Self-oxygenate self-stirring domestic sewage purification device
Technical field
The present invention relates to a kind of self-oxygenate self-stirring domestic sewage purification device.
Background technology
At present, pollution of area source has become the great water environmental problems of China, and one of domestic sewage in rural areas by using source that to be pollution of area source main.The most of grange layouts of China are messy, lack unified planning, do not have complete sewage collecting pipe network and sewage treatment facility; It is second-rate with three format manure pits that major part has been built the family, and easy to leak, wastewater purifying efficiency are not good.Domestic sewage in rural areas by using treating pond based on anaerobic treatment is used widely in China various places, and this technology COD removes efficient height, stable, convenient management.But still existing denitrification effect poor, long-time running easily produces the problem of sludgd deposition.On the basis of existing sewage purifier, adopt the present invention, oxygen compatibility pool and anaerobic pond are built jointly up and down, both can save occupation of land, strengthen denitrification effect again, avoid sludgd deposition.
Summary of the invention
The objective of the invention is to overcome the deficiency of existing dispersant type domestic wastewater treating pond, provide a kind of from the domestic sewage purification device of oxygenation from stirring.
Self-oxygenate self-stirring domestic sewage purification device comprises the grid catchment area, first elastic filler, fine fack, water inlet pipe, the first anaerobic zone air chamber, aerobic area, a L type barometric pipe, the second anaerobic zone air chamber, the 2nd L type barometric pipe, third square hole, the 3rd anaerobic zone air chamber, blast inlet, the aerobic area air chamber, the 3rd L type barometric pipe, pull out airduct, fourth square hole, water shoot, swash plate, the settling region, the 3rd bidirectional flow siphunculus, the 3rd anaerobic zone, the 3rd elastic filler, second one-way flow control, second elastic filler, second anaerobic zone, second square opening, first one-way flow control, first anaerobic zone, first square opening; The grid catchment area links to each other with the settling region successively with first anaerobic zone, second anaerobic zone, the 3rd anaerobic zone, aerobic area; Grid is provided with fine fack in the catchment area, grid catchment area upper portion side wall is provided with water inlet pipe, bottom, grid catchment area links to each other with first anaerobic zone by first square opening, be provided with first elastic filler in first anaerobic zone, first one-way flow control, the one L type barometric pipe and the first anaerobic zone air chamber, the first anaerobic zone bottom links to each other with second anaerobic zone by second square opening, be provided with second elastic filler in second anaerobic zone, second one-way flow control, the 2nd L type barometric pipe and the second anaerobic zone air chamber, the second anaerobic zone top links to each other with the 3rd anaerobic zone by third square hole, be provided with the 3rd elastic filler in the 3rd anaerobic zone, the 3rd bidirectional flow siphunculus, the 3rd L type barometric pipe and the 3rd anaerobic zone air chamber, the 3rd anaerobic zone links to each other with aerobic area by the 3rd bidirectional flow siphunculus, aerobic area is first, two, directly over three anaerobic zones, this top, district is provided with blast inlet, pull out airduct, aerobic area top links to each other with the settling region by fourth square hole, be provided with swash plate in the settling region, the settling region upper portion side wall is provided with water shoot; Aerobic area runs through by first one-way flow control, a L type barometric pipe mutually with first anaerobic zone, aerobic area runs through by second one-way flow control, the 2nd L type barometric pipe mutually with second anaerobic zone, and aerobic area runs through by the 3rd bidirectional flow siphunculus, the 3rd L type barometric pipe mutually with the 3rd anaerobic zone; Refining plant top earthing, can consider the greening, blast inlet and pull out airduct from the device top pick out.
