CN105481138A - Method and structure for removing turbidite in surface water and reducing temporary hardness in synergetic mode - Google Patents
Method and structure for removing turbidite in surface water and reducing temporary hardness in synergetic mode Download PDFInfo
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- CN105481138A CN105481138A CN201510941179.5A CN201510941179A CN105481138A CN 105481138 A CN105481138 A CN 105481138A CN 201510941179 A CN201510941179 A CN 201510941179A CN 105481138 A CN105481138 A CN 105481138A
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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
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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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/20—Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
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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
- 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
- C02F1/5281—Installations for water purification using chemical agents
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
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Abstract
The invention discloses a method and structure for removing turbidite in surface water and reducing temporary hardness in a synergetic mode. The structure solves the problems that sediment, scale and the like are generated after surface water in karst regions is boiled, and meanwhile the turbidite removal function is achieved. A grid flocculation basin and an inclined pipe sedimentation pool are arranged on the front section of the structure. Water discharged out of the inclined pipe sedimentation pool directly enters the acid (HCl) addition reaction section, dissolved CO2 is generated after hydrochloric acid reacts with HCO3- and CO32- in water, water containing dissolved CO2 enters an aeration tank, and aeration heads generate a large number of tiny bubbles which can be combined with CO2 dissolved in water and float out of the water surface so that CO2 can escape into air; meanwhile, tiny turbidite which does not precipitate in the inclined pipe sedimentation pool adheres to the tiny bubbles, and therefore turbidite rises to the water surface to be collected to a residue collection groove through a residue scraper and is then discharged. By means of the structure, a structure cell body is reduced by controlling the reaction precipitation time, lands are saved, and capital construction expenses are reduced; the principle is simple, operation is convenient, and a very high water scale removal rate is achieved for surface water with high temporary hardness.
Description
Technical field
The present invention relates to the structures of turbidity and temporary hardness in a kind of collaborative removal surface water.
Technical background
China is vast in territory, and landforms are varied, and the water quality flowing through different landforms place surface water is different.Karst landform refers to solublerock (carbonatite, sulfuric acid rock salt, halogen rock etc.) based on chemical corrosion, and flowing water erosion, gravity to be collapsed etc. and act as the special geomorphology that auxiliary geologic function formed.The distribution of Karst In China landforms is wide, area is large, and account for about 13% of total area, wherein maximum with Guangxi, Guizhou and Eastern Yunnan area occupied, the soil of Guizhou Province more than 70% is karst landform.
A large amount of undissolved suspended matter, colloidalmaterial and microorganism is equally there is in karst region surface water with other regional surface water of China.Simultaneously, it is higher for flowing through earth's surface, karst region water hardness, its hardness formation mechenism is that the carbonatite of indissoluble is under water and carbonic acid gas effect, the bicarbonate ion and the free metal ion (mainly calcium ion and magnesium ion) that generate solubility move in water by rock, current itself have and wash away corrosion, they often becoming the rock of block to be processed into particulate, accelerating the corrosion of rock, thus adding water hardness.Because carbonatite and river exist in a large number in karst region, the corrosion phenomenon of rock is extensively occurred, this is also the major cause that river, karst region hardness content is high.Incrustation scale is formed by temporary hardness in the process of boiling water, i.e. carbonate hardness, it is a part for total hardness, be equivalent to hydrocarbonate and a small amount of carbonate are combined in water calcium, hardness that magnesium is formed, when water boil, the hydrocarbonate of calcium, magnesium decomposes generation precipitation thus reduces water hardness, can remove part hardness by the method for boiling.If calcium and magnesium mainly exist with forms such as vitriol, nitrate and muriates in hard water, be permanent hardness.
Incrustation scale causes the aesthetic difference of drinking water more, to resident living with healthyly there is potential impact.Although the total hardness of regulation water more than 450mg/L, must not limit regulation to temporary hardness in China's " drinking water sanitary standard ".A large amount of HCO existed in the surface water of karst region
3 -and CO
3 2-, there is a large amount of precipitation and floating matter after boiled, cause turbidity to raise in ion, part water turbidity is more than 5NTU, and this and Drinking Water in China are about turbidity and must not have visible regulation contradiction in water.China's " drinking water sanitary standard " is formulating with reference to WHO and western developed country relevant criterion, it formulates foundation is drink unboiled water, and often drink to boil water with China resident and differ greatly, the former mainly drinks calcium, the magnesium ion of dissolving, what China resident drank is that part ion is converted into calcium carbonate, and long-term drinking high carbon acid calcium water affects not clear on normal people.The people often not quoting hard water once long-term drinking hard water, then there will be malaise symptoms, causes diarrhoea and functions of intestines and stomach disorder, i.e. so-called " not acclimatized "; With hard water laundry, soap foams few, causes waste; With the hard water cooking flesh of fish, vegetables, the nutritive value of food can be reduced because not easily boiling; With hard water hair washing, can make that hair coheres, embrittlement etc.
