CN201883001U - Novel high-turbidity and biochemistry integrated water purifier - Google Patents
Novel high-turbidity and biochemistry integrated water purifier Download PDFInfo
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- CN201883001U CN201883001U CN2010205788530U CN201020578853U CN201883001U CN 201883001 U CN201883001 U CN 201883001U CN 2010205788530 U CN2010205788530 U CN 2010205788530U CN 201020578853 U CN201020578853 U CN 201020578853U CN 201883001 U CN201883001 U CN 201883001U
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Abstract
The utility model belongs to water purifiers, and relates to a novel high-turbidity and biochemistry integrated water purifier which comprises a reaction chamber, a suspension clarifying chamber, an inclined tube settling chamber and an aeration biological filter chamber, wherein the reaction chamber (6) is inverse horn-shaped, a central mud conveying drum (9) and a mud conveying tube (8) are mounted in the center of the reaction chamber (6), and a mud hopper (7) is arranged at the periphery of the reaction chamber (6); the suspension clarifying chamber (32) is arranged on the mud hopper (7); the tube settling chamber (29) is mounted on the suspension clarifying chamber (32); the aeration biological filter chamber (20) is mounted at the top of equipment; a bearing layer (17) is arranged on a filter plate (16) of the filter chamber (20); filter media (18) are laid on the bearing layer (17); and a water outlet area (21) is arranged on the filter media. The water purifier integrates such advanced technologies as suspension clarifying, inclined tube settling, aeration biological filter and the like into a whole, realizes full-automatic operation, improves the clarifying efficiency, reduces the equipment volume, land occupation area and investment, is simple to operate and has low operation cost; and the comprehensive technical performance can achieve ideal effects.
Description
Technical field: the utility model relates to removing the water purifying plant of high turbidity inorganic pollutant and carbon containing, nitrogenous, phosphorus-containing matter pollutent, particularly a kind of novel high turbidity and biochemical integral water purifier simultaneously.
Background technology: prior art is most popular mostly to be reaction, suspension clarification, tube settling and four processing unit march-pasts of BAF, and its shortcoming has three: one, and each unit apportion floor space is big, particularly influences plant area, the cost height; The 2nd, the full-automatic operation of complex management and realization is complicated; The 3rd, many processing units are become single treatment facility separately, each the treatment stage water outlet mostly to store through intermediate pool, force (forcing) pump is sent into next unit and is gone to handle in the middle of the reuse again, investment is high, power consumption is high, working cost is high, maintenance capacity is big.
Summary of the invention: the sophisticated equipment that the purpose of this utility model is to provide a kind of incorporate realization coagulating, suspension clarification, tube settling, BAF novel process and has realized fully automatic operation.
Formation of the present utility model: form by upward flow reaction chamber, suspension clarifying chamber, tube settling chamber and upward flow aeration and biological filter chamber, reaction chamber is inverted tubaeform, wherein feel at ease central mud feeding drum, dredging tube are housed, the periphery is a bucket, and its top is the suspension clarifying chamber, and the tube settling chamber is installed on the suspension clarifying chamber, at the equipment top aeration and biological filter chamber is installed, be supporting layer on the filter chamber filter plate, lay filtrate on the supporting layer, exhalant region is arranged above the filtrate.
Equipment Foundations are simple RC Circular basis, and whole integral water purifier is installed on it.
Reaction chamber is positioned at the central authorities of equipment bottom, is vertically welded on the base plate, and water inlet pipe passes body, enters the bottom of reaction chamber, and central mud feeding drum is by dredging tube and reaction chamber welding.
There is the welding of inclined tube carriage and body the tube settling chamber below at the equipment middle part, assists on it and establishes the PVC honeycomb inclined-tube, and the space under it is the suspension clarifying chamber.
The aeration and biological filter chamber is at the equipment top, its filter plate and body welding, the filter plate carriage is in the filter plate bottom, upper end and body and filter plate welding, lower end and the welding of inclined tube carriage, the back flushing water inlet pipe, back flushing inlet pipe and aeration tube three pass body, and welding with it, the flitch settling region is an inverted tubaeform, is positioned at the equipment top, be vertically welded on the body top, grid type stabilier is welded on the inside top of body, and annular collecting vat and drip pan are welded on the top outer of body, and purify waste water water shoot and back flushing water shoot are in perforate and the welding with it of the bottom of drip pan, the vapor pipe of buffering water distributing area passes body and annular collecting vat, and perforate welding with it.
Sludge drainage system is surrounded by bucket, reaction chamber, body, annular porous sludge pipe and base plate welding, spoil disposal are responsible for and are passed body and welding with it, and manually-operated gate A and electrically operated valve are equipped with in its outer end, the clarification and effluent pipe passes body and welding with it on the bucket top, manually-operated gate B is installed in the lower end.
