CN113816565B - Integrated assembly type water treatment equipment - Google Patents

Integrated assembly type water treatment equipment Download PDF

Info

Publication number
CN113816565B
CN113816565B CN202111181301.5A CN202111181301A CN113816565B CN 113816565 B CN113816565 B CN 113816565B CN 202111181301 A CN202111181301 A CN 202111181301A CN 113816565 B CN113816565 B CN 113816565B
Authority
CN
China
Prior art keywords
tank
water
filter
denitrification
inner sleeve
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN202111181301.5A
Other languages
Chinese (zh)
Other versions
CN113816565A (en
Inventor
沈传明
徐敬
李学勤
沈加坡
颜野迪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jing Hua Holding Group Co ltd
Original Assignee
Jing Hua Holding Group Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jing Hua Holding Group Co ltd filed Critical Jing Hua Holding Group Co ltd
Priority to CN202310172777.5A priority Critical patent/CN116282678A/en
Priority to CN202111181301.5A priority patent/CN113816565B/en
Publication of CN113816565A publication Critical patent/CN113816565A/en
Application granted granted Critical
Publication of CN113816565B publication Critical patent/CN113816565B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • C02F1/30—Treatment of water, waste water, or sewage by irradiation
    • C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
    • C02F1/325—Irradiation devices or lamp constructions
    • 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
    • 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
    • C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • C02F1/56—Macromolecular compounds
    • 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
    • C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
    • 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
    • C02F2001/007—Processes including a sedimentation step
    • 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
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00—Specific treatment goals
    • C02F2303/04—Disinfection
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/28—Anaerobic digestion processes
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/10—Biological treatment of water, waste water, or sewage

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)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

The application discloses assembled water treatment facilities integrates, including denitrification tank, flocculation tank and filter tank, be provided with the haydite filter material in the denitrification tank, be provided with stirring rake and inclined immersed tube in the flocculation tank, be provided with the quartz sand filter layer in the filter tank, the tank bottoms of pipeline and flocculation tank are passed through to the tank deck of denitrification tank meets, and the tank deck of flocculation tank meets through the tank deck of pipeline and filter tank. The invention has the following beneficial effects: the combined use of the denitrification tank, the flocculation tank and the filtering tank is adopted, the integrated modular assembly type installation is realized, the installation is more convenient, no odor is generated in the treatment process, and the production field is saved more.