The technology of current process high hardness water mainly contains Medicine soften, ion exchange method and film tenderizer.Medicine soften is applicable to the little situation of water consumption, when water consumption is large run high expensive, due to add chemical substance make water application be greatly limited.Ion exchange softening method complex process equipment, need a large amount of acid of consumption or salt to cook regenerator, cost is relatively high.The consumption of film tenderizer operational process medium power is comparatively large, and water producing cost is higher.Ion exchange method and film tenderizer all need comparatively loaded down with trivial details preprocessing process, and to alleviate the pollution that in main process, resin or mould material are subject to, ion-exchange makes the increase such as sodium ion in water.
Existing softening technology processing cost is high, is badly in need of a kind of economic removal karst region surface water incrustation scale technique.The earth surface water source total hardness satisfied " drinking water sanitary standard " that China is common, but the dissatisfied complaint of the masses that incrustation scale causes is common, and existing treatment technology, need build complicated and huge treatment system in water factory, processing cost is high.And show that solubilize calcium magnesium ion does not make significant difference to human body from existing achievement in research, seek the technology processing karst region surface water incrustation scale economically, calcium carbonate potential problems are drunk for raising this area's drinking water sense organ and elimination extremely important, up to the present domestic and international about tap water hardness treatment research, mainly concentrating on total hardness reduces in technique, and to incrustation scale and temporary hardness research rare, without maturation process and equipment.Therefore the present invention puts forth effort on and seeks a kind of simple, and the quite cheap treatment process of cost removes temporary hardness, can work in coordination with simultaneously and remove turbidity in water.
Summary of the invention
Large for current tap water temporary hardness, the problem of easy fouling, the object of the invention is to, and designs a set of temporary hardness device can removing water, HCO from removal water
3 -and CO
3 2-angle set out, reduce the temporary hardness in water, reduce the generation of incrustation scale.Meanwhile, the present invention can work in coordination with the turbidity removed in water.
In order to realize above-mentioned task, the present invention takes following technical solution:
A method for turbidity and temporary hardness in collaborative removal surface water, removes the part turbidity in pending surface water successively by pending surface water after flocculation and precipitation, afterwards the surface water removing part turbidity is mixed with acid the HCO made in surface water
3 -cO is produced with acid-respons
2gas, finally again will containing CO
2the surface water aeration stripping of gas removes the CO in surface water
2gas and not removed turbidity.
Concrete, the gas-water ratio of described aeration stripping is 6:1, and the aeration stripping time is 10 ~ 20min.
Realize the structures of the method for turbidity and temporary hardness in described collaborative removal surface water, comprise be communicated with successively flocculation reaction district, settling region, acid adding reaction zone and aeration stripping district;
Part turbidity in pending surface water is removed by pending surface water successively behind flocculation reaction district and settling region, afterwards the surface water removing part turbidity is mixed the HCO made in surface water in acid adding reaction zone with acid
3 -cO is produced with acid-respons
2gas, finally again will containing CO
2the CO in surface water removed by the surface water of gas at aeration stripping district aeration stripping
2gas and not removed turbidity.
Concrete, described flocculation reaction district comprises the multiple flocculation basins arranged in a grid formation, the bottom of flocculation basin is communicated with shore pipe, adjacent flocculation basin is communicated with the first water outlet and the rational height of the first water outlet on adjacent flocculation basin is different, cross-sectional area along water (flow) direction flocculation basin increases successively, arranges the first perforation tracery wall and be communicated with flocculation zone and settling region bottom the flocculation basin adjacent with settling region.