Compared with prior art, the utility model gathers modern techniquies such as suspension clarification, tube settling and BAF in one, realized full-automatic operation, improved purification efficiency, equipment volume, floor space and investment have been reduced, simple to operate, working cost is low, and comprehensive technical performance all can reach ideal effect.The utility model can be realized the combination of materialization (clarification, precipitation) and biochemical (BAF) optimization with pre-treatment that to remove high turbidity suspended substance be follow-up biochemistry; finally reach the purpose of not only efficiently removing suspended substance but also removing carbon containing (C), nitrogenous (N), phosphorous (P) pollutent simultaneously; guarantee to handle the up to standard and reuse of back sewage; the protection environment; realize sewage recycling, and have following purposes:
1. raw water turbidity can be dropped to 1~10mg/L from 5000mg/L;
2. be applicable to the trade effluent turbidity removal cleansing and recycling technology that high turbidity and condition are more abominable.As power plant, industrial and mining enterprises' boiler flushing cinder, waste water such as wastewater from blast furnace, coal mine, coal washing, mine, casting sand removal, various dust towards grey waste water, metallurgy and non-ferrous metal industry and the high-turbidity water of chemical industry and Coal Chemical Industry industry are processed into industrial circulate water;
3. be applicable to high turbidity rivers source water and micro-polluted water are processed into tap water or water of productive use.
Description of drawings:
Accompanying drawing is a structural representation of the present utility model.
Among the figure 1, the basis, 2, base plate, 3, water inlet pipe, 4, manually-operated gate B, 5, the clarification and effluent pipe, 6, reaction chamber, 7, bucket, 8, dredging tube, 9, central authorities' mud feeding drum, 10, the inclined tube carriage, 11, the PVC honeycomb inclined-tube, 12, the back flushing water inlet pipe, 13, the back flushing inlet pipe, 14, aeration tube, 15, filter, 16, filter plate, 17, supporting layer, 18, filtrate, 19, the filter plate carriage, 20, the aeration and biological filter chamber, 21, exhalant region, 22, grid type stabilier, 23, landing and railing, 24, annular collecting vat, 25, drip pan, 26, the flitch settling region, 27, vapor pipe, 28, the buffering water distributing area, 29, the tube settling chamber, 30, the water shoot of purifying waste water, 31, the back flushing water shoot, 32, the suspension clarifying chamber, 33, body, 34, sludge drainage system, 35, annular porous sludge pipe, 36, spoil disposal is responsible for, and 37, manually-operated gate A, 38, electrically operated valve.
Embodiment: as shown in the figure:
One. Equipment Foundations: Equipment Foundations 1 are simple RC Circular basis, and whole integral water purifier is installed on it.
Two. reaction chamber: reaction chamber 6 is an inverted tubaeform, be positioned at the central authorities of equipment bottom, be vertically welded on the base plate 2, base plate 2 is tiled on the basis 1, water inlet pipe 3 passes body 33, enters the bottom of reaction chamber 6, and welds with them, central authorities' mud feeding drum 9 is installed in the top center of reaction chamber 6, by dredging tube 8 and reaction chamber 6 welding.
Three. tube settling chamber and suspension clarifying chamber: there are inclined tube carriage 10 and body 33 welding in tube settling chamber 29 below at the equipment middle part, assists on it and establishes PVC honeycomb inclined-tube 11, and the space under it is suspension clarifying chamber 32.
Four. the aeration and biological filter chamber: aeration and biological filter chamber 20 is at the equipment top, its filter plate 16 and body 33 welding, boring and filter 15 is housed on the filter plate 16, it on it supporting layer 17, lay filtrate 18 on the supporting layer 17, it above the filtrate 18 exhalant region 21, filter plate carriage 19 is in filter plate 16 bottoms, upper end and body 33 and filter plate 16 welding, lower end and 10 welding of inclined tube carriage, back flushing water inlet pipe 12, back flushing inlet pipe 13 and aeration tube 14 threes pass body 33, and welding with it, back flushing water inlet pipe 12 and back flushing inlet pipe 13 are installed in the buffering water distributing area 28, aeration tube 14 is installed in the supporting layer 17, flitch settling region 26 is an inverted tubaeform, be positioned at the equipment top, be vertically welded on body 33 tops, grid type stabilier 22 is welded on the inside top of body 33, annular collecting vat 24 and drip pan 25 are welded on the top outer of body 33, purify waste water water shoot 30 and back flushing water shoot 31 in perforate and the welding with it of the bottom of drip pan 25, the vapor pipe 27 of buffering water distributing area 28 passes body 33 and annular collecting vat 24, and perforate welding with it.