Description

Integrated assembly type water treatment equipment
Technical Field
The invention relates to the field of water purification, in particular to integrated assembled water treatment equipment.
Background
A large amount of sewage can be produced in industrial and agricultural production at present, in order to treat the sewage, a simple small-sized sewage treatment plant is built in many production type enterprises, the small-sized sewage treatment plant generally comprises three water tanks, namely a denitrification tank, a flocculation tank and a filtering tank, and the small-sized sewage treatment plant has the following defects: the first is that the three pools are all exposed, a large amount of odor is generated in the treatment process, and the probability of falling into water by workers exists; secondly, a small sewage treatment plant needs to occupy a larger production field.
Disclosure of Invention
The invention aims at the problems and provides an integrated assembly type water treatment device.
The technical scheme adopted by the invention is as follows:
the utility model provides an integrate assembled water treatment facilities, includes denitrification tank, flocculation tank and filter tank, be provided with the haydite filter material in the denitrification tank, be provided with stirring rake and inclined immersed tube in the flocculation tank, be provided with the quartz sand filter bed in the filter tank, the tank deck of denitrification tank meets through the tank bottoms of pipeline with the flocculation tank, and the tank deck of flocculation tank meets through the tank deck of pipeline with the filter tank.
Among this intermediate treatment facility, adopted denitrification jar, flocculation tank and filter tank combination to use together, realized integrated form modularization assembled installation, it is more convenient to install, can not have the foul smell to produce in the processing procedure, practices thrift the production place more.
The function of each pot in the device is as follows
The sewage flows from bottom to top (passes through a filter layer in the denitrification tank), a large amount of denitrification biological flora grows on the surface of the ceramsite filter material under the anoxic condition, and simultaneously, a high-quality carbon source is added, so that nitrite and nitrate are converted into nitrogen through denitrification, and the nitrogen is released from water. Compared with a deep bed filter tank adopting a quartz sand filter material, the denitrification capacity is greatly improved, the requirements of higher total nitrogen incoming water and lower total nitrogen outgoing water can be met, the denitrification tank adopts a design of flowing from bottom to top, drop oxygenation is avoided, a carbon source is saved, a nitrogen driving device is saved, the filtering speed is higher, the period is longer, and more efficient denitrification is realized.
And the flocculation tank is used for adding PAC (polyaluminium chloride) on a water outlet pipe of the denitrification tank and adding PAM (polyacrylamide) in the flocculation tank. Utilize the mechanical promotion of mixer, the active mud sediment of lower part is in the internal circulation flow of reaction barrel, fully contacts, collides and adsorbs with intaking, and continuous flocculation reaction takes place to realize the degree of depth of phosphorus and get rid of and the getting rid of suspended solid.
And the filter tank penetrates through the quartz sand filtering layer from top to bottom, the depth removal of solid suspended matters is realized through the interception of the thick filtering layer, and the SS (suspended solid) of the effluent is less than 2.0mg/L.
It needs to be further explained that the denitrification tank, the flocculation tank and the filtering tank in the scheme are actually integrated into a large tank, and mainly comprise two large cylinders, wherein the large cylinder inside is the flocculation tank, and the denitrification tank and the flocculation tank are separated from each other by a gap between the large cylinder inside and the large cylinder outside.
It is optional, the tank bottoms department of denitrification jar has connect the circular shape inlet tube, be provided with the manger plate post in the inlet tube, the diameter of manger plate post equals with the internal diameter of inlet tube, has seted up spiral helicine runner on the lateral wall of manger plate post, and the end department of manger plate post is provided with the hook hole, the inlet tube is the inlet tube of plastics material, the manger plate post is the manger plate post of metal material.
The spiral flow channel is arranged on the side wall of the water retaining column, the diameter of the water retaining column is equal to the inner diameter of the water inlet pipe, the design is that the water retaining column is attached to the pipe wall of the water inlet pipe, sewage flows away from the flow channel of the water retaining column, so that the sewage flows away in the water inlet pipe equivalently to form a spiral curve, compared with a linear mode, the flow speed of the sewage can be reduced by the walking method of the spiral curve, the sewage flows towards the denitrification tank more stably, the friction between the water and the pipeline and the water retaining column can be increased by the walking method of the spiral curve, the water temperature of the sewage is increased, the denitrification reaction speed can be properly accelerated when denitrification is carried out, and three water continuously rubs and hits the water retaining column and the water inlet pipe, silt (including other particles of the same type) dissolved and suspended in the sewage can be attached to the water retaining column and the water inlet pipe, so that the influence of the denitrification reaction on denitrifying bacteria can be furthest reduced.
