CN108640199A - A kind of underground water purified in situ processing method based on complex mineral filtrate - Google Patents
A kind of underground water purified in situ processing method based on complex mineral filtrate Download PDFInfo
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- CN108640199A CN108640199A CN201810438267.7A CN201810438267A CN108640199A CN 108640199 A CN108640199 A CN 108640199A CN 201810438267 A CN201810438267 A CN 201810438267A CN 108640199 A CN108640199 A CN 108640199A
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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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
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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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
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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
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/103—Arsenic compounds
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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
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
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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
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
- C02F2101/203—Iron or iron compound
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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
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/06—Contaminated groundwater or leachate
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The underground water purified in situ processing method based on complex mineral filtrate that the invention discloses a kind of, the complex mineral filtrate mixed in proportion by modified zeolite and natural manganese sand is set in well, to ground water cleaning, purified water is entered by floral tube part in drinking-water pipe to be extracted out from underground;After a period of time complex mineral filtrate activity is poor, it injects activator and activates complex mineral filtrate, purification of ground water can be re-used for, realize long-term recycling complex mineral filtrate, for high-arsenic underground water water quality characteristic, ammonia nitrogen, iron and arsenic three classes major pollutants in water removal can be removed simultaneously;Use environmentally protective natural minerals filtrate at low cost for raw material in processing;Complex mineral filtrate is directly embedded to drinking-water pipe surrounding in underground water pumped well construction work; instead of traditional river sand protective layer, realizes the purified in situ processing of underground water, also save the cost and floor space in surface construction water treatment system; method is simple, and water treatment effect is good.
Description
Technical field
The invention belongs to quality of groundwater processing technology fields, and in particular to a kind of underground water based on complex mineral filtrate
Purified in situ processing method.
Background technology
Arsenic is distributed widely in big gas and water, soil, rock and organism, is a kind of plasm with metalloid characteristic
Poisonous substance, average abundance is 5~10mg/kg in the earth's crust.Arsenic and its toxicity of compound are very big, arsenic by with protein in organism
With the combination of sulfydryl in enzyme, it is suppressed that the various biochemical and metabolic processes in organism.The sulfydryl knot of arsenic and pyruvate oxidase
It closes, so that it is lost activity, cause cell metabolism serious diseases.Arsenic content, which reaches 0.01~0.052g, can make one to be poisoned, and 0.06
~0.2g can be lethal;In air, the maximum permissible concentration of arsenic is 0.003mg/L.Thus arsenic has health very big
Harm.
Arsenic can enter human body by approach such as diet, skin contact, breathings, and arsenic poisoning effect is accumulation, energy
It is carcinogenic in savings liver,kidney,spleen in human body, muscle, bone and keratinized tissue.Acute and chronic arsenic poisoning can cause to breathe
The diseases such as system, digestive system, cardiovascular system, nervous system and hemopoietic system.Since arsenic compound property is stablized, certainly
It is not easily decomposed under right state, thus is easy residual and causes environmental pollution, it is very harmful.
In high-arsenic underground water distributed area, such as Hubei Province's Jianghan Plain, high arsenic in underground water, there are attendant phenomenons for high ferro, and
And since underground water is chronically at reproducibility environment, the ammonia-nitrogen content in underground water is higher.To a local motor-pumped well underground water water sample
Analysis test finds that arsenic from underwater content is more than 0.5mg/L, and total iron content is more than 10mg/L, and ammonia-nitrogen content is more than 2mg/L,
The above index has been more than the limit value of standards for drinking water quality.
In the related technology, independent minimizing technology or device are used for groundwater pollutants such as arsenic, iron, ammonia nitrogens, improved
The cost of groundwater treatment.
Invention content
In view of this, the embodiment provides a kind of groundwater treatment is at low cost, it can combine while remove depollution
The complex mineral filtrate purified in situ processing method of object.
In order to solve the above technical problems, technical solution used in the embodiment of the present invention is, one kind being based on complex mineral filtrate
Underground water purified in situ processing system, including pumped well, pump house and filling mix in proportion by modified zeolite and natural manganese sand
Complex mineral filtrate filter material frame;The pumped well includes drinking-water pipe, and the drinking-water pipe and filter material frame are respectively positioned on underground
In well, drinking-water pipe is located at the center of filter material frame, and its underpart is that tube wall sets foraminate floral tube part;The pump house includes medicament
The end of injection pipe, the medicament injection pipe is located in the complex mineral filtrate of the filter material frame, is injected by the medicament
Pipe injects the activator of activation complex mineral filtrate to the filter material frame.