More specifically, described settling region comprises settling tank, and set gradually finger-type groove and inclined tube from top to bottom in settling tank, water flows from bottom to top along inclined tube, realizes mud-water separation, the clear water act as after collection and treatment of finger-type groove; Be communicated with shore pipe bottom settling tank, settling tank top is communicated with acid adding reaction zone.
Preferably, described inclined tube length is 1m, and the pitch angle of inclined tube is 60 °.
Concrete, described acid adding reaction zone comprises acid adding reaction tank, the underwater of acid adding reaction tank arranges and adds acid tube, be arranged alternately multiple dividing plate adding level on the pond body inwall below acid tube, pond body wall below dividing plate is arranged the second perforation tracery wall, the second perforation tracery wall is communicated with acid adding reaction tank and aeration stripping district.
Preferably, the spacing of described adjacent separator is 0.5m.
Concrete, described aeration stripping district comprises aeration stripping pond, arranges dreg collecting slot in aeration stripping pond near the Chi Ding of acid adding reaction zone, arranges aerating apparatus at the bottom of the pond in aeration stripping pond, and the current after aeration are flowed out by the direction away from dreg collecting slot.
More specifically, described aerating apparatus comprises aeration supervisor, to arrange multiple aeration branch pipe perpendicular to the direction of supervisor, aeration branch pipe is arranged multiple aeration plate.
Advantage of the present invention is:
(1) fully for the water HCO that temporary hardness is high
3 -and CO
3 2-the characteristic of content, principle is simple
The structures of turbidity and temporary hardness in a kind of collaborative removal surface water of the present invention, HCO in water
3 -with the H in medicament (hydrochloric acid)
+there is following reaction: HCO
3 -+ H
+=H
2o+CO
2↑, produce a large amount of CO dissolved in water
2, on the water in flow process, solarization air cap is to the CO in water
2carry out aeration stripping thus make CO
2be diffused in air, the Cl simultaneously added
-ion is harmful to human health.
(2) structures of turbidity and temporary hardness in a kind of collaborative removal surface water of the present invention, wherein the hydraulic detention time of tube settler applied than current water factory of the hydraulic detention time of tube settler is short, so just the place's of making load is born together with aeration stripping pond by tube settler, tube settler mainly removes macrobead turbidity, and fine particle turbidity is mainly removed in aeration stripping pond.
(3), in acid adding reaction tank, add acid tube and be arranged on below water surface 0.5m and add acid tube, add acid tube perforate direction for obliquely 45 ° be symmetric, hydrochloric acid can be avoided like this to volatilize contaminate environment.Acid adding reaction tank is provided with dividing plate, and the water after acid adding back and forth flows and hydrochloric acid is fully mixed with water between dividing plate, makes reaction HCO
3 -+ H
+=H
2o+CO
2↑ more abundant.
(4) the primary effect of aeration tank is a large amount of carbonic acid gas produced after removal adds acid-respons, in addition the micro-bubble that solarization air cap produces can also stick density in the water turbidity little compared with water, turbidity is attached on bubble rises to the water surface to scrape to dreg collecting slot by slag scraper, improves effluent quality.
(5) structures floor space of the present invention is little, convenient management, and capital cost is little; The hydrochloric acid adopted belongs to common medicament, easily buys, easily configures, adding less, working cost is low.
Accompanying drawing explanation
Fig. 1 is the longitudinal sectional view of structures of the present invention, and in figure, arrow is water (flow) direction;
Fig. 2 is the upper strata vertical view of structures of the present invention and the composition graphs of lower floor's vertical view, and in figure, arrow is water (flow) direction, and in figure, A is upper strata vertical view, and in figure, B is lower floor's vertical view;
Fig. 3 is the sectional view of the acid adding reaction tank of structures of the present invention;
Label in figure represents respectively: 1-flocculation reaction district, 11-flocculation basin, 12-shore pipe, 13-first water outlet, 14-first bores a hole tracery wall, 15-collection mud hole, 2-settling region, 21-finger-type groove, 22-effluent weir, 23-inclined tube, 24-inclined-tube support, 25-second water outlet, 3-acid adding reaction zone, 31-adds acid tube, 32-dividing plate, 33-second bores a hole tracery wall, 4-aeration stripping district, 41-dreg collecting slot, 42-slag scraper, 43-aeration is responsible for, 44-the 3rd water outlet, 45-aeration branch pipe, 46-aeration plate, 5-water inlet pipe, 6-water leg, 7-rising pipe, 8-inspection-pit,
Below in conjunction with specification drawings and specific embodiments, the present invention is illustrated.