The metal support is selected for use to specific manger plate post, and the surface of manger plate post is the matte, and the inlet tube is the inlet tube of plastics material, and the inner wall of inlet tube is the smooth surface, can let most silt particle all attach to the surface of manger plate post like this, only need hook the hook hole on the manger plate post with the hook when needing to clear up, can pull out the inlet tube with the manger plate post.
Optionally, the water blocking column has many, and the axis of all water blocking columns coincides each other, and the spiral direction of the runner on two adjacent water blocking columns is opposite, and the hook hole intercommunication runner.
The water retaining columns are arranged, the spiral directions of two adjacent water retaining columns are opposite, water flow can be repeatedly switched between left rotation and right rotation due to the design, collision among suspended particles in water can be increased as much as possible due to repeated switching, most suspended particles can be attached to the water retaining columns, meanwhile, due to the flow direction switching of the water flow, the water temperature of sewage can be increased relatively higher, and the reaction speed can be accelerated as much as possible during subsequent denitrification reaction.
It should be noted that the water retaining column can remove a part of silt and other substances, but cannot remove all silt, and the silt remaining in the sewage still needs to be flocculated and precipitated by a flocculation tank by using a chemical flocculant.
Optionally, the water inlet device is further included, and the water inlet device is installed at the interface of the water inlet pipe; the water inlet device comprises a joint pipe, a filter barrel, an inner barrel and a retainer ring, the filter barrel is connected with the joint pipe, the inner barrel is arranged in the filter barrel, a hole is formed in the wall of the filter barrel, the wall of the inner barrel is parallel to that of the filter barrel, the retainer ring is arranged on the joint pipe, the retainer ring is horn-shaped, the filter barrel is positioned in the retainer ring, and a gap is formed between the retainer ring and the filter barrel.
Because sewage can have some large particulate matters when flowing into the inlet tube, some large particulate matters can be crushed and some cannot be crushed, the water inlet device is arranged, when water flows through the holes in the filter vat, the crushed particles can be crushed into smaller particles under the action of the holes, the particles which cannot be crushed can be blocked outside the filter vat, and meanwhile, the large particulate matters blocked outside the filter vat can be collected by the retainer ring due to the existence of the retainer ring.
The inner barrel is arranged in the filter vat, and the design is to realize the diversion of water flow by using the blocking effect of the inner barrel, so that the sewage flows into the filter vat and then is diverted, and then flows to the joint pipe (the joint pipe is connected with the water inlet pipe).
Therefore, to sum up, the existence of water installations can play the effect of smashing large granule silt in advance, avoids silt to block up the plunger.
Optionally, the water inlet device further comprises a guide sleeve, the guide sleeve is arranged in the inner cylinder, and the guide sleeve is parallel to the inner cylinder.
The guide sleeve has the function of leading the flowing water to stably flow to one direction after the flowing water is collected.
Optionally, the filter tank further comprises a water drainage pipe, wherein the water drainage pipe is arranged at the bottom of the filter tank and is connected with a sterilization device; the sterilizing device comprises a water outlet nozzle, an inner sleeve and an outer sleeve, the water outlet nozzle is connected with the water discharge pipe, the water outlet nozzle is fixedly arranged at one end of the inner sleeve, the water outlet nozzle is located outside the inner sleeve, a gap exists between the water outlet nozzle and the inner sleeve, the outer sleeve is sleeved outside the inner sleeve, the inner sleeve is made of transparent materials, and an ultraviolet lamp is arranged between the inner sleeve and the outer sleeve.
Because the bacterial content of sewage is very high, after denitrification, flocculation and filtration, the content of bacteria in water can not be effectively reduced (a part of bacteria can be adsorbed by flocculation and filtration), but the content is still very high, and some agricultural water has a limit on the bacterial content in water, and if the bacterial content is too high, the water cannot be used, so the sterilizing device is arranged, and the sterilizing device has the function of sterilizing flowing water leaving from a drain pipe to reduce the bacterial content in water.
The principle of the specific sterilization device is as follows, firstly, the water outlet nozzle is connected with the water discharge pipe, water leaving from the water outlet nozzle enters the inner sleeve, the water outlet nozzle is positioned outside the inner sleeve, and a gap exists between the water outlet nozzle and the inner sleeve, so that a negative pressure is formed near water flow, nearby gas can be pressed to the vicinity of the water flow continuously and continuously, part of gas can be mixed with water, in the process, due to the irradiation of the ultraviolet lamp, part of oxygen can be converted into ozone, part of ozone can be dissolved in the water, the ozone can kill bacteria in the water, and the bacteria content of discharged water is reduced.