Preferably, gauze layer is arranged in the floral tube part surface, and height is identical as the filter material frame.
Preferably, the length of the floral tube part is 1~2m, and the aperture of the aperture is 0.8cm~1.2cm;The yarn
The mesh number of layer of cloth is the mesh of 80 mesh~100.
Preferably, river sand protection is set gradually at the top surface of the filter material frame to the well head of the missile silo from top to bottom
Layer and clay water barrier.
Preferably, the inner surface of the filter material frame is strainer;The fixed medicament of bottom setting of the filter material frame
The tubule of injection pipe.
Preferably, further include suction pump, the suction pump is rest on the ground, and is extracted out from the drinking-water pipe purified
Water.
Preferably, the pump house further includes dose-storage bucket and medicament injection pump, medicament injection pump one end with it is described
Dose-storage bucket is connected to, and the other end is connected to the medicament injection pipe.
Preferably, the activator is the mixed solution of hydrochloric acid and sodium chloride.
Preferably, the complex mineral filtrate is 1 according to volume by modified zeolite and natural manganese sand:1 ratio uniform is mixed
It closes;The preparation process of the modified zeolite is:
(2-1) chooses the particle that natural clinoptilolite is broken, and grain size is obtained as 3~5mm after sieve of looking over so as to check;
The particle is placed in acid solution through ultrasonic cleaning by (2-2), and the particle after cleaning, which is placed in salting liquid, to be soaked
Bubble;
Drying obtains modified zeolite after (2-3) takes the particle washes clean after impregnating.
Preferably, MnO in the natural manganese sand2Content is 35% or more, and grain size is 3~5mm.
The underground water purified in situ processing method based on complex mineral filtrate that an embodiment of the present invention provides a kind of, including with
Lower step:
(1) Vertical Well hole is drilled out to underground using drilling machine;
(2) the complex mineral filtrate that modified zeolite and natural manganese sand mix in proportion is filled into filter material frame, by medicine
Agent injection pipe is fixedly connected with the tubule of filter material frame bottom, and mounted filter material frame is placed in borehole bottom;
(3) drinking-water pipe is put into wellhole, the center of the filter material frame is fixed in the floral tube part of drinking-water pipe lower part;
(4) clay, river sand are successively filled around the drinking-water pipe successively, and is compacted at well head;
(5) the medicament injection pipe for exposing river sand layer is connect with medicament injection pump, suction pump respectively with drinking-water pipe, suction pump
From being drawn water in well up to i.e. usable without silt in the water extracted out;
(6) when extracting well water water degradation out, medicament injection pump extracts medicament from dose-storage bucket and passes through medicament injection pipe
It injects in complex mineral filtrate, activates complex mineral filtrate, then extracted out medicament by suction pump, injected to dose-storage bucket
Clear water cleans activated complex mineral filtrate, you can extracts well water again and uses.
Compared with the relevant technologies, the advantageous effect that the technical solution of the embodiment of the present invention offer is brought is:The present invention's
A kind of underground water purified in situ processing method based on complex mineral filtrate, is arranged in well and is pressed by modified zeolite and natural manganese sand
The filter material frame of the complex mineral filtrate of ratio mixing, by complex mineral filtrate to ground water cleaning, purified water passes through
Floral tube part enters in drinking-water pipe extracts out from underground;After a period of time complex mineral filtrate activity is poor, pass through medicament injection pipe
It injects medicament and activates complex mineral filtrate, purification of ground water can be re-used for, realize long-term recycling complex mineral filtrate, needle
To high-arsenic underground water water quality characteristic, ammonia nitrogen, iron and arsenic three classes major pollutants in water removal can be removed simultaneously;System structure is simple,
It is easily operated, it is at low cost.
Description of the drawings
Fig. 1 is the system structure diagram of the embodiment of the present invention;
Fig. 2 is the system partial structural diagram of the embodiment of the present invention;
Fig. 3 is the method flow schematic diagram of the embodiment of the present invention.
Wherein:Filter material frame 1, complex mineral filtrate 11, drinking-water pipe 2, floral tube part 21, wellhole 3, medicament injection pipe 4, river
Husky protective layer 5, clay water barrier 6, suction pump 7, dose-storage bucket 8, medicament injection pump 9.
Specific implementation mode
To make the object, technical solutions and advantages of the present invention clearer, below in conjunction with attached drawing to embodiment party of the present invention
Formula is further described.