Five. sludge drainage system: sludge drainage system 34 is surrounded by bucket 7, reaction chamber 6, body 33 etc., annular porous sludge pipe 35 and base plate 2 welding, spoil disposal is responsible for 36 and is passed body 33 and welding with it, manually-operated gate A37 and electrically operated valve 38 are equipped with in its outer end, clarification and effluent pipe 5 passes body 33 and welding with it on the bucket top, manually-operated gate B4 is installed in the lower end.
Six. stair and platform: landing and railing 23 are welded to the top from ground along body 33, platform ringwise, and face down bonding is connected to the high security personnel's railing of 900mm outside.
Claims (3)
1. a novel high turbidity and biochemical integral water purifier, by the upward flow reaction chamber, the suspension clarifying chamber, tube settling chamber and upward flow aeration and biological filter chamber are formed, it is characterized in that: reaction chamber (6) is an inverted tubaeform, wherein feel at ease central mud feeding drum (9) is housed, dredging tube (8), the periphery is bucket (7), its top is suspension clarifying chamber (32), tube settling chamber (29) is installed on suspension clarifying chamber (32), aeration and biological filter chamber (20) is installed at the equipment top, on the filter chamber filter plate (16) supporting layer (17), supporting layer (17) is gone up and is laid filtrate (18), and exhalant region (21) is arranged above the filtrate; Equipment Foundations (1) are simple RC Circular basis, and whole integral water purifier is installed on it; Aeration and biological filter chamber (20) is at the equipment top, its filter chamber filter plate (16) and body (33) welding, filter plate carriage (19) is in filter chamber filter plate (16) bottom, upper end and body (33) and filter chamber filter plate (16) welding, lower end and inclined tube carriage (10) welding, back flushing water inlet pipe (12), back flushing inlet pipe (13) and aeration tube (14) three pass body (33), and welding with it, flitch settling region (26) is an inverted tubaeform, be positioned at the equipment top, be vertically welded on body (33) top, grid type stabilier (22) is welded on the inside top of body (33), annular collecting vat (24) and drip pan (25) are welded on the top outer of body (33), purify waste water water shoot (30) and back flushing water shoot (31) in perforate and the welding with it of the bottom of drip pan (25), the vapor pipe (27) of buffering water distributing area (28) passes body (33) and annular collecting vat (24), and perforate welding with it; Sludge drainage system (34) is surrounded by bucket (7), reaction chamber (6), body (33), annular porous sludge pipe (35) and base plate (2) welding, spoil disposal is responsible for (36) and is passed body (33) and welding with it, manually-operated gate A (37) and electrically operated valve (38) are equipped with in its outer end, clarification and effluent pipe (5) passes body (33) and welding with it on the bucket top, manually-operated gate B (4) is installed in the lower end.
2. a kind of novel high turbidity according to claim 1 and biochemical integral water purifier, it is characterized in that: reaction chamber (6) is positioned at the central authorities of equipment bottom, be vertically welded on the base plate (2), water inlet pipe (3) passes body (33), enter the bottom of reaction chamber (6), central mud feeding drum (9) is by dredging tube (8) and reaction chamber (6) welding.
3. a kind of novel high turbidity according to claim 1 and biochemical integral water purifier, it is characterized in that: tube settling chamber (29) are at the equipment middle part, inclined tube carriage (10) and body (33) welding are arranged below, assist on it and establish PVC honeycomb inclined-tube (11), the space under it is suspension clarifying chamber (32).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010205788530U CN201883001U (en) | 2010-10-27 | 2010-10-27 | Novel high-turbidity and biochemistry integrated water purifier |
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CN2010205788530U CN201883001U (en) | 2010-10-27 | 2010-10-27 | Novel high-turbidity and biochemistry integrated water purifier |
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CN201883001U true CN201883001U (en) | 2011-06-29 |
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CN2010205788530U Expired - Fee Related CN201883001U (en) | 2010-10-27 | 2010-10-27 | Novel high-turbidity and biochemistry integrated water purifier |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102050552A (en) * | 2010-10-27 | 2011-05-11 | 贵州绿色环保设备工程有限责任公司 | Novel high-turbidity and biochemical integrated water purifier |
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2010
- 2010-10-27 CN CN2010205788530U patent/CN201883001U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102050552A (en) * | 2010-10-27 | 2011-05-11 | 贵州绿色环保设备工程有限责任公司 | Novel high-turbidity and biochemical integrated water purifier |
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110629 Termination date: 20131027 |