The sterilization device is equivalent to a circle of airflow (airflow has the trend of flowing water columns) coated outside the water columns, and a layer of ultraviolet rays is coated outside the airflow, so that the sterilization device can sterilize flowing water at 360 degrees without dead angles, and the sterilization is more comprehensive.
The inner sleeve is made of glass, and the outer sleeve is made of metal, so that ultraviolet rays can be prevented from being exposed.
Optionally, the inner skleeve is the loudspeaker form, and goes out the water jet and be located inner skleeve's narrow mouth end one side, the outer sleeve is the round platform form.
The inner sleeve is in a horn shape, and the water outlet nozzle is positioned on one side of the narrow opening end of the inner sleeve, so that water flow (including air flow) flows from narrow to wide, and the splashing phenomenon generated when the water flow flows out is reduced. The outer sleeve is in a circular truncated cone shape, so that a plurality of water pipes can be connected conveniently.
Optionally, a funnel-shaped arc surface is arranged at the narrow-mouth end of the inner sleeve.
The funnel-shaped arc surface is arranged to play a role in guiding gas, so that gas can be mixed with water flow, and meanwhile, the dissipation phenomenon of the water flow can be reduced.
Optionally, the denitrification tank is connected with a vacuum pump through a pipeline (the pipeline is positioned above the liquid level).
The vacuum pump is arranged at the top of the denitrification tank, so that the denitrification tank is vacuumized at regular time, negative pressure is formed in the denitrification tank, nitrogen generated in the reaction process can escape from water conveniently, and the denitrification reaction can be accelerated.
Optionally, the inclined immersed tube is a ceramic inclined immersed tube.
The inclined settling tank is made of pottery clay, so that the inclined settling pipe has the characteristic of being porous, particles are adsorbed as much as possible, the weight of the whole tank body can be reduced, and the inclined settling tank is convenient to assemble.
The invention has the beneficial effects that: the combined use of the denitrification tank, the flocculation tank and the filtering tank is adopted, the integrated modular assembly type installation is realized, the installation is more convenient, no odor is generated in the treatment process, and the production field is saved more.
Description of the drawings:
figure 1 is a schematic diagram of an integrated assembly type water treatment device,
figure 2 is a schematic sketch of the structure of a water-retaining column,
figure 3 is a schematic diagram of the structure of a water intake device,
figure 4 is a schematic cross-sectional view of a water intake device,
figure 5 is a schematic diagram of the structure of the sterilization device,
FIG. 6 is a schematic diagram of the mating relationship of the inner sleeve and the water outlet nozzle.
The figures are numbered: 1. a water inlet pipe; 2. a denitrification tank; 201. filtering with ceramsite; 3. a flocculation tank; 301. obliquely sinking the pipe; 302. a stirring paddle; 4. a filter tank; 401. quartz sand; 5. a drain pipe; 6. a water blocking column; 601. a flow channel; 602. a hook hole; 701. a joint pipe; 702. a guide sleeve; 703. an inner barrel; 704. a retainer ring; 705. a filter vat; 801. a water outlet nozzle; 802. a support; 803. an inner sleeve; 804. an outer sleeve.
The specific implementation mode is as follows:
the present invention will be described in detail below with reference to the accompanying drawings.
As shown in the attached figure 1, an integrated assembled water treatment device comprises a denitrification tank 2, a flocculation tank 3 and a filtration tank 4, wherein a ceramsite filter material 201 is arranged in the denitrification tank 2, a stirring paddle 302 and an inclined immersed tube 301 are arranged in the flocculation tank 3, a quartz sand 401 filter layer is arranged in the filtration tank 4, the tank top of the denitrification tank 2 is connected with the tank bottom of the flocculation tank 3 through a pipeline, and the tank top of the flocculation tank 3 is connected with the tank top of the filtration tank 4 through a pipeline.
Among this intermediate treatment facility, adopted denitrification jar 2, flocculation tank 3 and filter tank 4 combination and used together, realized integrated form modularization assembled installation, it is more convenient to install, can not have the foul smell to produce in the processing procedure, practices thrift the production place more.
The function of each pot in the device is as follows
In the denitrification tank 2, sewage flows from bottom to top (passes through a filter layer in the denitrification tank 2), under the anoxic condition, a large amount of denitrification biological flora grows on the surface of the ceramsite filter material 201, and simultaneously, a high-quality carbon source is added, so that nitrite and nitrate are converted into nitrogen through denitrification, and the nitrogen is released from water. Compared with a deep bed filter tank adopting quartz sand 401 filter materials, the denitrification capacity is greatly improved, the requirements of higher total nitrogen incoming water and lower total nitrogen outgoing water can be met, the denitrification tank 2 adopts a design of flowing from bottom to top, drop oxygenation is avoided, a carbon source is saved, a nitrogen driving device is saved, the filtering speed is higher, the period is longer, and more efficient denitrification is realized.