Referring to FIG. 1, at the embodiment provides a kind of underground water purified in situ based on complex mineral filtrate
Reason system, including the complex mineral filtrate 11 that is mixed in proportion by modified zeolite and natural manganese sand of pumped well, pump house and filling
Filter material frame 1;The pumped well includes drinking-water pipe 2, and the drinking-water pipe 2 and filter material frame 1 are respectively positioned in subterranean boreholes 3, described
2 lower part of drinking-water pipe is that tube wall sets foraminate floral tube part 21;The complex mineral filtrate 11 is filled in the filter material frame 1
Interior, the floral tube part 21 is located at the center of filter material frame 1;The pump house includes medicament injection pipe 4, the medicament injection pipe 4
End be located in the complex mineral filtrate 11 of the filter material frame 1, by the medicament injection pipe 4 to complex mineral filtrate 11
The complex mineral filtrate 11 of the activator of middle injection activation complex mineral filtrate 11, modified zeolite and natural manganese sand composition purifies
Water afterwards is flowed by the aperture of the floral tube part 21 of the drinking-water pipe 2 in drinking-water pipe 2, and is extracted out underground from drinking-water pipe 2,
Complex mineral filtrate 11 removes arsenic, ammonia nitrogen and the iron three classes major pollutants in underground water, effectively increases water quality;When water quality becomes
When poor, activator is injected by the medicament injection pipe 4 and activates the complex mineral filtrate, the complex mineral filtrate then can be extensive
Its multiple purification function realizes that circulating repetition utilizes, reduces cost, while easy to operation, reduces the difficulty of water process and strong
Degree.
Further, river sand guarantor is set gradually at the top surface of the filter material frame 1 to the well head of the wellhole 3 from top to bottom
Sheath 5 and clay water barrier 6.6 filled media of clay water barrier is the day that quality is fine and smooth, plasticity is good and water penetration is poor
Right clay can gather materials on the spot to obtain, and be compacted after inserting well, and thickness is 1~2m, plays the role of water barrier;The river sand protection
5 filled media of layer are the natural river sand of 50~200 mesh, can gather materials on the spot to obtain, ground is padded up from clay water barrier, are used
In protection drinking-water pipe 2.
Further, further include suction pump 7, the suction pump 7 rest on the ground and is connected with the top of drinking-water pipe 2, from
Extract purified water in the drinking-water pipe 2 out.
Further, the pump house further includes dose-storage bucket 8 and medicament injection pump 9, described 9 one end of medicament injection pump with
The dose-storage bucket 8 is connected to, and the other end is connected to the medicament injection pipe 4.The medicament injection pipe 4 is aluminium-plastic pipe.
Further, 21 height of floral tube part is identical as the height of the filter material frame 1;Gauze is arranged in its surface
Layer, is entered by the aperture of floral tube part 21 in drinking-water pipe 2 through the 11 purified water of complex mineral filtrate in filter material frame 1,
Gauze layer can be further to entering the Water warfare in drinking-water pipe 2.
Further, the aperture of the aperture is 0.8cm~1.2cm;The mesh number of the gauze layer is the mesh of 80 mesh~100.
Further, the filter material frame 1 is annular, is highly interior diameter 20cm, overall diameter 60cm, 1~2m,
Its frame side wall is the PP plates that thickness is 5~10mm, is uniformly distributed the circular hole of diameter 5mm, and the strainer that inner surface is 80 mesh,
Using nylon material;Its bottom, which is the hollow of thickness 20cm, has round-ended cylinder frame, setting to fix the thin of the medicament injection pipe 4
Pipe;The pore of 1~2mm of aperture is uniformly distributed on the tubule.Underground water flows into complex mineral filter by the side wall of filter material frame 1
In material 11, after 11 adsorption cleaning of complex mineral filtrate, through in the aperture on floral tube part 21 to drinking-water pipe 2, being led to by suction pump 7
Drinking-water pipe 2 is crossed to extract out from underground.
