CN105502729A - Water treatment equipment - Google Patents
Water treatment equipment Download PDFInfo
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- CN105502729A CN105502729A CN201510851609.4A CN201510851609A CN105502729A CN 105502729 A CN105502729 A CN 105502729A CN 201510851609 A CN201510851609 A CN 201510851609A CN 105502729 A CN105502729 A CN 105502729A
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- mud discharging
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 136
- 238000001914 filtration Methods 0.000 claims abstract description 40
- 238000001179 sorption measurement Methods 0.000 claims abstract description 39
- 239000000463 material Substances 0.000 claims abstract description 11
- 239000010802 sludge Substances 0.000 claims abstract description 6
- 238000007599 discharging Methods 0.000 claims description 36
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 20
- 239000000706 filtrate Substances 0.000 claims description 10
- 230000015271 coagulation Effects 0.000 claims description 9
- 238000005345 coagulation Methods 0.000 claims description 9
- 239000011572 manganese Substances 0.000 claims description 7
- 229910052748 manganese Inorganic materials 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 229920000742 Cotton Polymers 0.000 claims description 6
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 239000004576 sand Substances 0.000 claims description 6
- 239000000741 silica gel Substances 0.000 claims description 6
- 229910002027 silica gel Inorganic materials 0.000 claims description 6
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 4
- 150000002696 manganese Chemical class 0.000 claims description 4
- 239000004793 Polystyrene Substances 0.000 claims description 3
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims description 3
- 239000003830 anthracite Substances 0.000 claims description 3
- 239000003245 coal Substances 0.000 claims description 3
- 238000001514 detection method Methods 0.000 claims description 3
- 239000008187 granular material Substances 0.000 claims description 3
- 229920002223 polystyrene Polymers 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 238000010926 purge Methods 0.000 claims description 3
- 238000004062 sedimentation Methods 0.000 abstract description 16
- 239000002384 drinking water standard Substances 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 description 12
- 239000012535 impurity Substances 0.000 description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 238000010276 construction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 231100001261 hazardous Toxicity 0.000 description 2
- 231100001240 inorganic pollutant Toxicity 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 230000001473 noxious effect Effects 0.000 description 2
- 239000002957 persistent organic pollutant Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 230000008570 general process Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 230000003245 working effect Effects 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
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5209—Regulation methods for flocculation or precipitation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The invention discloses water treatment equipment, which comprises a raw water tank, a primary sedimentation tower, an inclined tubing sedimentation room, a filtration room and an adsorption room. A water taking and filtering device is arranged inside the raw water tank. The device comprises a water taking tank and a fixed support. The bottom of the water taking tank is open and provided with grating, and the inside of the water taking tank is provided with a material filter layer. A water inlet pipeline is provided with an on-line flow detector, a coagulation-dosing device and a high pressure pump. The primary sedimentation tower comprises inner and outer towers and a sludge discharge channel arranged between the outer tower and the inner tower. Baffle plates which are tilted upwards are arranged in a relatively-crossed manner inside the inner tower. A sludge collecting device and an inclined tubing sedimentation device are disposed inside the inclined tubing sedimentation room. The middle part of the filtration room is provided with a filter layer. Multiple adsorption layers are arranged inside the adsorption room. Raw water at a water taking end can be preliminarily filtered, and turbidity of raw water is further reduced by the utilization of the primary sedimentation tower. Then, the raw water further flows through treatment rooms such as the inclined tubing sedimentation room, the filtration room and the like to reach the drinking water standard. The whole system has a compact layout and occupies a small area.
Description
Technical field
The present invention relates to water-suppling treatment equipment field, be specifically related to a kind of water treating equipment.
Background technology
The activity of the mankind can make a large amount of industry, agricultural and domestic refuse enter in water, water body is polluted, the current whole world about has the sewage of billion cubic meter more than 4200 to enter rivers,lakes and seas every year, pollute the fresh water of 5.5 tcms, this is equivalent to more than 14% of global runoff volume, increasingly the water pollutions aggravated, significant threat is formed to the living safety of the mankind, become human health, the major obstacles of economy and social sustainable development, investigate according to authoritative institution of the world, in developing country, various diseases has 80% to propagate because having drunk antihygienic water, at least cause global 200d 00,000 people dead because drinking unhygienic water every year, therefore water pollutions is referred to as " world's number one killer ", at present, in river and the dirty water decontamination handles, various informative water treating equipment just play an important role, but general water purifying plant requires that influent turbidity is not high, the water higher for some turbidity often is still difficult to reach drinking water standard after general process, in addition due to the complicacy of water technology, it is various to there is modular construction in traditional water supply water purification integration apparatus, the defect that land occupation resource is large.