And a flocculation tank 3, PAC is added on a water outlet pipe of the denitrification tank 2, and PAM is added in the flocculation tank 3. Utilize the mechanical promotion of mixer, the active mud sediment of lower part is in the internal circulation flow of reaction barrel, fully contacts, collides and adsorbs with intaking, and continuous flocculation reaction takes place to realize the degree of depth of phosphorus and get rid of and the getting rid of suspended solid.
And the filter tank 4 penetrates through the quartz sand 401 filter layer from top to bottom, the depth removal of solid suspended matters is realized through the interception of the thick filter layer, and the SS (suspended solid) of the effluent is less than 2.0mg/L.
It should be further explained that the denitrification tank 2, the flocculation tank 3 and the filtration tank 4 in the present scheme are actually integrated into a large tank, and mainly comprise two large cylinders, the large cylinder inside is the flocculation tank 3, and the gap between the large cylinder inside and the large cylinder outside is divided into the denitrification tank 2 and the flocculation tank 3 which are independent.
As shown in attached figures 1 and 2, the tank bottom of the denitrification tank 2 is connected with a circular water inlet pipe 1, a water blocking column 6 is arranged in the water inlet pipe 1, the diameter of the water blocking column 6 is equal to the inner diameter of the water inlet pipe 1, a spiral flow channel 601 is formed in the side wall of the water blocking column 6, a hook hole 602 is formed in the end of the water blocking column 6, the water inlet pipe 1 is made of plastic, and the water blocking column 6 is made of metal.
The water blocking column 6 is arranged, the spiral flow channel 601 is formed in the side wall of the water blocking column 6, the diameter of the water blocking column 6 is equal to the inner diameter of the water inlet pipe 1, the design is that the water blocking column 6 is attached to the pipe wall of the water inlet pipe 1, sewage flows away from the flow channel 601 of the water blocking column 6, the sewage flows along a spiral curve in the water inlet tank, compared with a linear mode, the flow speed of the sewage can be reduced by the spiral curve, the sewage flows towards the denitrification tank 2 more stably, the friction between the water and the pipeline and the water blocking column 6 can be increased, the water temperature of the sewage is increased, the denitrification reaction speed can be properly accelerated when denitrification is carried out, and sediment (including other same type particles) particles dissolved and suspended in the sewage can be attached to the water blocking column 6 and the water inlet pipe 1 in the process that the water continuously rubs against the water blocking column 6 and the water inlet pipe 1, and therefore the influence of denitrification reaction on denitrification bacteria can be reduced to the maximum extent.
Concrete manger plate post 6 chooses for use the metal to support, and the surface of manger plate post 6 is the matte, and inlet tube 1 is the inlet tube 1 of plastics material, and the inner wall of inlet tube 1 is the smooth surface, can let most silt granule all adhere to the surface of manger plate post 6 like this, only need hook the hook hole 602 on the manger plate post 6 with the hook when needing to clear up, can pull out inlet tube 1 with manger plate post 6.
As shown in fig. 2, there are a plurality of water blocking columns 6, the central axes of all the water blocking columns 6 are overlapped with each other, the spiral directions of the flow channels 601 on two adjacent water blocking columns 6 are opposite, and the hook holes 602 communicate with the flow channels 601.
The water retaining columns 6 are arranged, the spiral directions of two adjacent water retaining columns 6 are opposite, water flow can be repeatedly switched between left rotation and right rotation through the design, collision among suspended particles in water can be increased as much as possible through repeated switching, most suspended particles can be attached to the water retaining columns 6, meanwhile, due to the fact that the flow direction of the water flow is switched, the water temperature of sewage can be increased relatively higher, and the reaction speed can be accelerated as much as possible during subsequent denitrification reaction.
It should be noted that the water blocking column 6 can remove a part of silt and other substances, but cannot remove all silt, and the silt remaining in the sewage still needs to be flocculated and precipitated by the flocculation tank 3 through a chemical flocculant.
As shown in fig. 1, 3 and 4, the water inlet device is also included and is installed at the interface of the water inlet pipe 1; the water inlet device comprises a joint pipe 701, a filter barrel 705, an inner cylinder 703 and a retainer ring 704, wherein the filter barrel is connected with the joint pipe 701, the inner cylinder 703 is arranged in the filter barrel, the wall of the filter barrel 705 is provided with a hole, the wall of the inner cylinder 703 is parallel to the wall of the filter barrel, the retainer ring 704 is arranged on the joint pipe 701, the retainer ring 704 is horn-shaped, the filter barrel 705 is positioned in the retainer ring 704, and a gap is reserved between the retainer ring 704 and the filter barrel 705.
Because the sewage can have some large particles when flowing into the water inlet pipe 1, and thus some large particles can be crushed and some large particles can not be crushed, the water inlet device is provided, when the water flows through the holes on the filter barrel 705, the particles which can be crushed into smaller particles under the action of the holes, and the particles which can not be crushed can be blocked outside the filter barrel 705, and meanwhile, the large particles blocked outside the filter barrel 705 can be collected by the blocking ring 704 due to the existence of the blocking ring 704.