Further, the complex mineral filtrate 11 is 1 according to volume by modified zeolite and natural manganese sand:1 ratio is equal
It is even to mix;The preparation process of the modified zeolite is:
(2-1) chooses the particle that natural clinoptilolite is broken, and grain size is obtained as 3~5mm after sieve of looking over so as to check;
The particle is placed in acid solution through ultrasonic cleaning by (2-2), and the particle after cleaning, which is placed in salting liquid, to be soaked
Bubble;The acid solution pH value is 2, the time 10min of ultrasonic cleaning, and the salting liquid is the NaCl solution of 0.5mol/L,
It impregnates for 24 hours;Increase the ammonia nitrogen and heavy metal exchange adsorption capacity of zeolite;
Drying obtains modified zeolite after (2-3) takes the particle washes clean after impregnating.Clear water washes clean, drying temperature are
100℃。
Zeolite is a kind of a kind of manosil AS mineral of aqueous alkali or alkaline earth metal, has porosity, internal gutter
Interior duct and cavity containing exchangeable cations;Natural zeolite often contains various due to its build environment, in duct
Organic or inorganic impurity causes absorption property relatively low.Impurity in natural zeolite duct is removed by modified, sodium salt or sylvite is used in combination
Other metal ions in duct are exchanged, Adsorption effect of the zeolite to ammonia nitrogen can be promoted.The present invention utilizes this of zeolite
Characteristic prepares modified zeolite, and for the ammonia nitrogen pollutant in Adsorption underground water.
Further, MnO in the natural manganese sand2Content is 35% or more, and grain size is 3~5mm.Manganese sand is a kind of natural
Oxidant, the MnO contained2It can play the role of catalysis to the oxidation of Fe in water (II) and Mn (II), by dissolved state
Ferrous iron or bivalent manganese be oxidized into the compound of undissolved ferric iron or tetravalent manganese, reach removing ferro in water and manganese
Purpose purifies water.
The embodiment of the present invention additionally provides a kind of underground water purified in situ processing method based on complex mineral filtrate, including
Following steps:
(1) Vertical Well hole 3 is drilled out to underground using drilling machine;
It (2), will in the filling to filter material frame 1 of complex mineral filtrate 11 mixed modified zeolite and natural manganese sand in proportion
Medicament injection pipe 4 is fixedly connected with the tubule of 1 bottom of filter material frame, and mounted filter material frame 1 is placed in 3 bottom of wellhole;
(3) drinking-water pipe 2 is put into wellhole 3, the filter material frame 1 is fixed in the floral tube part 21 of 2 lower part of drinking-water pipe
Center;
(4) clay, river sand are successively filled from the bottom up around the drinking-water pipe 2 successively, formation river sand protective layer 5,
Clay water barrier 6, and be compacted at well head;
(5) the medicament injection pipe 4 for exposing river sand protective layer 5 is connected with medicament injection pump 9, suction pump 7 respectively with drinking-water pipe 2
It connects, suction pump 7 in well from drawing water up to i.e. usable without silt in the water extracted out;
(6) when extracting well water water degradation out, medicament injection pump 9 extracts activator from dose-storage bucket 8 and is noted by medicament
Enter pipe 4 to inject in complex mineral filtrate, activate complex mineral filtrate, then extracted out activator by suction pump 7, is store to medicament
It deposits 8 injected clear water of bucket and cleans activated complex mineral filtrate 11, you can extract well water again and use.The activator is
The hydrochloric acid of 0.5mol/L and the sodium chloride mixed liquor of 0.5mol/L;Used modified zeolite and natural manganese sand filtrate are using one
After the section time, because absorption ammonia nitrogen reaches saturation inside modified zeolite, adsorption capacity declines;Natural manganese sand then because Surface Fe and
The deposition of manganese forms a large amount of ferrimanganic deposits, reduces ability of the manganese sand except iron, manganese, in this case it is necessary to be filtered to mineral
Material carries out activating and regenerating.
The mechanism of activating and regenerating is to be rinsed to mineral filtrate using faintly acid solution containing sodium ion, and demanganization sand is removed in dissolving
Impurity inside the ferrimanganic deposit and zeolite pores on surface, sodium at high concentration ion can also displace ammonia nitrogen so that zeolite is again
The secondary ability for restoring absorption ammonia nitrogen.Medicament uses water flushing again after injection cleaning a period of time, restores normal water outlet.