Embodiment
Turbidity in surface water of the present invention refers to suspended substance in surface water and colloid.
The flocculation agent that the present invention uses can be that such as flocculation agent can be polymerize aluminum chloride (PAC), and coagulant aids can be polyacrylamide (PAM) for the flocculation agent that water treatment uses in prior art.
The gas-water ratio of aeration stripping of the present invention refers to the gas volume of aeration and the long-pending ratio of staying water.
The method of turbidity and temporary hardness in a kind of collaborative removal surface water of the present invention, part turbidity in pending surface water is removed by pending surface water successively after flocculation and precipitation, afterwards the surface water removing part turbidity is mixed with acid the HCO made in surface water
3 -cO is produced with acid-respons
2gas, finally again will containing CO
2the surface water aeration stripping of gas removes the CO in surface water
2gas and not removed turbidity.
Composition graphs 1-3, realize collaborative remove turbidity and the structures of the method for temporary hardness in surface water comprise be communicated with successively flocculation reaction district 1, settling region 2, acid adding reaction zone 3, aeration stripping district 4, water inlet pipe 5, water leg 6, rising pipe 7 and inspection-pit 8; Part turbidity in pending surface water is removed by water inlet pipe 5 by pending surface water successively behind flocculation reaction district 1 and settling region 2, afterwards the surface water removing part turbidity is mixed with acid the HCO made in surface water in acid adding reaction zone 3
3 -cO is produced with acid-respons
2gas, finally again will containing CO
2the CO in surface water removed by the surface water of gas at aeration stripping district 4 aeration stripping
2gas and not removed turbidity, wherein:
Flocculation reaction district 1 comprises the multiple flocculation basins 11 arranged in a grid formation, the bottom of flocculation basin 11 is communicated with shore pipe 12, adjacent flocculation basin 11 is communicated with the first water outlet 13 and the rational height of the first water outlet 13 on adjacent flocculation basin 11 is different, cross-sectional area along water (flow) direction flocculation basin 11 increases successively, arranges the first perforation tracery wall 14 and be communicated with flocculation reaction district 1 and settling region 2 bottom the flocculation basin 11 adjacent with settling region 2;
Settling region 2 comprises settling tank, sets gradually finger-type groove 21 and inclined tube 23 in settling tank from top to bottom, and water flows from bottom to top along inclined tube 23 and realizes mud-water separation, the clear water act as after collection and treatment of finger-type groove 21; Be communicated with shore pipe 12 bottom settling tank, settling tank top is communicated with acid adding reaction zone 3.
Acid adding reaction zone 3 comprises acid adding reaction tank, the underwater of acid adding reaction tank arranges and adds acid tube 31, in acid adding reaction tank, acid adding pipe is set under water surface 0.5m, add acid tube perforate direction for obliquely 45 ° be symmetric, adding acid tube is provided with check valve, is provided with gate valve before and after check valve, add below acid tube and be provided with dividing plate, bottom pond, be provided with shore pipe.Be arranged alternately multiple dividing plate 32 adding level on the pond body inwall below acid tube 31, the pond body wall below dividing plate 32 arranged the second perforation tracery wall 33, second tracery wall 33 of boring a hole and be communicated with acid adding reaction tank and aeration stripping district 4.
Aeration stripping district 4 comprises aeration stripping pond, arranges dreg collecting slot 41 in aeration stripping pond near the Chi Ding of acid adding reaction zone 3, arranges aerating apparatus at the bottom of the pond in aeration stripping pond, and the current after aeration are flowed out by the direction away from dreg collecting slot 41.
Aerating apparatus comprises aeration supervisor 43, to arrange multiple aeration branch pipe 45 perpendicular to the direction of aeration supervisor 43, aeration branch pipe 45 is arranged multiple aeration plate 46.
