by 1 pond successively, to reach precipitation or to kill the object of parasitic ovum and pathogen enterobacteria in ight soil, the 3rd pond excrement liquid becomes high-quality chemical fertilizer.
Owing to septic tank has new injection every day, therefore when sludge clearing, often there is manure fermentation and become thoroughly decomposed the problem of time deficiency, a large amount of pathogenic agent exists, therefore, it is necessary to a kind of better septic tank of design, to solve the problem.
Summary of the invention
For prior art Problems existing, the present invention provides a kind of problem solving manure fermentation deficiency when mud is drawn clearly, kills pressure reduction formula green ecological septic tank and the using method thereof of harmful levels of pathogens to the full extent.
In order to realize above-mentioned purpose, the present invention adopts following technical scheme:
A kind of pressure reduction formula green ecological septic tank, comprise shell, described shell is divided into the elementary corruption room of separate type, separate type degree of depth corruption room and separate type clarification room, described separate type elementary corruption room comprises room after elementary corruption cup and elementary corruption, described elementary corruption cup is provided with water inlet pipe, controlled water pipe by pressure reduction between described elementary corruption cup with room after described elementary corruption to be connected, described separate type degree of depth corruption room comprises degree of depth corruption cup and the rear room of degree of depth corruption, cross water pipe by overflow type between room with room after described elementary corruption after the corruption of the described degree of depth to be connected, controlled water pipe by pressure reduction between described degree of depth corruption cup with room after the corruption of the described degree of depth to be connected, described separate type clarification room comprises clarification cup and the rear room of clarification, cross water pipe by overflow type between described clarification cup with described degree of depth corruption cup to be connected, controlled water pipe by pressure reduction between room with described clarification cup after described clarification to be connected, after described clarification, room is provided with rising pipe.
Further, described shell is described separate type elementary corruption room, described separate type degree of depth corruption room and described separate type clarification room by the first baffle for separating, described separate type elementary corruption room is divided into room after elementary corruption cup and elementary corruption by second partition, described separate type degree of depth corruption room is separated into room after described degree of depth corruption cup and the corruption of the described degree of depth by described second partition, and described separate type clarification room is divided into room after described clarification cup and described clarification by described second partition.
Further, described elementary corruption cup, after room, described degree of depth corruption cup, the corruption of the described degree of depth, after room, described clarification cup and described clarification, the top cover of room has all offered inspection slag removing hole after described elementary corruption.
Further, described pressure reduction formula controlled water pipe and comprised control tube, the side of described control tube is provided with cup water inlet pipe, another side is provided with rear room rising pipe, the closed bottom of described control tube, top is provided with unlimited retaining plate, the lower section of described unlimited retaining plate is provided with cup hydraulic piston plate, the bottom of described cup hydraulic piston plate is connected with union lever, described union lever is arranged with spring, the top of described spring is connected to described cup hydraulic piston plate, bottom is connected to fixing seal plate, described fixing seal plate is placed on described union lever, can slide by relatively described union lever, the lower section of described fixing seal plate is provided with rear room hydraulic piston plate, described rear room hydraulic piston plate is fixed on described union lever, the bottom of described union lever is fixedly connected with pressure reduction control plug.
Further, described cup water inlet pipe is L-shaped, comprise horizontal section and vertical section, described horizontal section is vertical with described control tube, described vertical section is positioned at described control tube, and arrange with described control tube is concentric, described rear room hydraulic piston plate is sheathed on the periphery of described vertical section, and the control of described pressure reduction is filled in the bottom opening of described vertical section.
Further, described overflow type crosses entrance location that water pipe connects room after described elementary corruption lower than the outlet position connecting room after the corruption of the described degree of depth, and the entrance location connecting described degree of depth corruption cup is lower than the outlet position connecting described clarification cup.
Based on a using method for above-mentioned pressure reduction formula green ecological septic tank, comprising:
Step one: add excrement liquid in described elementary corruption cup by described water inlet pipe;
Step 2: septic tank carries out degenerating and fermenting automatically, and regularly draw clearly;
Step 3: the liquid after separation is discharged by the rising pipe clarifying rear room.