Embodiment two
According to embodiments of the present invention one system and method choose Jianghan Plain Xiantao City village of Hubei Province be experimental field, into
Row field experiment.The specific implementation process of this example is as follows:
(1) a diameter of 60cm is drilled out to underground using drilling machine, depth is the wellhole 3 of 15m, keeps well casing perpendicular in drilling process
Directly;
(2) complex mineral filtrate 11 is inserted in the filter material frame 1 of annular, ensures filtrate compacting, does not interspace;By 8
The aluminium-plastic pipe that length is 13m or more, to being connect using nut, ensures connection jail with 8 stainless steel tubules in annular filter material frame 1
Gu and pipe internal channel penetrates through;Mounted annular filter material frame 1 is put into 3 bottom of wellhole;
(3) drinking-water pipe 2 that length is 15m is put into wellhole 3, annular filter is inserted into the floral tube part 21 that bottom lengths are 2m
The central circular of material frame frame 1;
(4) clay, river sand are inserted into 2 surrounding of drinking-water pipe in wellhole 3, the thickness of clay water barrier 6 from the bottom up successively
For 1~2m;11~12m of thickness of river sand protective layer 5 is compacted after completing on ground, ensures that 3 stabilization of wellhole will not settle movement;
(5) after river sand protective layer 5 completes, the drinking-water pipe 2 of 8 medicament injection pipes 4 and center is exposed on ground;By 8 medicaments
Injection pipe 4 is pooled to total injection pipe of a 25~30mm of diameter by adapter, and is connected to the medicament injection of ground computer room
Pump 9;Drinking-water pipe 2 is connected to suction pump 7;
(6) well-flushing to the extraction limpid no silt of water that starts to draw water after installing can begin to use well water;System operation 1
A month or so or observe effluent quality be deteriorated can utilize medicament activating and regenerating mineral filtrate absorption property;First on ground
The sodium chloride mixed liquor that the hydrochloric acid and 0.5mol/L of 0.5mol/L are prepared in computer room medicament barrel, opens medicament injection pump 9, by 100L
Medicament is slowly injected into well, and zeolite and manganese sand are reactivated, while opening the extraction of the medicament after suction pump 7 will use;Then
100L clear water is put into medicament barrel again, mineral filtrate is cleaned in injection complex mineral filtrate 11;Implement through the present invention
The water quality comparison before and after the processing of the system and method for example is shown in Table 1.Remaining is the same as embodiment one.
System and method of 1 water quality of table through embodiment of the present invention data comparison before and after the processing
The method of the embodiment of the present invention is directed to high-arsenic underground water water quality characteristic, can remove ammonia nitrogen, iron and arsenic in water removal simultaneously
Three classes major pollutants;Use natural minerals filtrate for raw material in processing, have it is environmentally protective, it is cheap and easy to get, it is at low cost etc.
Advantage;Complex mineral filtrate 11 is directly embedded to 2 surrounding of drinking-water pipe in underground water pumped well construction work, instead of traditional river
Husky protective layer 5, may be implemented underground water purified in situ processing, also save surface construction water treatment system cost and account for
Ground area, method is simple, and water treatment effect is good.
Herein, the nouns of locality such as involved front, rear, top, and bottom are to be located in figure with parts in attached drawing and zero
Part mutual position defines, only for the purpose of expressing the technical solution clearly and conveniently.It should be appreciated that the noun of locality
Use should not limit the claimed range of the application.
In the absence of conflict, the feature in embodiment and embodiment herein-above set forth can be combined with each other.
The foregoing is merely presently preferred embodiments of the present invention, is not intended to limit the invention, it is all the present invention spirit and
Within principle, any modification, equivalent replacement, improvement and so on should all be included in the protection scope of the present invention.
Claims (7)
1. a kind of underground water purified in situ processing method based on complex mineral filtrate, characterized in that include the following steps:
(1) Vertical Well hole is drilled out to underground using drilling machine;
(2) the complex mineral filtrate that modified zeolite and natural manganese sand mix in proportion is filled into filter material frame, medicament is noted
Enter pipe to be fixedly connected with the tubule of filter material frame bottom, mounted filter material frame is placed in borehole bottom;
(3) drinking-water pipe is put into wellhole, the center of the filter material frame is fixed in the floral tube part of drinking-water pipe lower part;
(4) clay, river sand are successively filled from the bottom up around the drinking-water pipe successively, formed river sand protective layer, clay every
Water layer, and be compacted at well head;
(5) the medicament injection pipe for exposing river sand protective layer is connect with medicament injection pump, suction pump respectively with drinking-water pipe, suction pump
From being drawn water in well up to i.e. usable without silt in the water extracted out;
(6) when extracting well water water degradation out, medicament injection pump extracts activator from dose-storage bucket and is noted by medicament injection pipe
Enter in complex mineral filtrate, activate complex mineral filtrate, then extracted out activator by suction pump, is injected to dose-storage bucket
Clear water cleans activated complex mineral filtrate, you can extracts well water again and uses.