The self-oxygenate self-stirring domestic sewage purifying method is: sanitary sewage enters the grid catchment area through water inlet pipe, hydraulic detention time 12h, remove in the sewage behind the macrobead dirt, go into first anaerobic zone through the first square orifice flow, hydraulic detention time 16h, go into second anaerobic zone through the second square orifice flow, hydraulic detention time 16h, flow into the 3rd anaerobic zone through third square hole, hydraulic detention time 16h flows into aerobic area through the 3rd bidirectional flow siphunculus, hydraulic detention time 24h, flow into the settling region through fourth square hole, hydraulic detention time 12h is after the water shoot qualified discharge; The first anaerobic zone air chamber, the second anaerobic zone air chamber and the 3rd anaerobic zone air chamber are respectively by a L type barometric pipe, the 2nd L type barometric pipe and the realization of the 3rd L type barometric pipe air pressure balance with the aerobic area air chamber; First anaerobic zone, second anaerobic zone and the 3rd anaerobic zone are realized can effectively avoiding the sludgd deposition of anaerobic zone endoparticle from agitating function by first one-way flow control, second one-way flow control and the 3rd bidirectional flow siphunculus respectively; Aerobic area is by blast inlet and pull out the airduct realization from the oxygenation function, can reach 150mgO from oxygenation capacity
2/ (m
2D), denitrification effect can reach 0.1-0.2kgN/ (m
3D); Refining plant top earthing 0.5m, air intake flap are higher than the about 0.06m of earthing, pull out airduct and are higher than the about 0.1m of earthing, and water inlet pipe and the about 0.3-0.5m of rising pipe difference of altitude can guarantee that sewage flow to rising pipe certainly by water inlet pipe.
The invention has the beneficial effects as follows: 1) treating pond adopts buried integral structure, and aerobic area and anaerobic zone are built jointly up and down, the treating pond compact construction, and floor space is few; 2) treating pond adopts the anaerobism+oxygen technology of holding concurrently, and denitrogenation de-carbon effect is good; 3) treating pond adopts shallow-layer oxygenation principle, strengthens aerobic area from the oxygenation function, improves denitrification effect; 4) treating pond is provided with L type barometric pipe and single-direction and dual-direction circulating tube, can realize that anaerobic zone is from stirring and denitrification denitrogenation.
Description of drawings
Accompanying drawing is a kind of self-oxygenate self-stirring domestic sewage purification device synoptic diagram of the present invention;
Among the figure: grid catchment area 1, first elastic filler 2, fine fack 3, water inlet pipe 4, the first anaerobic zone air chamber 5, aerobic area 6, the one L type barometric pipes 7, the second anaerobic zone air chamber 8, the 2nd L type barometric pipe 9, third square hole 10, the 3rd anaerobic zone air chamber 11, blast inlet 12, aerobic area air chamber 13, the 3rd L type barometric pipe 14, pull out airduct 15, fourth square hole 16, water shoot 17, swash plate 18, settling region 19, the 3rd bidirectional flow siphunculus 20, the 3rd anaerobic zone 21, the 3rd elastic filler 22, second one-way flow control 23, second elastic filler 24, second anaerobic zone 25, second square opening 26, first one-way flow control 27, first anaerobic zone 28, first square opening 29.
Embodiment
As shown in drawings, self-oxygenate self-stirring domestic sewage purification device comprises grid catchment area 1, first elastic filler 2, fine fack 3, water inlet pipe 4, the first anaerobic zone air chamber 5, aerobic area 6, the one L type barometric pipes 7, the second anaerobic zone air chamber 8, the 2nd L type barometric pipe 9, third square hole 10, the 3rd anaerobic zone air chamber 11, blast inlet 12, aerobic area air chamber 13, the 3rd L type barometric pipe 14, pull out airduct 15, fourth square hole 16, water shoot 17, swash plate 18, settling region 19, the 3rd bidirectional flow siphunculus 20, the 3rd anaerobic zone 21, the 3rd elastic filler 22, second one-way flow control 23, second elastic filler 24, second anaerobic zone 25, second square opening 26, first one-way flow control 27, first anaerobic zone 28, first square opening 29; Grid catchment area 1 links to each other with settling region 19 successively with first anaerobic zone 28, second anaerobic zone 25, the 3rd anaerobic zone 21, aerobic area 6; Be provided with fine fack 3 in the grid catchment area 1, grid catchment area 1 upper portion side wall is provided with water inlet pipe 4,1 bottom, grid catchment area links to each other with first anaerobic zone 28 by first square opening 29, be provided with first elastic filler 2 in first anaerobic zone 28, first one-way flow control 27, the one L type barometric pipe 7 and the first anaerobic zone air chamber 5, first anaerobic zone, 28 bottoms link to each other with second anaerobic zone 25 by second square opening 26, be provided with second elastic filler 24 in second anaerobic zone 25, second one-way flow control 23, the 2nd L type barometric pipe 9 and the second anaerobic zone air chamber 8, second anaerobic zone, 25 tops link to each other with the 3rd anaerobic zone 21 by third square hole 10, be provided with the 3rd elastic filler 22 in the 3rd anaerobic zone 21, the 3rd bidirectional flow siphunculus 20, the 3rd L type barometric pipe 14 and the 3rd anaerobic zone air chamber 11, the 3rd anaerobic zone 21 links to each other with aerobic area 6 by the 3rd bidirectional flow siphunculus 20, aerobic area 6 is first, two, directly over three anaerobic zones, this top, district is provided with blast inlet 12, pull out airduct 15, aerobic area 6 tops link to each other with settling region 19 by fourth square hole 16, be provided with swash plate 18 in the settling region 19, settling region 19 upper portion side wall are provided with water shoot 17; Aerobic area 6 runs through by first one-way flow control 27, a L type barometric pipe 7 mutually with first anaerobic zone 28, aerobic area 6 runs through by second one-way flow control 23, the 2nd L type barometric pipe 9 mutually with second anaerobic zone 25, and aerobic area 6 runs through by the 3rd bidirectional flow siphunculus 20, the 3rd L type barometric pipe 14 mutually with the 3rd anaerobic zone 21; Refining plant top earthing can be considered greening, blast inlet 12 and pull out airduct 15 and pick out from the device top.