Summary of the invention
For solving above technical problem, the invention provides a kind of a kind of water treating equipment being applicable to the higher former water of turbidity.
Technical scheme is as follows:
A kind of water treating equipment, comprise connect successively former pond, primary settling tower, tube settling room, filtration chamber, adsorption chamber and clean water basin, its key is:
Water intaking filtration unit is provided with in described former pond, described water intaking filtration unit comprises fetching tank for water and fixed support, described fetching tank for water is fixed on described fixed support, described fetching tank for water bottom surface opening is also provided with grid, be provided with filter material layer in described fetching tank for water, described fetching tank for water top is connected with described primary settling tower bottom by inlet channel;
Described inlet channel is provided with coagulation dosing device, and this coagulation dosing device is connected with online flow detection meter on the inlet channel of the side in described former pond, and the inlet channel of this coagulation dosing device near described primary settling tower side is provided with high-pressure pump;
Described primary settling tower comprises Wai Ta and Nei Ta, therebetween mud discharging passage is formed, the bottom of described interior tower is connected with inlet channel, intersect from top to bottom at described Nei Tanei and be provided with at least two traverse baffles, this traverse baffle is inclined upwardly 5-10 °, described traverse baffle lower side is fixedly connected with the tower wall of described interior tower, described traverse baffle upper side edge is respectively equipped with baffle plate, each described traverse baffle and described Nei Ta junction are respectively equipped with mud discharging mouth, and the lower rim of this mud discharging mouth is concordant with this traverse baffle lower side;
Described tube settling indoor are provided with inclined-pipe settler, and the described tube settling room below this inclined-pipe settler is connected by pipeline and described interior top of tower;
Described filter chamber top is provided with water distributor, and described water distributor feed-water end and top, described tube settling room are connected, and be provided with water outlet, be provided with filtering layer in the middle part of described filtration chamber bottom described filtration chamber;
Adsorption layer and vertical water distributor is provided with in described adsorption chamber, the two ends of this vertical water distributor pass described adsorption layer respectively, the upper end of this vertical water distributor is connected with water distributor, the lower end of this vertical water distributor is stretched out described adsorption chamber and is connected with the water outlet of described filtration chamber, adsorption chamber below described adsorption layer is connected with described clean water basin by outlet conduit, described adsorption layer comprises the diatomite layer set gradually from the bottom up, fluffy cotton layer, layer of silica gel and active carbon layer, described diatomite layer, fluffy cotton layer, the Thickness Ratio of layer of silica gel and active carbon layer is 3:2:1.5:1.
The beneficial effect adopting the technical program is because the water intaking end at water source is provided with water intaking filtration unit, effectively can remove the floating matter in water, and the organic pollutant to other, the impurity such as inorganic pollutant have preliminary filtration result, simultaneously at feed-water end by online flow monitoring meter Real Time Observation flooding velocity, and regulate the coagulated agent amount added in former water according to this, with the addition of the traverse baffle of the former water after coagulated agent through primary settling tower, the larger alumen ustum of condensation can enter Wai Tazhong by preliminary sedimentation on traverse baffle, now the turbidity of former water reduces greatly, the impurity of former water after the secondary sedimentation of tube settling room in water is removed substantially, former water again after filter chamber filters can reach drinking water standard substantially, the peculiar smell that now former water is residual in water after adsorption chamber adsorption filtration again and hazardous and noxious substances will be removed further.
As preferably: above-mentioned water distributor comprises star-like arm, described star-like arm is Samsung arm, angle between adjacent arm is 120 °, this star-like arm external part is connected with same outer endless tube, interior endless tube is provided with in this outer endless tube, described outer endless tube and interior endless tube are connected with described star-like arm respectively, and described interior endless tube, outer endless tube and star-like arm are respectively equipped with water distributing pore.Adopt and the invention has the beneficial effects as follows that water source can be distributed to the top of adsorption layer by disc type narrow meshed water distributor uniformly, and larger turbulent water can not be produced.