A kind of preferred design: flocculation basin 11 has 12, it is rectangular pond body that 12 flocculation basins 11 form a cross section, current flow with broken line form in the body of rectangular pond, and the height of the first water outlet 13 on adjacent flocculation basin 11 is different, the path of maximum increase current, surface water and flocculation agent are fully contacted and to the enough sedimentation time of particulate matter after flocculating, also can add grizzly bar in flocculation basin 11, the descending promotion flco of the velocity slope of pending water is grown up, flocculation time can be determined according to the process amount of water and the add-on etc. of flocculation agent, the flocculation time adopted in the present invention is 10 ~ 20min, be provided with shore pipe bottom flocculation basin the particulate matter after flocculation is got rid of, settling tank liquid level load is 7m
3/ (m
2.h), inclined tube length is 1m, and inclination angle is 60 °, vertical distance in acid adding reaction tank between adjacent separator 32 is 0.5m, and the acid adding reaction times is 1 ~ 35min, in aeration stripping pond, gas-water ratio is 6:1, and the aeration stripping time is 10 ~ 20min.
Water fully flocculates in flocculation basin 11, make the macrobead turbidity of formation free settling, flocculation basin 11 water outlet enters settling tank and completes mud-water separation process by the centrifugation of inclined tube 23, precipitating sludge is discharged outside pond by shore pipe 12 under the effect of hydrostaticpressure, and the surface water removing macrobead turbidity generates CO after entering acid adding reaction zone 3 and mixed in hydrochloric acid
2gas, containing CO
2the water of gas and the tiny turbidity of part enters aeration stripping district 4, is made the CO in water by the aeration effect in aeration stripping district 4
2gas ease, in air, makes the tiny turbidity in water be suspended into the water surface and scrapes to dreg collecting slot 41 by slag scraper 42, is finally collected by water leg 6 and removes CO
2with the water removing turbidity, then carried out subsequent disposal or the transport of water by rising pipe 7.
Concrete, the structures that the method removing turbidity and temporary hardness in surface water is worked in coordination with in realization of the present invention are worked in coordination with the process removing turbidity and temporary hardness in surface water and are comprised:
Pending surface water is first through static mixer, in static mixer, pending surface water has fully mixed agglomeration process with flocculation agent, the water completing agglomeration process enters in flocculation basin 11 by water inlet pipe 5, water goes up current downflow successively in flocculation basin 11, the cross-sectional dimension of flocculation basin 11 increases successively along water (flow) direction, and the speed of current reduces thus realize G value to have reduced flocculation process successively successively.Shore pipe 12, sludge hopper and collection mud hole 15 is provided with bottom flocculation basin, the turbidity that the turbidity that surface water Midst density is larger than water and small portion complete flocculation process can precipitate at flocculation basin 11 in the process of water flow, mud after precipitation enters in sludge hopper, is discharged in the mud-collecting slot of flocculation basin 11 both sides under the effect of hydrostaticpressure by collection mud hole 15 by shore pipe 12.
The water flowed out from flocculation basin 11 enters settling tank through the first perforation tracery wall 14, and the effect of the first perforation tracery wall 14 is that flocculation basin 11 water outlet is assigned in settling tank equably.Inclined tube 23 is fixed by inclined-tube support 24, and inclined tube 23 length is 1m, inclination angle is 60 °, and water flows from bottom to top along inclined tube 23, realizes mud-water separation, and the mud of precipitation enters mud-collecting slot after being collected by shore pipe 12 under the effect of hydrostaticpressure.Clear water enters finger-type groove 21, water after finger-type groove 21 is provided with triangle effluent weir 22 precipitation drops to finger-type groove 21 by leg-of-mutton effluent weir 22, the effect of finger-type groove 21 is the clear water after the precipitation of collecting precipitation pond, and finger-type groove 21 can be fixed on settling tank by joist steel.In the present invention, the sedimentation time of settling tank is shorter than the sedimentation time of general water factory tube settler, when object is shorter precipitation, the time can make the macrobead turbidity in water complete precipitation, tiny turbidity does not precipitate, and so just makes the load of settling tank process water reduce, and reduces pond and holds.