2. a kind of underground water purified in situ processing method based on complex mineral filtrate according to claim 1, feature
It is that in the step (2), the complex mineral filtrate is 1 according to volume by modified zeolite and natural manganese sand:1 ratio uniform
It mixes;The preparation process of the modified zeolite is:
(2-1) chooses the particle that natural clinoptilolite is broken, and grain size is obtained as 3~5mm after sieve of looking over so as to check;
The particle is placed in acid solution through ultrasonic cleaning by (2-2), and the particle after cleaning, which is placed in salting liquid, to be impregnated;
Drying obtains modified zeolite after (2-3) takes the particle washes clean after impregnating.Clear water washes clean, drying temperature 100
℃。
3. a kind of underground water purified in situ processing method based on complex mineral filtrate according to claim 2, feature
It is that in the step (2-2), the acid solution pH value is 2, the time 10min of ultrasonic cleaning, and the salting liquid is
The NaCl solution of 0.5mol/L is impregnated for 24 hours.
4. a kind of underground water purified in situ processing method based on complex mineral filtrate according to claim 1, feature
It is that in the step (2), the floral tube Partial Height is identical as the height of the filter material frame;Gauze layer, yarn is arranged in its surface
The mesh number of layer of cloth is the mesh of 80 mesh~100;The aperture of the aperture of floral tube part is 0.8cm~1.2cm.
5. a kind of underground water purified in situ processing method based on complex mineral filtrate according to claim 1, feature
It is that in the step (2), the filter material frame is annular, and side wall is uniformly distributed circular hole, and strainer is arranged in inner surface;Its bottom
It is hollow to have round-ended cylinder frame, the tubule of the fixed medicament injection pipe of setting;It is uniformly distributed 1~2mm's of aperture on the tubule
Pore.
6. a kind of underground water purified in situ processing method based on complex mineral filtrate according to claim 1, feature
It is that in the step (4), the thickness of the clay water barrier is 1~2m;The river sand protective layer filled media is 50~200
Purpose natural river sand.
7. a kind of underground water purified in situ processing method based on complex mineral filtrate according to claim 1, feature
It is that in the step (6), the activator is the sodium chloride mixed liquor of the hydrochloric acid and 0.5mol/L of 0.5mol/L.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111334661A (en) * | 2019-12-13 | 2020-06-26 | 四川共拓岩土科技股份有限公司 | Method for quickly injecting in-situ leaching solution |
CN113877304A (en) * | 2021-09-07 | 2022-01-04 | 哈尔滨工业大学 | Preparation method and application of functionalized deep manganese removal filter material |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000117020A (en) * | 1998-10-16 | 2000-04-25 | Konichi Komatsu | Contact purifying material and its production |
CN105967442A (en) * | 2016-06-03 | 2016-09-28 | 吉林大学 | Method for in-situ removal of iron, manganese and ammonia nitrogen in underground water and in-situ well design method |
CN107673440A (en) * | 2017-11-22 | 2018-02-09 | 南昌工程学院 | A kind of well and method for removing iron for removing Fe Element in Groundwater |
-
2018
- 2018-05-09 CN CN201810438267.7A patent/CN108640199A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2000117020A (en) * | 1998-10-16 | 2000-04-25 | Konichi Komatsu | Contact purifying material and its production |
CN105967442A (en) * | 2016-06-03 | 2016-09-28 | 吉林大学 | Method for in-situ removal of iron, manganese and ammonia nitrogen in underground water and in-situ well design method |
CN107673440A (en) * | 2017-11-22 | 2018-02-09 | 南昌工程学院 | A kind of well and method for removing iron for removing Fe Element in Groundwater |
Non-Patent Citations (2)
Title |
---|
商平: "《环境矿物材料》", 31 January 2009, 化学工业出版社 * |
李彩霞等: "膨润土/沸石制备猫砂实验研究", 《硅酸盐通报》 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111334661A (en) * | 2019-12-13 | 2020-06-26 | 四川共拓岩土科技股份有限公司 | Method for quickly injecting in-situ leaching solution |
CN113877304A (en) * | 2021-09-07 | 2022-01-04 | 哈尔滨工业大学 | Preparation method and application of functionalized deep manganese removal filter material |
CN113877304B (en) * | 2021-09-07 | 2023-01-10 | 哈尔滨工业大学 | Preparation method and application of functionalized deep manganese removal filter material |
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