Back-purge system is provided with below above-mentioned adsorption layer.The beneficial effect of this scheme is adopted to be the work-ing life that effectively can extend adsorption layer.
Above-mentioned traverse baffle is 20-30, is evenly distributed at the bottom of the tower of described interior tower and between tower top.Adopt the beneficial effect of this scheme to be that traverse baffle density is arranged rationally, shorten the distance of alumen ustum sedimentation, be conducive to the sedimentation accelerating alumen ustum.
Be provided with the first mud discharging pipe at the bottom of the tower of above-mentioned outer tower, described first mud discharging pipe is provided with the first mud discharging variable valve.The beneficial effect of this scheme is adopted to be that the mud be deposited at the bottom of outer tower tower is regularly discharged by mud discharging pipe.
Be provided with mud collection bucket bottom above-mentioned tube settling room, the bottom of this mud collection bucket is provided with the second mud discharging pipe, and described second mud discharging pipe is provided with the second mud discharging variable valve.Adopt the beneficial effect of this scheme to be can periodically blowdown, avoid mud overheap to affect tube settling effect.
Above-mentioned first mud discharging variable valve and the second described mud discharging variable valve opening time are spaced apart 20-24 hour.Adopt the beneficial effect of this scheme to be regularly got rid of by the mud of deposition, avoid mud overheap, affect sedimentation effect.
Be provided with sludge sump below above-mentioned primary settling tower and described tube settling room, the top of above-mentioned primary settling tower, tube settling room, filtration chamber and described adsorption chamber is equipped with viewing window, and top, described tube settling room is provided with automatic exhaust steam valve.Adopt the beneficial effect of this scheme to be that the mud of deposition can be concentrated and is emitted in sludge sump, facilitate workman to concentrate cleaning, workman fast checks water purifying plant inner case by viewing window.
Above-mentioned filtering layer comprises manganese layer of sand and is laid on the anthracite coal measure on this manganese layer of sand.The beneficial effect of this scheme is adopted to be the residual impurity, particularly iron can removed further in water, manganese class impurity.
Filtrate in above-mentioned filter material layer is granules of polystyrene, is provided with filtrate catch net above described filter material layer.Adopt the beneficial effect of this scheme to be the weight that filtrate proportion gentlier effectively can alleviate whole intake equipment, facilitate M R, the filtrate catch net above filtrate can effectively stop filtrate to float, and guarantees that filter material layer position is fixed and has certain density.
Beneficial effect:
Adopting the invention has the beneficial effects as follows because the water intaking end at water source is provided with water intaking filtration unit, effectively can remove the floating matter in water, and the organic pollutant to other, the impurity such as inorganic pollutant have preliminary filtration result, simultaneously at feed-water end by online flow monitoring meter Real Time Observation flooding velocity, and regulate the coagulated agent amount added in former water according to this, with the addition of the former water after coagulated agent through primary settling tower, the larger alumen ustum of condensation can sedimentation layer by layer on traverse baffle, traverse baffle density arranges rationally, shorten the distance of alumen ustum sedimentation, be conducive to the sedimentation accelerating alumen ustum, reduce the turbidity of former water, former water filters through filter chamber after the secondary sedimentation of tube settling room again can reach drinking water standard substantially, the peculiar smell that now former water is residual in water after adsorption chamber adsorption filtration again and hazardous and noxious substances will be removed further, this device is to the iron in water in addition, the impurity such as manganese have good filtration result, whole system reasonable in design, compact in design, greatly save the floor space of structures, be not only applicable to the construction of water supply plant on a small scale, the construction of larger water supply plant can also be used for by the mode of multiple stage parallel connection.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Fig. 2 is the enlarged view a of Fig. 1;
Fig. 3 is water distributor structure schematic diagram;
Fig. 4 is water intaking filter apparatus configuration schematic diagram.
Embodiment
Below in conjunction with embodiment and accompanying drawing, the invention will be further described.
As Figure 1-4, a kind of water treating equipment, comprise connect successively former pond 5, primary settling tower 1, tube settling room 2, filtration chamber 3, adsorption chamber 4 and clean water basin 20.