The inner cylinder 703 is provided in the filter barrel 705, and is designed to turn the flow of the sewage after flowing into the filter barrel 705 by using the blocking effect of the inner cylinder 703, so that the sewage is turned first and then flows to the joint pipe 701 (the joint pipe 701 is used for connecting with the water inlet pipe 1).
Therefore, to sum up, the existence of water installations can play the effect of smashing large granule silt in advance, avoids silt to block up plunger 6.
As shown in fig. 3 and 4, the water inlet device further includes a guiding sleeve 702, the guiding sleeve 702 is disposed in the inner cylinder 703, and the guiding sleeve 702 is parallel to the inner cylinder 703.
The guide sleeve 702 functions to allow the flowing water to stably flow in one direction after the flowing water is collected.
As shown in the attached figures 1, 5 and 6, the water filter further comprises a drain pipe 5, the drain pipe 5 is arranged at the bottom of the filter tank 4, and the drain pipe 5 is connected with a sterilizing device; the sterilization device comprises a water outlet nozzle 801, an inner sleeve 803 and an outer sleeve, wherein the water outlet nozzle 801 is connected with the water discharge pipe 5, the water outlet nozzle 801 is fixedly arranged at one end of the inner sleeve 803, the water outlet nozzle 801 is positioned outside the inner sleeve 803, a gap is formed between the water outlet nozzle 801 and the inner sleeve 803, the outer sleeve is sleeved outside the inner sleeve 803, the inner sleeve 803 is a transparent inner sleeve 803, and an ultraviolet lamp is arranged between the inner sleeve 803 and the outer sleeve.
Because the bacteria content of the sewage is very high, after denitrification, flocculation and filtration, the content of bacteria in the water cannot be effectively reduced (a part of bacteria can be adsorbed by the flocculation and filtration), but the content is still very high, and some agricultural water has a limit on the bacteria content in the water, and if the bacteria content is too high, the water cannot be used, so the sterilization device is arranged, and the sterilization device has the function of performing certain sterilization on running water leaving from the drain pipe 5 to reduce the bacteria content in the water.
The principle of the specific sterilization device is that firstly, the water outlet nozzle 801 is connected with the water discharge pipe 5, water leaving from the water outlet nozzle 801 enters the inner sleeve 803, because the water outlet nozzle 801 is positioned outside the inner sleeve 803, and a gap exists between the water outlet nozzle 801 and the inner sleeve 803, a negative pressure is formed near water flow, nearby gas is continuously pressed near the water flow, part of the gas is mixed with the water, in the process, part of oxygen is converted into ozone due to the irradiation of an ultraviolet lamp, so that part of ozone is dissolved in the water, and because the ozone can kill bacteria in the water, the bacteria content of the discharged water is reduced.
The sterilization device is equivalent to a circle of airflow (airflow has the trend of flowing water columns) coated outside the water columns, and a layer of ultraviolet rays is coated outside the airflow, so that the sterilization device can sterilize flowing water at 360 degrees without dead angles, and the sterilization is more comprehensive.
In particular, the inner sleeve 803 is made of glass and the outer sleeve is made of metal, so that exposure of ultraviolet rays can be prevented.
As shown in fig. 5 and 6, the inner sleeve 803 is horn-shaped, and the water outlet nozzle 801 is located at one side of the narrow end of the inner sleeve 803, and the outer sleeve is truncated cone-shaped.
Specifically, the inner sleeve 803 is trumpet-shaped, and the water outlet nozzle 801 is located at one side of the narrow end of the inner sleeve 803, so that the water flow (including the air flow) flows from narrow to wide, and the splashing phenomenon generated when the water flow flows out is reduced. The outer sleeve is in a circular truncated cone shape, so that a plurality of water pipes can be connected conveniently.
As shown in fig. 5 and 6, the narrow end of the inner sleeve 803 is provided with a funnel-shaped arc surface.
The funnel-shaped arc surface is arranged to play a role in guiding gas, so that gas can be mixed with water flow, and meanwhile, the dissipation phenomenon of the water flow can be reduced.
As shown in the figure, the denitrification tank 2 is connected with a vacuum pump through a pipeline (the pipeline is positioned above the liquid level).
The vacuum pump is arranged at the top of the denitrification tank 2, so that the denitrification tank 2 is vacuumized at regular time, negative pressure is formed in the denitrification tank 2, nitrogen generated in the reaction process can escape from water conveniently, and the denitrification reaction can be accelerated.
As shown in fig. 1, the dip tube 301 is a ceramic dip tube 301.
The inclined sinking tank is made of pottery clay, so that the inclined sinking pipe 301 has the characteristic of being porous, particles are adsorbed as much as possible, the weight of the whole tank body can be reduced, and the assembly is convenient.
It should be further noted that the arrows in fig. 1 and fig. 4 are schematic flow directions of the water flow.
The above description is only a preferred embodiment of the present invention, and is not intended to limit the scope of the present invention, which is defined by the claims, and all the modifications and equivalents of the claims, which can be directly or indirectly applied to other related fields, are also included in the scope of the present invention.