Further, after described elementary corruption cup and described elementary corruption, indoor liquid level is with time high, described pressure reduction controlled water pipe and was in closing condition, described elementary corruption cup accumulates the excrement liquid of certain time again, water pipe valve value was controlled when pressure reduction between room after described elementary corruption cup and described elementary corruption reaches described pressure reduction, it is open that described pressure reduction controlled water pipe, excrement liquid flows into room after described elementary corruption from described elementary corruption cup, after elementary corruption in room and described elementary corruption cup liquid level with, time high, described pressure reduction controlled water pipe and closed.
Further, when after described elementary corruption, the liquid level of room degenerates the liquid level of rear room less than or equal to the described degree of depth, described overflow type is crossed water pipe and is in closing condition, after described elementary corruption, room accumulates the excrement liquid of certain time again, when the liquid level of room after described elementary corruption crosses the outlet of water pipe higher than described overflow type, described overflow type is crossed water pipe and is opened, liquid indoor after described elementary corruption is indoor after flowing into the corruption of the described degree of depth, after the corruption of the described degree of depth after room and described elementary corruption indoor liquid level with, time high, described overflow type crosses water pipe closedown.
Further, excrement liquid flowed into described degree of depth corruption cup by room after the corruption of the described degree of depth, flowed into described clarification by described clarification cup after the method for room with to flow into the step of room after described elementary corruption by described elementary corruption cup identical, excrement liquid degenerates, by the described degree of depth, method that cup flows into described clarification cup, and to degenerate the step of rear room identical with flowing into the described degree of depth by room after described elementary corruption.
The useful effect of the present invention:
By septic tank being divided into the elementary corruption room of separate type, separate type degree of depth corruption room and separate type clarification room, and corruption room is separated and clarifies room for being divided into cup and rear room, avoid excrement liquid new to the indoor injection of same corruption continuously, ensure that the indoor manure fermentation of each corruption time of becoming thoroughly decomposed is enough, kill harmful levels of pathogens to the full extent, ensure ecological environment security health, employing pressure reduction controlled water pipe and overflow type crosses water pipe, make automatically to carry out in septic tank classification corruption and fermentative processing, easy to use, and can effectively ensure ecotope greenization.
Accompanying drawing explanation
Fig. 1 is the structural representation of pressure reduction formula green ecological septic tank of the present invention;
Fig. 2 is A-A diagrammatic cross-section in Fig. 1 of the present invention;
Fig. 3 is the diagrammatic cross-section that in Fig. 1, pressure reduction controlled water pipe;
In figure, the 1 elementary corruption room of separate type, 101 elementary corruption cups, room after 102 elementary corruptions, 2 separate type degree of depth corruption rooms, 201 degree of depth corruption cups, room after 202 degree of depth corruptions, 3 separate type clarification rooms, 301 clarification cups, room after 302 clarifications, 4 shells, 5 first dividing plates, 6 second partitions, 7 water inlet pipes, 8 rising pipes, 9 overflow types cross water pipe, 10 pressure reduction controlled water pipe, 11 inspection slag removing holes, 12 cup water inlet pipes, room rising pipe after 13, 14 control tubes, 15 fixed closed plates, 16 open wide retaining plate, 17 cup hydraulic piston plates, room hydraulic piston plate after 18, 19 springs, 20 union levers, 21 pressure reduction control plugs, 22 horizontal sections, 23 vertical sections.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is only a part of embodiment of the present invention, instead of whole embodiments. Based on the embodiment in the present invention, those of ordinary skill in the art, not making other embodiments all obtained under creative work prerequisite, belong to the scope of protection of the invention.
Need explanation, all directivity instruction (such as up, down, left, right, before and after in the embodiment of the present invention ...) only for explaining relative position relation between each parts, motion conditions etc. under a certain particular pose (as shown in drawings), if when this particular pose changes, then directionality instruction also correspondingly changes thereupon.
In addition, the description relating to " first ", " the 2nd " etc. in the present invention is only for describing object, and can not be interpreted as instruction or imply its relative importance or the implicit quantity indicating indicated technology feature. Thus, be limited with " first ", the feature of " the 2nd " can express or implicit comprise at least one this feature. In addition; technical scheme between each embodiment can be combined with each other; but must be can be embodied as basis with those of ordinary skill in the art; when technical scheme combination occur conflicting maybe cannot realize time will be understood that the combination of this kind of technical scheme does not exist, also not the present invention require protection domain within.