Water intaking filtration unit 25 is provided with in described former pond 5, described water intaking filtration unit 25 comprises fetching tank for water 251 and fixed support 254, described fetching tank for water 251 is fixed on described fixed support 254, described fetching tank for water 251 bottom surface opening is also provided with grid 252, filter material layer 253 is provided with in described fetching tank for water 251, described fetching tank for water 251 top is connected with described primary settling tower 1 bottom by inlet channel 6, filtrate in described filter material layer 253 is granules of polystyrene, is provided with filtrate catch net 255 above described filter material layer 253.
Described inlet channel 6 is provided with coagulation dosing device 9, this coagulation dosing device 9 is connected with online flow detection meter 7 on the inlet channel 6 of the side in described former pond 5, and the inlet channel 6 of this coagulation dosing device 9 near described primary settling tower 1 side is provided with high-pressure pump 8.
Described primary settling tower 1 comprises outer tower 104 and Nei Ta 103, therebetween mud discharging path 10 6 is formed, the bottom of described interior tower 103 is connected with inlet channel 6, intersect from top to bottom in described interior tower 103 and be provided with at least two traverse baffles 102, described traverse baffle 102 is 20-30, be evenly distributed at the bottom of the tower of described interior tower 103 and between tower top, this traverse baffle 102 is inclined upwardly 5-10 °, described traverse baffle 102 lower side is fixedly connected with the tower wall of described interior tower 103, described traverse baffle 102 upper side edge is respectively equipped with baffle plate 101, each described traverse baffle 102 is respectively equipped with mud discharging mouth 105 with described interior tower 103 junction, the lower rim of this mud discharging mouth 105 is concordant with this traverse baffle 102 lower side, the mud be deposited on thus on traverse baffle 102 enters in mud discharging path 10 6 by described mud discharging mouth 105, and be deposited at the bottom of the tower of outer tower 104 gradually, the first mud discharging pipe 10 is provided with at the bottom of the tower of described outer tower 104, described first mud discharging pipe 10 is provided with the first mud discharging variable valve 11.
Inclined-pipe settler 202 is provided with in described tube settling room 2, described tube settling room 2 below this inclined-pipe settler 202 is connected by pipeline 15 and described interior tower 103 top, mud collection bucket 201 is provided with bottom described tube settling room 2, the bottom of this mud collection bucket 201 is provided with the second mud discharging pipe 16, described second mud discharging pipe 16 is provided with the second mud discharging variable valve 17, and described first mud discharging variable valve 11 and the second described mud discharging variable valve 17 opening time are spaced apart 20-24 hour.
Top, described filtration chamber 3 is provided with water distributor 18, described water distributor 18 feed-water end and top, described tube settling room 2 are connected by pipeline, water outlet is provided with bottom described filtration chamber 3, be provided with filtering layer in the middle part of described filtration chamber 3, described filtering layer comprises manganese layer of sand and is laid on the anthracite coal measure on this manganese layer of sand.
Adsorption layer 4 and vertical water distributor 21 is provided with in described adsorption chamber 19, the two ends of this vertical water distributor 21 pass described adsorption layer 4 respectively, the upper end of this vertical water distributor 21 is connected with water distributor 22, the lower end of this vertical water distributor 21 is stretched out described adsorption chamber 19 and is connected with the water outlet of described filtration chamber 3, adsorption chamber 19 below described adsorption layer 4 is connected with described clean water basin 20 by outlet conduit 24, described adsorption layer 4 comprises the diatomite layer 401 set gradually from the bottom up, fluffy cotton layer 402, layer of silica gel 403 and active carbon layer 404, described diatomite layer 401, fluffy cotton layer 402, the Thickness Ratio of layer of silica gel 403 and active carbon layer 404 is 3:2:1.5:1, back-purge system 23 is provided with below described adsorption layer 4.
Described water distributor 22 comprises star-like arm 224, described star-like arm 224 is Samsung arm, angle between adjacent arm is 120 °, this star-like arm 224 external part is connected with same outer endless tube 222, interior endless tube 223 is provided with in this outer endless tube 222, described outer endless tube 222 and interior endless tube 223 are connected with described star-like arm 224 respectively, and described interior endless tube 223, outer endless tube 222 and star-like arm 224 are respectively equipped with water distributing pore 221.
It can also be seen that from figure, sludge sump 13 is provided with below described primary settling tower 1 and tube settling room 2, the top of described primary settling tower 1, tube settling room 2, filtration chamber 3 and described adsorption chamber 19 is equipped with viewing window 12, and top, described tube settling room 2 is provided with automatic exhaust steam valve 14.