Claims (6)

1. An integrated assembly type water treatment device is characterized by comprising a denitrification tank, a flocculation tank and a filtering tank, wherein a ceramsite filter material is arranged in the denitrification tank, a stirring paddle and an inclined immersed tube are arranged in the flocculation tank, a quartz sand filter layer is arranged in the filtering tank, the tank top of the denitrification tank is connected with the tank bottom of the flocculation tank through a pipeline, and the tank top of the flocculation tank is connected with the tank top of the filtering tank through a pipeline;
the denitrification tank is characterized in that a circular water inlet pipe is connected to the bottom of the denitrification tank, a water blocking column is arranged in the water inlet pipe, the diameter of the water blocking column is equal to the inner diameter of the water inlet pipe, a spiral flow channel is formed in the side wall of the water blocking column, a hook hole is formed in the end of the water blocking column, the water inlet pipe is made of plastic materials, and the water blocking column is made of metal materials;
the water blocking columns are provided with a plurality of water blocking columns, the central axes of all the water blocking columns are overlapped, the spiral directions of the flow channels on two adjacent water blocking columns are opposite, and the hook holes are communicated with the flow channels;
the water inlet device is arranged at the interface of the water inlet pipe; the water inlet device comprises a joint pipe, a filter cylinder, an inner cylinder and a retainer ring, the filter cylinder is connected with the joint pipe, the inner cylinder is arranged in the filter cylinder, a hole is formed in the cylinder wall of the filter cylinder, the cylinder wall of the inner cylinder is parallel to the cylinder wall of the filter cylinder, the retainer ring is arranged on the joint pipe, the retainer ring is horn-shaped, the filter cylinder is positioned in the retainer ring, and a gap is formed between the retainer ring and the filter cylinder;
the water inlet device also comprises a guide sleeve, the guide sleeve is arranged in the inner cylinder, and the guide sleeve is parallel to the inner cylinder;
the surface of the water blocking column is used for attaching silt particles;
the inner cylinder turns the sewage after flowing into the filter cylinder.
2. An integrated assembled water treatment device as claimed in claim 1, further comprising a drain pipe, wherein the drain pipe is arranged at the bottom of the filter tank, and a sterilization device is connected to the drain pipe; the sterilizing device comprises a water outlet nozzle, an inner sleeve and an outer sleeve, the water outlet nozzle is connected with the water discharge pipe, the water outlet nozzle is fixedly arranged at one end of the inner sleeve, the water outlet nozzle is located outside the inner sleeve, a gap exists between the water outlet nozzle and the inner sleeve, the outer sleeve is sleeved outside the inner sleeve, the inner sleeve is made of transparent materials, and an ultraviolet lamp is arranged between the inner sleeve and the outer sleeve.
3. An integrated assembled water treatment device as defined in claim 2 wherein the inner sleeve is trumpet-shaped, the water outlet nozzle is located at one side of the narrow end of the inner sleeve, and the outer sleeve is truncated cone-shaped.
4. An integrated assembly water treatment device as claimed in claim 3 wherein the narrow end of the inner sleeve is provided with a funnel-shaped arcuate surface.
5. An integrated assembled water treatment apparatus as claimed in claim 1, wherein the denitrification tank is connected with a vacuum pump through a pipeline.
6. An integrated assembly water treatment apparatus as claimed in claim 1 wherein said dip tube is a ceramic dip tube.
CN202111181301.5A 2021-10-11 2021-10-11 Integrated assembly type water treatment equipment Active CN113816565B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN202310172777.5A CN116282678A (en) 2021-10-11 2021-10-11 Integrated assembly type sewage nitrogen and sand removal equipment
CN202111181301.5A CN113816565B (en) 2021-10-11 2021-10-11 Integrated assembly type water treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202111181301.5A CN113816565B (en) 2021-10-11 2021-10-11 Integrated assembly type water treatment equipment