Settling tank clear water falls into acid adding reaction zone 3 by the second water outlet 25, acid adding reaction zone 3 is provided with and adds acid tube 31, add acid tube 31 and be located at below water surface 0.5m, add acid tube 31 perforate direction for obliquely 45 ° be symmetric, the object done like this be add acid tube 31 flow out hydrochloric acid directly to current downflow, owing to adding acid tube at below water surface 0.5m, the hydrochloric acid in water reacts with water and can not escape in air at once in the process upwards flowed, thus avoids the waste of hydrochloric acid.Water after acid adding enters dividing plate reaction zone, and water back and forth flows in dividing plate 32, thus water is fully mixed with hydrochloric acid, completes HCO
3 -+ H
+=H
2o+CO
2↑ reaction, makes CO in water
2amount raise; Tiny flocs unit in settling tank water outlet can precipitate at acid adding reaction tank, and this part precipitation is discharged in mud-collecting slot by shore pipe.Conveniently to the maintenance of the parts such as the valve adding acid tube 31, inspection-pit 8 is set at the valve position adding acid tube;
The water outlet of acid adding reaction zone 3 is assigned to aeration stripping district 4 equably by the second perforation tracery wall 33.Gas blower makes the air of compression enter aeration supervisor 43, and aeration supervisor 43 delivers air to aeration branch pipe 45, and air is delivered to aeration plate 46 by aeration branch pipe 45.Aeration plate 46 produces a large amount of micro-bubble, micro-bubble in uphill process be dissolved in CO in water
2be combined into air pocket, these air pockets rise to the water surface thus make CO
2ease is in air, and micro-bubble sticks unprecipitated tiny turbidity in water simultaneously, makes turbidity rise to the water surface and is collected into discharge in dreg collecting slot 41 by slag scraper 42.Because the aeration stripping pond water surface contains tiny turbidity, therefore the 3rd water outlet 44 in aeration stripping pond is in underwater, and the turbidity in aeration stripping pond can be avoided like this to enter water leg 6.Water after collection is carried by rising pipe 7 by water leg 6.
Claims (10)
1. the collaborative method removing turbidity and temporary hardness in surface water, it is characterized in that, part turbidity in pending surface water is removed by pending surface water successively after flocculation and precipitation, afterwards the surface water removing part turbidity is mixed with acid the HCO made in surface water
3 -cO is produced with acid-respons
2gas, finally again will containing CO
2the surface water aeration stripping of gas removes the CO in surface water
2gas and not removed turbidity.
2. the collaborative method removing turbidity and temporary hardness in surface water as claimed in claim 1, it is characterized in that, the gas-water ratio of described aeration stripping is 6:1, and the aeration stripping time is 10 ~ 20min.
3. realize the structures of the method for turbidity and temporary hardness in the collaborative removal surface water described in claim 1 or 2, it is characterized in that, comprise be communicated with successively flocculation reaction district (1), settling region (2), acid adding reaction zone (3) and aeration stripping district (4);
Part turbidity in pending surface water is removed by pending surface water successively behind flocculation reaction district (1) and settling region (2), afterwards the surface water (3) in acid adding reaction zone removing part turbidity is mixed with acid the HCO made in surface water
3 -cO is produced with acid-respons
2gas, finally again will containing CO
2the CO in surface water removed by the surface water of gas at aeration stripping district (4) aeration stripping
2gas and not removed turbidity.
4. the structures realizing the method for turbidity and temporary hardness in collaborative removal surface water as claimed in claim 3, it is characterized in that, described flocculation reaction district (1) comprises the multiple flocculation basins (11) arranged in a grid formation, the bottom of flocculation basin (11) is communicated with shore pipe (12), adjacent flocculation basin (11) is communicated with the first water outlet (13) and the rational height of the first water outlet (13) on adjacent flocculation basin (11) is different, cross-sectional area along water (flow) direction flocculation basin (11) increases successively, flocculation basin (11) bottom adjacent with settling region (2) arranges the first perforation tracery wall (14) and is communicated with flocculation reaction district (1) and settling region (2).
5. the structures realizing the method for turbidity and temporary hardness in collaborative removal surface water as claimed in claim 3, it is characterized in that, described settling region (2) comprises settling tank, finger-type groove (21) and inclined tube (23) is set gradually from top to bottom in settling tank, water flows from bottom to top along inclined tube (23), realize mud-water separation, the clear water act as after collection and treatment of finger-type groove (21);
Be communicated with shore pipe (12) bottom settling tank, settling tank top is communicated with acid adding reaction zone (3).
6. the structures realizing the method for turbidity and temporary hardness in collaborative removal surface water as claimed in claim 5, it is characterized in that, described inclined tube (23) length is 1m, and the pitch angle of inclined tube (23) is 60 °.