Claims (10)
1. water treating equipment, comprise connect successively former pond (5), primary settling tower (1), tube settling room (2), filtration chamber (3), adsorption chamber (19) and clean water basin (20), it is characterized in that:
Water intaking filtration unit (25) is provided with in described former pond (5), described water intaking filtration unit (25) comprises fetching tank for water (251) and fixed support (254), described fetching tank for water (251) is fixed on described fixed support (254), described fetching tank for water (251) bottom surface opening is also provided with grid (252), be provided with filter material layer (253) in described fetching tank for water (251), described fetching tank for water (251) top is connected with described primary settling tower (1) bottom by inlet channel (6);
Described inlet channel (6) is provided with coagulation dosing device (9), this coagulation dosing device (9) is connected with online flow detection meter (7) on the inlet channel (6) of the side of described former pond (5), and the inlet channel (6) of this coagulation dosing device (9) near described primary settling tower (1) side is provided with high-pressure pump (8);
Described primary settling tower (1) comprises outer tower (104) and interior tower (103), therebetween mud discharging passage (106) is formed, the bottom of described interior tower (103) is connected with inlet channel (6), intersect from top to bottom in described interior tower (103) and be provided with at least two traverse baffles (102), this traverse baffle (102) is inclined upwardly 5-10 °, described traverse baffle (102) lower side is fixedly connected with the tower wall of described interior tower (103), described traverse baffle (102) upper side edge is respectively equipped with baffle plate (101), each described traverse baffle (102) and described interior tower (103) junction are respectively equipped with mud discharging mouth (105), the lower rim of this mud discharging mouth (105) is concordant with this traverse baffle (102) lower side,
Be provided with inclined-pipe settler (202) in described tube settling room (2), the described tube settling room (2) of this inclined-pipe settler (202) below is connected by pipeline (15) and described interior tower (103) top;
Described filtration chamber (3) top is provided with water distributor (18), described water distributor (18) feed-water end and described tube settling room (2) top are connected, bottom, described filtration chamber (3) is provided with water outlet, and described filtration chamber (3) middle part is provided with filtering layer;
Adsorption layer (4) and vertical water distributor (21) is provided with in described adsorption chamber (19), the two ends of this vertical water distributor (21) pass described adsorption layer (4) respectively, the upper end of this vertical water distributor (21) is connected with water distributor (22), the lower end of this vertical water distributor (21) is stretched out described adsorption chamber (19) and is connected with the water outlet of described filtration chamber (3), the adsorption chamber (19) of described adsorption layer (4) below is connected with described clean water basin (20) by outlet conduit (24), described adsorption layer (4) comprises the diatomite layer (401) set gradually from the bottom up, fluffy cotton layer (402), layer of silica gel (403) and active carbon layer (404), described diatomite layer (401), fluffy cotton layer (402), the Thickness Ratio of layer of silica gel (403) and active carbon layer (404) is 3:2:1.5:1.
2. a kind of water treating equipment according to claim 1, it is characterized in that: described water distributor (22) comprises star-like arm (224), described star-like arm (224) is Samsung arm, angle between adjacent arm is 120 °, this star-like arm (224) external part is connected with same outer endless tube (222), interior endless tube (223) is provided with in this outer endless tube (222), described outer endless tube (222) and interior endless tube (223) are connected with described star-like arm (224) respectively, described interior endless tube (223), outer endless tube (222) and star-like arm (224) are respectively equipped with water distributing pore (221).
3. a kind of water treating equipment according to claim 1 and 2, is characterized in that: described adsorption layer (4) below is provided with back-purge system (23).
4. a kind of water treating equipment according to claim 1, is characterized in that: described traverse baffle (102) is 20-30, is evenly distributed at the bottom of the tower of described interior tower (103) and between tower top.
5. a kind of water treating equipment according to claim 1 or 4, it is characterized in that: be provided with the first mud discharging pipe (10) at the bottom of the tower of described outer tower (104), described first mud discharging pipe (10) is provided with the first mud discharging variable valve (11).
6. a kind of water treating equipment according to claim 5, it is characterized in that: described tube settling room (2) bottom is provided with mud collection bucket (201), the bottom of this mud collection bucket (201) is provided with the second mud discharging pipe (16), and described second mud discharging pipe (16) is provided with the second mud discharging variable valve (17).