The self-oxygenate self-stirring domestic sewage purifying method is: sanitary sewage enters grid catchment area 1 through water inlet pipe 4, hydraulic detention time 12h, remove in the sewage behind the macrobead dirt, flow into first anaerobic zone 28 through first square opening 29, hydraulic detention time 16h, flow into second anaerobic zone 25 through second square opening 26, hydraulic detention time 16h, flow into the 3rd anaerobic zone 21 through third square hole 10, hydraulic detention time 16h flows into aerobic area 6 through the 3rd bidirectional flow siphunculus 20, hydraulic detention time 24h, flow into settling region 19 through fourth square hole, hydraulic detention time 12h is after water shoot 17 qualified discharges; The first anaerobic zone air chamber 5, the second anaerobic zone air chamber 8 and the 3rd anaerobic zone air chamber 11 are respectively by a L type barometric pipe 7, the 2nd L type barometric pipe 9 and 14 realizations of the 3rd L type barometric pipe air pressure balance with aerobic area air chamber 13; First anaerobic zone 28, second anaerobic zone 25 and the 3rd anaerobic zone 21 are realized can effectively avoiding the sludgd deposition of anaerobic zone endoparticle from agitating function by first one-way flow control 27, second one-way flow control 23 and the 3rd bidirectional flow siphunculus 20 respectively; Aerobic area 6 is by blast inlet 12 and pull out airduct 15 realizations from the oxygenation function, can reach 150mg O from oxygenation capacity
2/ (m
2D), denitrification effect can reach 0.1-0.2kgN/ (m
3D); Refining plant top earthing 0.5m, blast inlet 12 lids are higher than the about 0.06m of earthing, pull out airduct 15 and are higher than the about 0.1m of earthing, and water inlet pipe 4 and the about 0.3-0.5m of rising pipe 17 both difference of altitude can guarantee that sewage flow to rising pipe 17 certainly by water inlet pipe 4.
Operation scheme of the present invention is: sanitary sewage enters grid water collecting basin 1 through water inlet pipe 4, flow into first anaerobic zone 28 by first square opening 29, flow into second anaerobic zone 25 through second square opening 26, flow into the 3rd anaerobic zone 21 through third square hole 10, flow into aerobic area 6 through the 3rd bidirectional flow siphunculus 20, flow into settling region 19 through fourth square hole 16 again, after water shoot 17 qualified discharges; Air flows into aerobic area air chambers 13 by blast inlet 12, discharges aerobic area air chambers 13 by pulling out airduct 15, by contact with sewage in the aerobic area 6, thereby realization aerobic area 6 from the oxygenation function; Sewage is by the air pressure balance poising action of a L type barometric pipe 7, the 2nd L type barometric pipe 9 and the 3rd L type barometric pipe 14 in the aerobic area 6, through first one-way flow control 27, second one-way flow control 23 and the 3rd bidirectional flow siphunculus 20, flow into first anaerobic zone 28, second anaerobic zone 25 and the 3rd anaerobic zone 21 respectively, settled sludge in the anaerobic zone is produced fierce shock action, thus realize each anaerobic zone from agitating function.