Such as Fig. 1, the present invention provides a kind of pressure reduction formula green ecological septic tank, comprise shell 4, shell 4 is divided into the elementary corruption room 1 of separate type, separate type degree of depth corruption room 2 and separate type clarification room 3, separate type elementary corruption room 1 comprises room 102 after elementary corruption cup 101 and elementary corruption, separate type degree of depth corruption room 2 comprises degree of depth corruption cup 201 and the rear room 202 of degree of depth corruption, and separate type clarification room 3 comprises clarification cup 301 and the rear room 302 of clarification.
Shell 4 is divided into the elementary corruption room 1 of separate type, separate type degree of depth corruption room 2 and separate type clarification room 3 by the first dividing plate 5 of longitudinal direction, separate type elementary corruption room 1 divides 6 to be divided into room 102 after elementary corruption cup 101 and elementary corruption by the second partition of transverse direction, separate type degree of depth corruption room 2 is separated into degree of depth corruption cup 201 and the rear room 202 of degree of depth corruption by the second partition 6 of transverse direction, and separate type clarification room 3 is divided into clarification cup 301 and the rear room 302 of clarification by the second partition 6 of transverse direction. After elementary corruption cup 101, elementary corruption, after room 102, degree of depth corruption cup 201, the rear room 202 of degree of depth corruption, clarification cup 301 and clarification, the top cover of room 302 has all been offered and has been checked slag removing hole 11, for checking corruption situation and scarfing cinder.
The front end of elementary corruption cup 101 is provided with water inlet pipe 7, controlled water pipe 10 by pressure reduction between elementary corruption cup 101 with room 102 after elementary corruption to be connected, pressure reduction controlled water pipe 10 and automatically opened or closed according to pressure reduction between room 102 after elementary corruption cup 101 and elementary corruption, when pressure reduction when between the two reaches the valve value that pressure reduction controlled water pipe 10, pressure reduction controlled water pipe 10 and automatically opened, so that the excrement liquid in elementary corruption cup 101 flows into after elementary corruption in room 102. After degree of depth corruption cup 201 and degree of depth corruption between room 202, all controlled water pipe 10 by above-mentioned pressure reduction between room 302 and clarification cup 301 after clarification and it was connected. After clarification, rear end, room 302 is provided with rising pipe 8.
Such as Fig. 1 and Fig. 3, pressure reduction formula controlled water pipe 10 and comprised control tube 14, the side of control tube 14 is provided with cup water inlet pipe 12, another side is provided with rear room rising pipe 13, the closed bottom of control tube 14, top is provided with unlimited retaining plate 16, the lower section opening wide retaining plate 16 is provided with cup hydraulic piston plate 17, the two bottom sides of cup hydraulic piston plate 17 is connected to union lever 20, each union lever 20 is arranged with a spring 19, the quantity of spring 19 is equal with the quantity of union lever 20, the top of spring 19 is connected to cup hydraulic piston plate 17, bottom is connected to fixing seal plate 15, fixing seal plate 15 is placed on union lever 20, can relatively slide by union lever 20. the lower section of fixing seal plate 15 is provided with rear room hydraulic piston plate 18, and rear room hydraulic piston plate 18 is fixed on union lever 20, and the bottom of union lever 20 is fixedly connected with pressure reduction control plug 21. cup water inlet pipe 12 is L-shaped, comprise horizontal section 22 and vertical section 23, horizontal section 22 is vertical with control tube 14, vertical section 23 is positioned at control tube 14, and arrange with control tube 14 is concentric, rear room hydraulic piston plate 18 is sheathed on the periphery of vertical section 23, and pressure reduction control plug 21 is filled in the bottom opening of vertical section 23. when pressure reduction between room 102 after elementary corruption cup 101 and elementary corruption be less than pressure reduction controlled water pipe 10 valve value time, the bottom opening that pressure reduction control plug 21 clogs cup water inlet pipe 12, the excrement liquid in elementary corruption cup 101 cannot enter after elementary corruption in room 102. when pressure reduction between room 102 after elementary corruption cup 101 and elementary corruption reach pressure reduction controlled water pipe 10 valve value time, pressure reduction control plug 21 is opened, leave the bottom of cup water inlet pipe 12, cup water inlet pipe 12 and rear room rising pipe 13 are connected, excrement liquid in elementary corruption cup 101 enters after elementary corruption in room 102, now pressure reduction control plug 21 drive union lever 20 moves down together, then spring 19 is compressed. when pressure reduction between room 102 after elementary corruption cup 101 and elementary corruption return to controlled water pipe 10 valve value lower than pressure reduction time, under the effect of spring 19 restoring force, pressure reduction control plug 21 returns to original position, the bottom opening of clogging cup water inlet pipe 12. it is identical with above-mentioned principle that pressure reduction between other corruption room controlled water pipe 10.
Such as Fig. 1 and Fig. 2, cross water pipe 9 by overflow type between room 202 with room 102 after elementary corruption after degree of depth corruption to be connected, when after elementary corruption, in room 102, liquid level reaches the outlet height that overflow type crosses water pipe 9, after elementary corruption after the excrement liquid automatic overflow in room 102 to degree of depth corruption in room 202. Also cross water pipe 9 by overflow type between clarification cup 301 with degree of depth corruption cup 201 to be connected, overflow type crosses entrance location that water pipe 9 connects room 102 after elementary corruption lower than the outlet position connecting room 202 after degree of depth corruption, and the entrance location connecting degree of depth corruption cup 201 is lower than the outlet position connecting clarification cup 301.
Above-mentioned pressure reduction formula green ecological septic tank has that weight capacity is strong, long service life, acid-alkali-corrosive-resisting, easy for installation, without advantages such as infiltrations. Adopt cup and rear room to be provided separately, avoid the continuous excrement liquid new to the indoor injection of same corruption, ensure that each is degenerated indoor manure fermentation and becomes thoroughly decomposed the time enough, kill harmful levels of pathogens to the full extent, ensure ecological environment security health.
The using method of above-mentioned pressure reduction formula green ecological septic tank is as follows:
Step one: add excrement liquid in elementary corruption cup 101 by water inlet pipe 7;
Step 2: septic tank carries out degenerating and fermenting automatically, and regularly draw clearly;
Step 3: the liquid after separation is discharged by the rising pipe 8 clarifying rear room 302.
Detailed process is: after injecting excrement liquid in elementary corruption cup 101, excrement liquid degenerates fermentation in elementary corruption cup 101, when liquid level in room 102 after elementary corruption cup 101 with elementary corruption is substantially with time high, pressure reduction controlled water pipe 10 and was in closing condition, elementary corruption cup 101 accumulates the excrement liquid of certain time (about 10 days) again, after elementary corruption cup 101 and elementary corruption, pressure reduction between room 102 can reach pressure reduction and controlled water pipe 10 valve value, it is open that pressure reduction controlled water pipe 10, excrement liquid flow into elementary corruption from elementary corruption cup 101 after room 102, after elementary corruption, room 102 and liquid level in elementary corruption cup 101 are with time high, pressure reduction controlled water pipe 10 and closed.
When after elementary corruption, the liquid level of room 102 degenerates the liquid level of rear room 202 less than or equal to the degree of depth, overflow type is crossed water pipe 9 and is in closing condition, after elementary corruption, room 102 accumulates the excrement liquid of certain time again, after elementary corruption, the liquid level of room 102 can cross the outlet of water pipe 9 higher than overflow type, overflow type is crossed water pipe 9 and is opened, after elementary corruption, the liquid in room 102 flows into after degree of depth corruption in room 202, after degree of depth corruption after room 202 and elementary corruption in room 102 liquid level with, time high, overflow type is crossed water pipe 9 and is closed.
Same as above, excrement liquid flowed into degree of depth corruption cup 201 by room 202 after degree of depth corruption, flowed into clarification by clarification cup 301 after the method for room 302 with to flow into the step of room 102 after elementary corruption by elementary corruption cup 101 identical, excrement liquid degenerates, by the degree of depth, method that cup 201 flows into clarification cup 301, and to degenerate the step of rear room 202 identical with flowing into the degree of depth by room 102 after elementary corruption. According to aforesaid method, excrement liquid can being made automatically to carry out classification corruption and fermentative processing in septic tank, it may also be useful to convenient, in the excrement liquid processed, the big degree of pathogenic agent is killed, and efficiently solves manure fermentation and becomes thoroughly decomposed the problem of time deficiency, ensure that ecotope greenization.
Above embodiment is only in order to illustrate the technical scheme of the present invention and unrestricted, although with reference to better embodiment to invention has been detailed explanation, those skilled in the art are to be understood that, the technical scheme of the present invention can be modified or equivalent replacement, and not departing from objective and the scope of the technical program, it all should be encompassed in the right of the present invention.
Claims (10)
1. a pressure reduction formula green ecological septic tank, it is characterized in that, comprise: shell, described shell is divided into the elementary corruption room of separate type, separate type degree of depth corruption room and separate type clarification room, described separate type elementary corruption room comprises room after elementary corruption cup and elementary corruption, described elementary corruption cup is provided with water inlet pipe, controlled water pipe by pressure reduction between described elementary corruption cup with room after described elementary corruption to be connected, described separate type degree of depth corruption room comprises degree of depth corruption cup and the rear room of degree of depth corruption, cross water pipe by overflow type between room with room after described elementary corruption after the corruption of the described degree of depth to be connected, controlled water pipe by pressure reduction between described degree of depth corruption cup with room after the corruption of the described degree of depth to be connected, described separate type clarification room comprises clarification cup and the rear room of clarification, cross water pipe by overflow type between described clarification cup with described degree of depth corruption cup to be connected, controlled water pipe by pressure reduction between room with described clarification cup after described clarification to be connected, after described clarification, room is provided with rising pipe.
2. pressure reduction formula green ecological septic tank according to claim 1, it is characterized in that: described shell is described separate type elementary corruption room, described separate type degree of depth corruption room and described separate type clarification room by the first baffle for separating, described separate type elementary corruption room is divided into room after elementary corruption cup and elementary corruption by second partition, described separate type degree of depth corruption room is separated into room after described degree of depth corruption cup and the corruption of the described degree of depth by described second partition, and described separate type clarification room is divided into room after described clarification cup and described clarification by described second partition.
3. pressure reduction formula green ecological septic tank according to claim 1, it is characterised in that: after described elementary corruption cup, described elementary corruption, after room, described degree of depth corruption cup, the corruption of the described degree of depth, after room, described clarification cup and described clarification, the top cover of room has all offered inspection slag removing hole.
4. pressure reduction formula green ecological septic tank according to claim 1, it is characterized in that: described pressure reduction formula controlled water pipe and comprises control tube, the side of described control tube is provided with cup water inlet pipe, another side is provided with rear room rising pipe, the closed bottom of described control tube, top is provided with unlimited retaining plate, the lower section of described unlimited retaining plate is provided with cup hydraulic piston plate, the bottom of described cup hydraulic piston plate is connected with union lever, described union lever is arranged with spring, the top of described spring is connected to described cup hydraulic piston plate, bottom is connected to fixing seal plate, described fixing seal plate is placed on described union lever, can slide by relatively described union lever, the lower section of described fixing seal plate is provided with rear room hydraulic piston plate, described rear room hydraulic piston plate is fixed on described union lever, the bottom of described union lever is fixedly connected with pressure reduction control plug.
5. pressure reduction formula green ecological septic tank according to claim 4, it is characterized in that: described cup water inlet pipe is L-shaped, comprise horizontal section and vertical section, described horizontal section is vertical with described control tube, described vertical section is positioned at described control tube, and arrange with described control tube is concentric, described rear room hydraulic piston plate is sheathed on the periphery of described vertical section, and the control of described pressure reduction is filled in the bottom opening of described vertical section.
6. pressure reduction formula green ecological septic tank according to claim 1, it is characterized in that: described overflow type crosses entrance location that water pipe connects room after described elementary corruption lower than the outlet position connecting room after the corruption of the described degree of depth, and the entrance location connecting described degree of depth corruption cup is lower than the outlet position connecting described clarification cup.
7. the using method based on pressure reduction formula green ecological septic tank according to claim 1, it is characterised in that, comprising:
Step one: add excrement liquid in described elementary corruption cup by described water inlet pipe;
Step 2: septic tank carries out degenerating and fermenting automatically, and regularly draw clearly;
Step 3: the liquid after separation is discharged by the rising pipe clarifying rear room.
8. using method according to claim 7, it is characterized in that: after described elementary corruption cup and described elementary corruption, indoor liquid level is with time high, described pressure reduction controlled water pipe and was in closing condition, described elementary corruption cup accumulates the excrement liquid of certain time again, water pipe valve value was controlled when pressure reduction between room after described elementary corruption cup and described elementary corruption reaches described pressure reduction, it is open that described pressure reduction controlled water pipe, excrement liquid flows into room after described elementary corruption from described elementary corruption cup, after elementary corruption in room and described elementary corruption cup liquid level with time high, described pressure reduction controlled water pipe and closed.
9. using method according to claim 8, it is characterized in that: when after described elementary corruption, the liquid level of room degenerates the liquid level of rear room less than or equal to the described degree of depth, described overflow type is crossed water pipe and is in closing condition, after described elementary corruption, room accumulates the excrement liquid of certain time again, when the liquid level of room after described elementary corruption crosses the outlet of water pipe higher than described overflow type, described overflow type is crossed water pipe and is opened, liquid indoor after described elementary corruption is indoor after flowing into the corruption of the described degree of depth, after the corruption of the described degree of depth after room and described elementary corruption indoor liquid level with time high, described overflow type is crossed water pipe and is closed.
10. using method according to claim 9, it is characterized in that: excrement liquid flowed into described degree of depth corruption cup by room after the corruption of the described degree of depth, flowed into described clarification by described clarification cup after the method for room with to flow into the step of room after described elementary corruption by described elementary corruption cup identical, excrement liquid degenerates, by the described degree of depth, method that cup flows into described clarification cup, and to degenerate the step of rear room identical with flowing into the described degree of depth by room after described elementary corruption.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610115056.0A CN105621840B (en) | 2016-02-29 | 2016-02-29 | A kind of differential green ecological septic tank and its application method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610115056.0A CN105621840B (en) | 2016-02-29 | 2016-02-29 | A kind of differential green ecological septic tank and its application method |
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Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS555724A (en) * | 1978-06-27 | 1980-01-16 | Matsushita Electric Works Ltd | Septic tank |
| JPH11104673A (en) * | 1997-09-30 | 1999-04-20 | Hitachi Chem Co Ltd | Septic tank |
| CN201386843Y (en) * | 2009-04-27 | 2010-01-20 | 周玉图 | Dynamic flow and pressure-difference balancing valve |
| CN203728693U (en) * | 2014-02-18 | 2014-07-23 | 苗岗 | Manure treatment system |
| CN104830912A (en) * | 2015-05-20 | 2015-08-12 | 陆永柱 | Method for generating biogas by parallel-type hydraulic-chamber biogas fermentation system |
| CN105314798A (en) * | 2015-11-26 | 2016-02-10 | 沈阳建筑大学 | Green ecological four-chamber septic tank and sewage treatment method |
| CN205398420U (en) * | 2016-02-29 | 2016-07-27 | 沈阳建筑大学 | Differential green ecologization manure pit |
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2016
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Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS555724A (en) * | 1978-06-27 | 1980-01-16 | Matsushita Electric Works Ltd | Septic tank |
| JPH11104673A (en) * | 1997-09-30 | 1999-04-20 | Hitachi Chem Co Ltd | Septic tank |
| CN201386843Y (en) * | 2009-04-27 | 2010-01-20 | 周玉图 | Dynamic flow and pressure-difference balancing valve |
| CN203728693U (en) * | 2014-02-18 | 2014-07-23 | 苗岗 | Manure treatment system |
| CN104830912A (en) * | 2015-05-20 | 2015-08-12 | 陆永柱 | Method for generating biogas by parallel-type hydraulic-chamber biogas fermentation system |
| CN105314798A (en) * | 2015-11-26 | 2016-02-10 | 沈阳建筑大学 | Green ecological four-chamber septic tank and sewage treatment method |
| CN205398420U (en) * | 2016-02-29 | 2016-07-27 | 沈阳建筑大学 | Differential green ecologization manure pit |
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| CN105621840B (en) | 2018-01-30 |
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Effective date of registration: 20200619 Address after: 253100 Shandong Province Economic Development Zone Bang de Lu Dezhou plain county No. 2 Patentee after: SHANDONG BANGDE OUJING ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: 110168 Liaoning province Shenyang Hunnan Hunnan Road No. 9 Patentee before: SHENYANG JIANZHU University |
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