7. a kind of water treating equipment according to claim 6, is characterized in that: described first mud discharging variable valve (11) and the second described mud discharging variable valve (17) opening time are spaced apart 20-24 hour.
8. a kind of water treating equipment according to claim 1,4 or 6, it is characterized in that: described primary settling tower (1) and tube settling room (2) below are provided with sludge sump (13), the top of described primary settling tower (1), tube settling room (2), filtration chamber (3) and described adsorption chamber (19) is equipped with viewing window (12), and described tube settling room (2) top is provided with automatic exhaust steam valve (14).
9. a kind of water treating equipment according to claim 8, is characterized in that: described filtering layer comprises manganese layer of sand and is laid on the anthracite coal measure on this manganese layer of sand.
10. a kind of water treating equipment according to claim 1 or 8, is characterized in that: the filtrate in described filter material layer (253) is granules of polystyrene, and described filter material layer (253) top is provided with filtrate catch net (255).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510851609.4A CN105502729B (en) | 2015-11-28 | 2015-11-28 | A kind of water treatment facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510851609.4A CN105502729B (en) | 2015-11-28 | 2015-11-28 | A kind of water treatment facilities |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105502729A true CN105502729A (en) | 2016-04-20 |
| CN105502729B CN105502729B (en) | 2018-02-16 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510851609.4A Expired - Fee Related CN105502729B (en) | 2015-11-28 | 2015-11-28 | A kind of water treatment facilities |
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| CN (1) | CN105502729B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105347565A (en) * | 2015-11-30 | 2016-02-24 | 綦江县狮子桥供水有限公司 | Integrated water purifying device of tap water plant |
| CN105347564A (en) * | 2015-11-30 | 2016-02-24 | 綦江县狮子桥供水有限公司 | Tap water plant integrated water purification equipment with water getting and filtering device |
| CN105461091A (en) * | 2015-11-30 | 2016-04-06 | 綦江县狮子桥供水有限公司 | Water treating equipment for waterworks |
| CN105502713A (en) * | 2015-11-30 | 2016-04-20 | 綦江县狮子桥供水有限公司 | Waterwork water purification treatment equipment |
| CN105502714A (en) * | 2015-11-30 | 2016-04-20 | 綦江县狮子桥供水有限公司 | Waterwork water purification treatment equipment with water taking and filtering device |
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| CN201240953Y (en) * | 2008-07-08 | 2009-05-20 | 甘臻 | Integral water purifying apparatus |
| CN201770557U (en) * | 2010-09-01 | 2011-03-23 | 浙江沃特水处理设备有限公司 | Integrated water purifying device |
| US20140021148A1 (en) * | 2012-07-21 | 2014-01-23 | Don M. Buckner | Method and system to separate solids from liquids |
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| US20090095690A1 (en) * | 2007-10-14 | 2009-04-16 | Mccabe Derald L | Solids removal system and method |
| CN201240953Y (en) * | 2008-07-08 | 2009-05-20 | 甘臻 | Integral water purifying apparatus |
| CN201770557U (en) * | 2010-09-01 | 2011-03-23 | 浙江沃特水处理设备有限公司 | Integrated water purifying device |
| US20140021148A1 (en) * | 2012-07-21 | 2014-01-23 | Don M. Buckner | Method and system to separate solids from liquids |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105347565A (en) * | 2015-11-30 | 2016-02-24 | 綦江县狮子桥供水有限公司 | Integrated water purifying device of tap water plant |
| CN105347564A (en) * | 2015-11-30 | 2016-02-24 | 綦江县狮子桥供水有限公司 | Tap water plant integrated water purification equipment with water getting and filtering device |
| CN105461091A (en) * | 2015-11-30 | 2016-04-06 | 綦江县狮子桥供水有限公司 | Water treating equipment for waterworks |
| CN105502713A (en) * | 2015-11-30 | 2016-04-20 | 綦江县狮子桥供水有限公司 | Waterwork water purification treatment equipment |
| CN105502714A (en) * | 2015-11-30 | 2016-04-20 | 綦江县狮子桥供水有限公司 | Waterwork water purification treatment equipment with water taking and filtering device |
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| Publication number | Publication date |
|---|---|
| CN105502729B (en) | 2018-02-16 |
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