7. the structures realizing the method for turbidity and temporary hardness in collaborative removal surface water as claimed in claim 3, it is characterized in that, described acid adding reaction zone comprises acid adding reaction tank, the underwater of acid adding reaction tank arranges and adds acid tube (31), on the pond body inwall adding acid tube (31) below, level is arranged alternately multiple dividing plate (32), the pond body wall of dividing plate (32) below arranges the second perforation tracery wall (33), and the second perforation tracery wall (33) is communicated with acid adding reaction tank and aeration stripping district (4).
8. the structures realizing the method for turbidity and temporary hardness in collaborative removal surface water as claimed in claim 7, it is characterized in that, the vertical spacing of described adjacent separator (32) is 0.5m.
9. the structures realizing the method for turbidity and temporary hardness in collaborative removal surface water as claimed in claim 3, it is characterized in that, described aeration stripping district (4) comprises aeration stripping pond, in aeration stripping pond, dreg collecting slot (41) is set near the Chi Ding of acid adding reaction zone (3), arrange aerating apparatus at the bottom of the pond in aeration stripping pond, the current after aeration are flowed out by the direction away from dreg collecting slot (41).
10. the structures realizing the method for turbidity and temporary hardness in collaborative removal surface water as claimed in claim 9, it is characterized in that, described aerating apparatus comprises aeration supervisor (43), to arrange multiple aeration branch pipe (45) perpendicular to the direction of aeration supervisor (43), aeration branch pipe (45) is arranged multiple aeration plate (46).
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108640327A (en) * | 2018-04-11 | 2018-10-12 | 西安建筑科技大学 | It is a kind of intensive style turbidity removal and scale removal purifier |
| CN109896586A (en) * | 2019-03-22 | 2019-06-18 | 魏应杰 | A kind of novel decarburization acid device and method |
| CN110240332A (en) * | 2019-05-30 | 2019-09-17 | 西安建筑科技大学 | Dirty processing method and processing device drops in a kind of softening of crystallization filtering type underground water |
| CN111821728A (en) * | 2020-07-31 | 2020-10-27 | 同济大学建筑设计研究院(集团)有限公司 | Slag scraping device and method for sewage treatment |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101798147A (en) * | 2009-12-30 | 2010-08-11 | 中国第一重型机械股份公司 | Pretreatment system of sea water desalinization with hot method |
| CN102557307A (en) * | 2011-11-08 | 2012-07-11 | 兖州煤业股份有限公司 | Process and system for advanced treatment of mine water |
| CN103755096A (en) * | 2014-01-17 | 2014-04-30 | 上海交通大学 | Coupled Fenton oxidation and anaerobic digestion reactor for treating surplus sludge |
-
2015
- 2015-12-15 CN CN201510941179.5A patent/CN105481138B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101798147A (en) * | 2009-12-30 | 2010-08-11 | 中国第一重型机械股份公司 | Pretreatment system of sea water desalinization with hot method |
| CN102557307A (en) * | 2011-11-08 | 2012-07-11 | 兖州煤业股份有限公司 | Process and system for advanced treatment of mine water |
| CN103755096A (en) * | 2014-01-17 | 2014-04-30 | 上海交通大学 | Coupled Fenton oxidation and anaerobic digestion reactor for treating surplus sludge |
Cited By (7)
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| CN108640327A (en) * | 2018-04-11 | 2018-10-12 | 西安建筑科技大学 | It is a kind of intensive style turbidity removal and scale removal purifier |
| CN108640327B (en) * | 2018-04-11 | 2020-08-04 | 西安建筑科技大学 | Intensive water purification unit for turbidity removal and scale removal |
| CN109896586A (en) * | 2019-03-22 | 2019-06-18 | 魏应杰 | A kind of novel decarburization acid device and method |
| CN110240332A (en) * | 2019-05-30 | 2019-09-17 | 西安建筑科技大学 | Dirty processing method and processing device drops in a kind of softening of crystallization filtering type underground water |
| CN110240332B (en) * | 2019-05-30 | 2022-03-08 | 西安建筑科技大学 | Crystallization filtering type underground water softening and scale reducing treatment device |
| CN111821728A (en) * | 2020-07-31 | 2020-10-27 | 同济大学建筑设计研究院(集团)有限公司 | Slag scraping device and method for sewage treatment |
| CN111821728B (en) * | 2020-07-31 | 2023-10-13 | 同济大学建筑设计研究院(集团)有限公司 | Slag scraping device for sewage treatment and method thereof |
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| Publication number | Publication date |
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