Related Child Applications (1)

Application Number Title Priority Date Filing Date
CN202310172777.5A Division CN116282678A (en) 2021-10-11 2021-10-11 Integrated assembly type sewage nitrogen and sand removal equipment

Publications (2)

Publication Number Publication Date
CN113816565A CN113816565A (en) 2021-12-21
CN113816565B true CN113816565B (en) 2023-04-07

Family

ID=78920273

Family Applications (2)

Application Number Title Priority Date Filing Date
CN202310172777.5A Pending CN116282678A (en) 2021-10-11 2021-10-11 Integrated assembly type sewage nitrogen and sand removal equipment
CN202111181301.5A Active CN113816565B (en) 2021-10-11 2021-10-11 Integrated assembly type water treatment equipment

Family Applications Before (1)

Application Number Title Priority Date Filing Date
CN202310172777.5A Pending CN116282678A (en) 2021-10-11 2021-10-11 Integrated assembly type sewage nitrogen and sand removal equipment

Country Status (1)

Country Link
CN (2) CN116282678A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116986776B (en) * 2023-09-27 2023-12-08 上海朗蔚环保科技有限公司 High-efficiency anaerobic denitrification reactor for removing high-concentration nitrate nitrogen

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08303680A (en) * 1995-05-08 1996-11-22 Migaku Hanno City water hose coupling part inserting type impurity removing device
CN201400627Y (en) * 2009-02-27 2010-02-10 丁晓 All-in-one water processing device
US20150136671A1 (en) * 2012-05-30 2015-05-21 Ronald L. Barnes Sanitizer system
US10293310B2 (en) * 2016-11-14 2019-05-21 Innovative Water Care, Llc Apparatus and method of forming a chemical solution
CN111283970A (en) * 2020-04-02 2020-06-16 绍兴市思德龙热流道有限公司 Insert and hot runner system are adjusted to hot runner flow and stream length
CN113045125A (en) * 2021-03-19 2021-06-29 净化控股集团股份有限公司 High standard combined sewage treatment device

Also Published As

Publication number Publication date
CN116282678A (en) 2023-06-23
CN113816565A (en) 2021-12-21

Similar Documents

Publication Publication Date Title
CN102225803B (en) Biomembrane reactor, waste water treating system and method for treating waste water
CN109574392A (en) A kind of integrated apparatus and method purifying black-odor riverway sewage
KR102170601B1 (en) Advanced sewage and wastewater separation membrane device using low temperature plasma
CN109231435A (en) A kind of integration reinforcing aerobic granule sludge membrane bioreactor system
CN113816565B (en) Integrated assembly type water treatment equipment
CN109399793A (en) A kind of precipitating filter back-flush reinforcing mud-water separation integrated water treatment equipment
BG66054B1 (en) Sewage treatment plant
CN204369736U (en) Samll cities and towns' integration Water feeding treatment device
CN201785288U (en) Treatment system for treating inferior V-class surface water into domestic drinking water
CN205676326U (en) A kind of integrated sewage disposal intermediate filtered bioreactor
CN201161964Y (en) Integral water purifying device for slight-pollution water
CN210438573U (en) Stifled oxygenation type constructed wetland system of inhibiting
CN208802966U (en) A kind of waterworks water purification installation
CN111747605A (en) Multistage physicochemical-biochemical combined domestic sewage treatment system and treatment method
CN110720420A (en) Take water farming systems of anaerobism denitrification facility
CN212065388U (en) Device for purifying suspended particles in flowing water aquaculture water body
CN214880939U (en) Formaldehyde-containing wastewater purifying equipment
CN213141734U (en) Domestic sewage treatment system combining multistage physicochemical and biochemical treatment
CN212425789U (en) Domestic sewage treatment device
CN211394142U (en) Drinking water treatment device
CN205367866U (en) Aeration biological filter
CN209412045U (en) Efficient BMR sewage-treatment plant
CN215365377U (en) Plant oxidation pond system for livestock and poultry breeding wastewater treatment
CN108706838A (en) Medical waste water zero discharge treatment device and method
CN210286896U (en) Medical treatment sewage treatment membrane jar and sewage treatment system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant