CN112340823A - Wastewater treatment device and treatment method thereof - Google Patents

Wastewater treatment device and treatment method thereof Download PDF

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Publication number
CN112340823A
CN112340823A CN202011166457.1A CN202011166457A CN112340823A CN 112340823 A CN112340823 A CN 112340823A CN 202011166457 A CN202011166457 A CN 202011166457A CN 112340823 A CN112340823 A CN 112340823A
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CN
China
Prior art keywords
wastewater treatment
sewage
pressure gas
fixedly connected
breather pipe
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Granted
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CN202011166457.1A
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Chinese (zh)
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CN112340823B (en
Inventor
李宇
杨骏
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Sichuan University of Science and Engineering
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Beijing Dunyi Technology Co ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5281Installations for water purification using chemical agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
    • C02F2201/004Seals, connections
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/14Maintenance of water treatment installations
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/26Reducing the size of particles, liquid droplets or bubbles, e.g. by crushing, grinding, spraying, creation of microbubbles or nanobubbles

Abstract

The invention discloses a wastewater treatment device and a treatment method thereof, belonging to the field of production wastewater treatment devices, and the wastewater treatment device and the treatment method thereof are characterized in that high-pressure gas is continuously introduced into sewage, the high-pressure gas passes through a foaming net before entering the sewage and is split into a plurality of tiny bubbles under the action of the foaming net, the bubbles are broken due to pressure reduction in the floating process, the instant explosion formed by the breaking can generate great instant energy, which is beneficial to the combination of organic matters in the sewage and a flocculating agent to generate a flocculating agent and accelerate the speed of flocculating agent treatment, meanwhile, reinforcing fibers are doped into the high-pressure gas to ensure that the reinforcing fibers can be dissolved into the bubbles, and the instant high energy generated at the instant of the breaking of the bubbles can enable the reinforcing fibers to be ejected out to be combined with the flocculating agent in a contact manner, so as to increase the bonding strength of the structure in the flocculating agent, the subsequent cleaning and recovery work is convenient.

Description

Wastewater treatment device and treatment method thereof
Technical Field
The invention relates to the field of resin production wastewater treatment devices, in particular to a wastewater treatment device and a treatment method thereof.
Background
The ink resin is a carrier of the pigment in the ink, is a core material of the ink, and the quality of the ink resin directly influences the performance of the ink, because the binder determines the viscosity, the drying property, the fluidity and other properties of the ink to a great extent.
The adhesion force generated between the ink and the printing stock mainly comprises chemical bond force (i.e. interatomic force), intermolecular force (hydrogen bond force and Vanderwaals force), interface electrostatic attraction force and mechanical force. The primary source of these forces is the interaction between the resin binder for the ink and the substrate. The selection of proper resin connecting materials is also critical for different base materials, generally speaking, for nonpolar base materials such as PE, PP and the like, the surface tension can only reach about 38 dynes even if the corona surface treatment is carried out, and the resin connecting materials such as chlorinated polypropylene resin connecting materials with nonpolar resin structures are adopted; for the surface polar substrate such as PET and PA, a polyurethane resin binder can be used. The polyurethane ink binder system can solve the problem of adhesion on a nonpolar base material by adding a small amount of adhesion promoters specially used for PP and PE or combining a small amount of chlorinated polypropylene resin with polyurethane resin, and can achieve the problem of universality of a resin binder.
Although the resin is at the adhesion force problem of the printing ink on nonpolar substrate that solves to a certain extent, this also causes the stickness of printing ink too big, in the in-process of resin printing ink production, it bonds on positions such as storage jar and conveyer pipe very easily to cause the printing ink, influence going on of production, need shut down the clearance, and in the in-process of clearance produce a large amount of waste water that is rich in organic matter very easily, need handle the back and just can discharge in nature, current processing method roughly can divide into the preliminary sedimentation, utilize the flocculating agent to precipitate, utilize activated sludge to carry out final processing to remaining organic matter in the sewage at last, wherein, it is comparatively slow to utilize the flocculating agent to carry out the processing procedure, though utilize the stirring machine to stir can effectively promote reaction rate, but the promotion effect is limited.
Disclosure of Invention
1. Technical problem to be solved
The technical scheme is that the device is used for treating sewage by using a flocculating agent in a resin printing ink sewage treatment process, in the treatment process, a vent pipe continuously fills gas into a cleaning tank body through a gas pump connected with the vent pipe, when the gas enters the sewage in the cleaning tank body through a gas outlet and a foaming net, a plurality of bubbles can be formed due to the function of the foaming net, the bubbles can be broken due to the pressure reduction in the floating process, and the instantaneous explosion formed by the breaking can generate great instantaneous energy, so that organic matters in the sewage and the flocculating agent are combined to generate flocculating agents, and the speed of flocculating agent treatment is accelerated.
2. Technical scheme
In order to solve the above problems, the present invention adopts the following technical solutions.
The utility model provides a waste water treatment device and processing method thereof, includes the clearance jar body, the opening part fixedly connected with of the clearance jar body and self assorted sealed lid, it has the breather pipe to peg graft on the sealed lid, the one end of breather pipe runs through sealed lid and extends to the clearance jar internal, the breather pipe is located the one end port department of the internal clearance jar of clearance jar and is the enclosed segment, it has a plurality of evenly distributed's venthole to cut on the lateral wall of breather pipe, the venthole is located the one side that is close to the enclosed end, the interior fixedly connected with of venthole and self assorted foaming net, foaming net is close to the outer wall of venthole, sliding connection has the sealed piston with self assorted in the breather pipe, the lateral wall of sealed piston cuts has the annular groove, fixedly connected with washs the fibre cluster in the annular groove, it includes a plurality of elastic fiber to wash the fibre cluster, and a plurality of elastic fiber, it is a plurality of elastic fiber presents the trend of shrink under the restraint of breather pipe, the blind end fixedly connected with toper compression spring of sealing piston and breather pipe, this scheme device is arranged in the stage that utilizes the flocculating agent to handle sewage among the resin printing ink sewage treatment process, in the course of the treatment, the breather pipe is through the continuous gassing of air pump to the internal source of clearance jar that is connected with self, gas is when getting into the internal sewage of clearance jar through venthole and foaming net, because the effect of playing the foaming net can form a plurality of bubbles, the bubble can break because pressure reduction's reason can take place at the in-process of come-up, the instantaneous explosion that the fracture formed can produce very big instantaneous energy, organic matter and flocculating agent that help in the sewage combine to generate the flocculating agent, the speed that the flocculating agent was handled with higher speed.
Further, the breather pipe is when letting in high-pressure gas, mixes the reinforcing fiber in high-pressure gas, reinforcing fiber's length is no longer than 1 millimeter, and reinforcing fiber can form the bubble along with high-pressure gas and get into the production sewage of the clearance jar body, and in the bubble explosion process, reinforcing fiber easily produces great kinetic energy, makes the reinforcing fiber insert in the flocculating constituent that is growing, increases the bonding strength of flocculating constituent structure, makes things convenient for subsequent clearance and recovery work.
Furthermore, the reinforced fiber is in a three-dimensional spiral shape, the reinforced fiber is made of a high-elasticity material, and the three-dimensional spiral reinforced fiber can provide enough three-dimensional space for the growth of the flocculating constituent, so that the strength of the flocculating constituent after growth is greatly increased.
Further, toper compression spring is the back taper, the closed section of breather pipe be with toper compression spring assorted arcwall face for toper compression spring is difficult for taking place the non-work because of exogenic action and to deformation, is difficult for causing toper compression spring to become invalid.
Furthermore, the one end that conical compression spring was kept away from to sealed piston is the cambered surface of caving in, the cross-section of venthole is nearly trapezoidal wide in the interior narrow outward, and the venthole is close to the one end lateral wall interval of venthole inner wall great, and the shape of sealed piston and venthole all has certain guide effect in fact, avoids the venthole to carry high-pressure gas to cause excessive wearing and tearing to sealed piston and venthole, is difficult for causing sealed piston and venthole to become invalid.
Further, the lower extreme fixedly connected with vortex device of breather pipe, vortex device includes the spoiler, evenly cut out the vortex hole on the spoiler, the downside of spoiler is equipped with the contact plate, fixedly connected with cylindricality compression spring between spoiler and the contact plate, the upper end fixedly connected with a pair of connecting rod of spoiler, the one end that the spoiler was kept away from to the connecting rod runs through sealed lid and extends to the upside of sealed lid, a plurality of the upper end fixedly connected with atress ring of connecting rod, the atress ring cup joints in the outside of breather pipe, be equipped with the bellows with self assorted in the breather pipe, the both ends of bellows all with breather pipe fixed connection, when the internal reaction of clearance jar is slower, can realize promoting the spoiler through pressing the atress ring, and when the spoiler is in the internal motion of sewage, because the hole that self chiseling can cause sewage to take place comparatively obvious stirring, the growth of the floccule is accelerated.
Furthermore, the telescopic link is spliced in the cylindricality compression spring, the both ends of telescopic link respectively with spoiler and contact plate fixed connection, the telescopic link can effectively protect cylindricality compression spring for cylindricality compression spring is difficult for taking place the non-work under the effect of spoiler to deformation, is difficult for causing cylindricality compression spring inefficacy.
Further, sealed lid is connected with the sealing ring with the breather pipe, sealing ring and sealed lid fixed connection, be interference fit between breather pipe and the sealing ring for the breather pipe can be hung and connect on sealed covering, makes the breather pipe be difficult for taking place the structure collapse because of the dead weight, is difficult for influencing waste water treatment device's normal use.
Further, be connected with sealed the pad between the clearance jar body and the sealed lid, sealed pad and sealed fixed connection that covers, sealed pad chooses for use elastic rubber to make, effectively alleviates the vibrations that produce when the breather pipe fills high-pressure gas, is difficult for influencing the holistic stability of the clearance jar body and closing cap because of the normal work of breather pipe.
Furthermore, a treatment method of a wastewater treatment device, high-pressure gas is continuously introduced into the sewage to be treated in a cleaning tank body through a vent pipe, the high-pressure gas passes through a foaming net before entering the sewage, the high-pressure gas flow is split under the action of the foaming net, a plurality of tiny bubbles are formed after entering the sewage, the bubbles are broken due to the pressure reduction in the floating process, the instant explosion formed by the breaking can generate great instant energy, which is beneficial to the combination of organic matters in the sewage and a flocculating agent to generate a flocculating agent and accelerate the speed of flocculating agent treatment, meanwhile, reinforcing fibers can be doped into the high-pressure gas to dissolve the reinforcing fibers into the bubbles, and the instant high energy generated at the instant of the breaking of the bubbles can enable the reinforcing fibers to be ejected out to be combined with the flocculating agent in a contact manner to form a flocculating agent framework, so as to increase the bonding strength of the flocculating agent structure, convenient subsequent clearance and recovery work can realize manually stirring work to sewage through the vortex device simultaneously, promotes going on of flocculation work.
3. Advantageous effects
Compared with the prior art, the invention has the advantages that:
the scheme continuously introduces high-pressure gas into the sewage, the high-pressure gas passes through the foaming net before entering the sewage, and the bubbles are split into a plurality of tiny bubbles under the action of the foam net, the bubbles can be broken due to the pressure reduction in the floating process, the instant explosion formed by the breaking can generate great instant energy, which is helpful for combining organic matters in the sewage with the flocculating agent to generate flocculating constituents and accelerating the speed of the flocculating agent treatment, meanwhile, the reinforcing fibers are mixed in high-pressure gas, so that the reinforcing fibers can be dissolved in the bubbles, the instantaneous high energy generated at the moment of bubble rupture can eject the reinforced fiber out to be combined with the flocculating constituent, thereby increasing the bonding strength of the structure in the flocculating constituent, facilitating the subsequent cleaning and recovery work, meanwhile, manual stirring work for sewage can be realized through the turbulence device, and the flocculation work is promoted.
Drawings
FIG. 1 is an exploded view of the main structure of a wastewater treatment apparatus of the present invention;
FIG. 2 is a schematic view showing the construction of a wastewater treatment apparatus according to the present invention;
FIG. 3 is a front sectional view of a wastewater treatment plant according to the invention in normal operation;
FIG. 4 is a schematic view of the structure at A in FIG. 3;
FIG. 5 is a front sectional view of the wastewater treatment apparatus of the present invention in standby state
FIG. 6 is a schematic view of the sealing piston structure of the present invention;
FIG. 7 is a schematic structural diagram of a flow perturbation device of the present invention;
fig. 8 is a top cross-sectional view of a snorkel of the present invention at an air outlet.
The reference numbers in the figures illustrate:
the device comprises a cleaning tank body 1, a sealing cover 2, a sealing gasket 3, a vent pipe 4, a corrugated pipe 5, a sealing piston 6, a cleaning fiber cluster 7, a conical compression spring 8, an air outlet hole 9, a spoiler 10, a turbulent flow hole 11, a telescopic rod 12, a contact plate 13, a cylindrical compression spring 14, a connecting rod 15, a stress ring 16, a sealing ring 17 and a foaming net 18.
Detailed Description
The technical solution in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention; it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments, and all other embodiments obtained by those skilled in the art without any inventive work are within the scope of the present invention.
In the description of the present invention, it should be noted that the terms "upper", "lower", "inner", "outer", "top/bottom", and the like indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the referred device or element must have a specific orientation, be constructed in a specific orientation, and be operated, and thus should not be construed as limiting the present invention. Furthermore, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it should be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "disposed," "sleeved/connected," "connected," and the like are to be construed broadly, e.g., "connected," which may be fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
Example 1:
referring to fig. 1-4, 6 and 8, a wastewater treatment device comprises a cleaning tank body 1, a sealing cover 2 matched with the cleaning tank body is fixedly connected to an opening of the cleaning tank body 1, a vent pipe 4 is inserted into the sealing cover 2, one end of the vent pipe 4 penetrates through the sealing cover 2 and extends into the cleaning tank body 1, a port of the vent pipe 4, which is located in the cleaning tank body 1, is a closed section, a plurality of uniformly distributed vent holes 9 are drilled in a side wall of the vent pipe 4, the vent holes 9 are located at one side close to the closed end, a foaming net 18 matched with the vent pipe 4 is fixedly connected in the vent holes 9, the foaming net 18 is close to the outer wall of the vent holes 9, a sealing piston 6 matched with the vent pipe 4 is slidably connected in the vent pipe 4, an annular groove is drilled in the side wall of the sealing piston 6, a cleaning fiber cluster 7 is fixedly connected in the annular groove, the cleaning fiber, the elastic fibers are distributed in a staggered mode, the elastic fibers tend to shrink under the constraint of the vent pipe 4, the sealing piston 6 and the closed end of the vent pipe 4 are fixedly connected with the conical compression spring 8, and particularly, when high-pressure gas is not introduced into the vent pipe 4, the sealing piston and the cleaning fiber cluster 7 can be pushed to the upper side of the air outlet hole shown in fig. 5 under the action of the conical compression spring 8.
Specially, the demonstration is just used a sewage treatment plant to the jar shape to the clearance jar body 1 in this scheme, sealed lid 2 and sealed pad 3, in the actual production, the technical staff can carry out reasonable design according to the actual production process and the on-the-spot condition in production place, the one end that closed end was kept away from to breather pipe 4 is linked together with high-pressure air pump in addition, deposit the sewage that produces in the resin printing ink production process in the clearance jar body 1, and technical staff carries out pH regulation and drops into the flocculating agent according to actual conditions in the sewage, the flocculating agent is ferrous sulfate usually.
This scheme device is arranged in the stage that utilizes the flocculating agent to handle sewage among the resin printing ink sewage treatment process, in the course of the treatment, breather pipe 4 is through the air pump that is connected with self to the continuous gassing of the internal source of the clearance jar 1, gas is when getting into the sewage of the internal 1 of clearance jar through venthole 9 and foaming net 18, because the effect that plays foaming net 18 can form a plurality of bubbles, the bubble can take place to break owing to pressure reduction's reason at the in-process of come-up, the explosion in the twinkling of an eye that the formation that breaks can produce very big instantaneous energy, help organic matter and flocculating agent in the sewage to combine to generate the flocculating agent, the speed of flocculating agent processing accelerates.
The breather pipe 4 is when letting in high-pressure gas, the reinforcing fiber is doped in high-pressure gas, reinforcing fiber's length is no longer than 1 millimeter, reinforcing fiber can form the bubble along with high-pressure gas and get into the production sewage of the clearance jar body 1, in the bubble explosion process, reinforcing fiber easily produces great kinetic energy, impel reinforcing fiber to insert in the flocculating constituent that is growing, increase the bonding strength of flocculating constituent internal structure, make things convenient for subsequent clearance and recovery work, reinforcing fiber is the three-dimensional heliciform, reinforcing fiber chooses high elastic material for use and makes, the reinforcing fiber of three-dimensional heliciform can provide sufficient cubical space for the growth of flocculating constituent, the intensity after the flocculating constituent grows up is greatly increased.
Wherein the sealing piston 6 and the cleaning fiber cluster 7 are mainly used for cleaning floccules and reinforcing fibers adhered on the foaming net 18, when the closed end of the vent pipe 4 is inserted into sewage, please refer to fig. 5, due to the action of the conical compression spring 8, the sealing piston 6 and the cleaning fiber cluster 7 are pushed against the upper side of the air outlet 9, the phenomenon that the sewage flows back along the backflow direction of the vent pipe 4 can not occur, when the device of the scheme normally works, under the action of high-pressure gas, the sealing piston 6 and the cleaning fiber cluster 7 compress the conical compression spring 8 to the position shown by 3-4, at the moment, the high-pressure gas can be ejected from the foaming net 18, and when the foaming net 18 is blocked by the floccules or the reinforcing fibers, the high-pressure gas ejected by the vent pipe 4 is blocked and becomes larger, at the moment, under the combined action of frequently opening and closing the high-pressure gas pump and the conical compression spring 8 in the compression state, so that the sealing piston 6 and the cleaning fiber cluster 7 reciprocate in the range of the air outlet 9 to clean the foaming net 18.
Referring to fig. 4, 6 and 7, the conical compression spring 8 is in an inverted cone shape, the closed section of the vent pipe 4 is an arc-shaped surface matched with the conical compression spring 8, so that the conical compression spring 8 is not prone to non-working deformation due to external force, and the conical compression spring 8 is not prone to failure, the end, away from the conical compression spring 8, of the sealing piston 6 is an inward-concave arc surface, the cross section of the vent hole 9 is nearly trapezoidal, with the inner width being large and the outer width being small, and the distance between the side walls of the end, close to the inner wall of the vent pipe 4, of the vent hole 9 is large, the shapes of the sealing piston 6 and the vent hole 9 actually have a certain guiding function, excessive wear of the sealing piston 6 and the vent hole 9 caused by high-pressure gas output by the vent pipe 4 is avoided.
Referring to fig. 3 and 7, a spoiler device is fixedly connected to a lower end of the vent pipe 4, the spoiler device includes a spoiler 10, spoiler holes 11 are uniformly drilled in the spoiler 10, a contact plate 13 is disposed on a lower side of the spoiler 10, a cylindrical compression spring 14 is fixedly connected between the spoiler 10 and the contact plate 13, a pair of connecting rods 15 is fixedly connected to an upper end of the spoiler 10, one end of each connecting rod 15, which is far away from the spoiler 10, penetrates through the sealing cover 2 and extends to an upper side of the sealing cover 2, stress rings 16 are fixedly connected to upper ends of the connecting rods 15, the stress rings 16 are sleeved on outer sides of the vent pipe 4, a corrugated pipe 5 matched with the connector is disposed in the vent pipe 4, i.e., a portion of the vent pipe 4 is replaced by the corrugated pipe 5, both ends of the corrugated pipe 5 are fixedly connected to the vent pipe 4, when the reaction in the tank body 1 is, when the spoiler 10 moves in sewage, the spoiler holes 11 dug by the spoiler 10 can cause the sewage to generate obvious stirring, the growth of floccules is accelerated, the telescopic rod 12 is inserted in the cylindrical compression spring 14, two ends of the telescopic rod 12 are respectively fixedly connected with the spoiler 10 and the contact plate 13, and the telescopic rod 12 can effectively protect the cylindrical compression spring 14, so that the cylindrical compression spring 14 is not easy to deform in a non-working direction under the action of the spoiler 10, and the cylindrical compression spring 14 is not easy to fail.
Specially, the vortex device in this scheme can utilize hydraulic means to drive, and technical personnel in the field can carry out reasonable design to its overall arrangement according to prior art can for it is great to deal with the clearance jar body 1, the great problem of the required strength of drive vortex device.
Cut on the sealed lid 2 and have the air vent, the one end of connecting rod 15 runs through the air vent, the diameter of air vent is greater than the 15 diameters of connecting rod, fill the high-pressure gas in the clearance jar body 1 into by breather pipe 4 and can discharge through the air vent and clear up jar body 1 in, be difficult for forming the high pressure in the clearance jar body 1, the difficult clearance jar body 1 accident that bursts that takes place, be connected with sealed the pad 3 between the clearance jar body 1 and the sealed lid 2, sealed pad 3 and sealed 2 fixed connection of covering, sealed pad 3 chooses for use elastic rubber to make, effectively alleviate the vibrations that produce when breather pipe 4 fills high-pressure gas, be difficult for influencing the clearance jar body 1 and the holistic stability of closing cap.
Sealed lid 2 is connected with sealing ring 17 with breather pipe 4, and sealing ring 17 and sealed 2 fixed connection of lid are interference fit between breather pipe 4 and the sealing ring 17 for breather pipe 4 can be hung and connect on sealed lid 2, makes breather pipe 4 be difficult for taking place the structure breakdown because of the dead weight, is difficult for influencing waste water treatment device's normal use.
This scheme passes through breather pipe 4 and continues lets in high-pressure gas to the pending sewage in the cleaning tank body 1, high-pressure gas can pass through bubble net 18 earlier before getting into sewage, and under the effect of bubble net 18, the high-pressure gas stream splits, form a plurality of tiny bubbles behind the entering sewage, and the bubble can break because of pressure reduction's reason in the in-process of come-up, the instantaneous explosion that the fracture formed can produce very big instantaneous energy, organic matter and flocculating agent in the sewage combine and generate the flocculating constituent, the speed of flocculating constituent processing is accelerated, it can make in the above-mentioned bubble that the reinforcing fiber can be dissolved to mix simultaneously in high-pressure gas, and the instantaneous high energy that produces in the moment of bubble fracture can make the reinforcing fiber launch out and contact combination with the flocculating constituent, become the flocculating constituent skeleton, increase the bonding strength of flocculating constituent structure, make things convenient for subsequent clearance and recovery work, meanwhile, manual stirring work for sewage can be realized through the turbulence device, and the flocculation work is promoted.
The foregoing is only a preferred embodiment of the present invention; the scope of the invention is not limited thereto. Any person skilled in the art should be able to cover the technical scope of the present invention by equivalent or modified solutions and modifications within the technical scope of the present invention.

Claims (10)

1. The utility model provides a wastewater treatment device, includes the clearance jar body (1), its characterized in that: the opening part fixedly connected with of the clearance jar body (1) and self assorted sealed lid (2), it has breather pipe (4) to peg graft on sealed lid (2), the one end of breather pipe (4) runs through sealed lid (2) and extends to the clearance jar body (1) in, one end port department that breather pipe (4) are located the clearance jar body (1) is the enclosed segment, dig venthole (9) that have a plurality of evenly distributed on the lateral wall of breather pipe (4), venthole (9) are located the one side that is close to the enclosed end, the internal fixedly connected with of venthole (9) and self assorted foaming net (18), foaming net (18) are close to the outer wall of venthole (9), sliding connection has with self assorted sealed piston (6) in breather pipe (4), the lateral wall of sealed piston (6) is dug annular groove, fixedly connected with washs fibre cluster (7) in the ring channel, it includes a plurality of elastic fiber to wash fibre cluster (7), and is a plurality of elastic fiber is the staggered distribution, and is a plurality of elastic fiber presents the trend of shrink under the restraint of breather pipe (4), sealed piston (6) and blind end fixedly connected with toper compression spring (8) of breather pipe (4).
2. A wastewater treatment plant according to claim 1, characterized in that: when high-pressure gas is introduced into the ventilating pipe (4), the high-pressure gas is doped with the reinforced fibers, the length of the reinforced fibers is not more than 1 mm, and the reinforced fibers can form bubbles along with the high-pressure gas and enter the production sewage of the cleaning tank body (1).
3. A wastewater treatment plant according to claim 2, characterized in that: the reinforced fiber is in a three-dimensional spiral shape and is made of a high-elasticity material.
4. A wastewater treatment plant according to claim 1, characterized in that: the conical compression spring (8) is in an inverted cone shape, and the closed section of the vent pipe (4) is an arc-shaped surface matched with the conical compression spring (8).
5. A wastewater treatment plant according to claim 1, characterized in that: one end, far away from the conical compression spring (8), of the sealing piston (6) is an inward-sunken cambered surface, the cross section of the air outlet hole (9) is nearly trapezoidal with an inner width and an outer width, and the distance between the side walls of one end, close to the inner wall of the vent pipe (4), of the air outlet hole (9) is large.
6. A wastewater treatment plant according to claim 1, characterized in that: the lower end of the vent pipe (4) is fixedly connected with a turbulence device which comprises a turbulence plate (10), turbulent flow holes (11) are uniformly drilled on the spoiler (10), a contact plate (13) is arranged at the lower side of the spoiler (10), a cylindrical compression spring (14) is fixedly connected between the spoiler (10) and the contact plate (13), the upper end of the spoiler (10) is fixedly connected with a pair of connecting rods (15), one end of the connecting rod (15) far away from the spoiler (10) penetrates through the sealing cover (2) and extends to the upper side of the sealing cover (2), the upper ends of the connecting rods (15) are fixedly connected with stress rings (16), the stress ring (16) is sleeved outside the vent pipe (4), the vent pipe (4) is internally provided with a corrugated pipe (5) matched with the stress ring, both ends of the corrugated pipe (5) are fixedly connected with the vent pipe (4).
7. The wastewater treatment apparatus according to claim 6, characterized in that: an expansion rod (12) is inserted in the cylindrical compression spring (14), and two ends of the expansion rod (12) are respectively and fixedly connected with the spoiler (10) and the contact plate (13).
8. A wastewater treatment plant according to claim 1, characterized in that: sealing cover (2) are connected with sealing ring (17) with breather pipe (4), sealing ring (17) and sealing cover (2) fixed connection, be interference fit between breather pipe (4) and sealing ring (17).
9. A wastewater treatment plant according to claim 1, characterized in that: be connected with sealed pad (3) between the clearance jar body (1) and sealed lid (2), sealed pad (3) and sealed lid (2) fixed connection, sealed pad (3) select for use elastic rubber to make.
10. The use method of the wastewater treatment device according to claim 1: utilize breather pipe (4) to continuously let in high-pressure gas to the pending sewage in the cleaning tank body (1), high-pressure gas can pass through bubble net (18) earlier before getting into the sewage, and under the effect of bubble net (18), high-pressure gas splits, form a plurality of small bubbles behind the entering sewage, and the bubble can break because reasons such as pressure reduction can take place for the in-process of come-up, the instant explosion that the fracture formed can produce very big instantaneous energy, it combines to generate the flocculating constituent to help organic matter and flocculating agent in the sewage, it can make in the above-mentioned bubble that reinforcing fiber can be dissolved to mix reinforcing fiber in high-pressure gas simultaneously, and the high energy in the twinkling of an eye that the bubble broke produces can make reinforcing fiber launch out and flocculating constituent contact combination, become the flocculating constituent skeleton.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113105778A (en) * 2021-04-14 2021-07-13 徐鹏 Efficient preparation process of thickening agent

Citations (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2943870A1 (en) * 1979-10-30 1981-06-11 Universal Gesellschaft zur Errichtung von Umweltschutzanlagen mbH & Co, 2410 Mölln Sewage clarification - in two flock(s) precipitation stages by injecting calcium salt and iron salt in aeration up draught
CN1060453A (en) * 1990-08-27 1992-04-22 纽卡斯尔大学研究公司 The aeration of liquid
DE4143107A1 (en) * 1991-12-24 1993-07-01 Amon Hermann Dr Ing Chemical treatment of liq(s). esp. contaminated waters - comprises intimately mixing with liq. or gaseous reagent, pressure is then increased, liq. is mixed with body of untreated liq.
CN1254686A (en) * 1998-11-24 2000-05-31 梁维安 Vortex equipment for treating sewage
CN201065378Y (en) * 2007-07-27 2008-05-28 北京天灏柯润环境科技有限公司 Treatment device for caustic sludge waste water
CN101284703A (en) * 2008-04-29 2008-10-15 陈焕龙 Highly effective waste water treating method and special equipment for the treatment
CN101693580A (en) * 2009-10-16 2010-04-14 同济大学 Efficient compound biological treatment device
CN101774731A (en) * 2010-01-27 2010-07-14 四川大学 Enhanced coagulation-gas stripping-membrane integration method and device for lightening membrane pollution
CN101786712A (en) * 2010-03-05 2010-07-28 泉州师范学院 Anti-wave emergency restoration process for polluted natural water body
CN101786713A (en) * 2010-03-05 2010-07-28 泉州师范学院 Emergency restoring process for pollution of water body, substrate sludge and mud flat by heavy metal
CN204310835U (en) * 2014-12-04 2015-05-06 南京市环境保护科学研究院 Utilize the sewage defoaming device of high-voltage power supply
CN106186638A (en) * 2016-07-28 2016-12-07 上海交通大学 The method of microbubble/flocculant coupling and intensifying dewatering performance of sludge
CN108557981A (en) * 2018-01-31 2018-09-21 王志华 A kind of micro-nano bubble water treatment facilities
CN208054996U (en) * 2018-03-14 2018-11-06 乾坤环保股份有限公司 Flocculation clarification sewage disposal device
CN208151138U (en) * 2018-04-06 2018-11-27 泉州顺鑫餐饮有限公司 A kind of green building water treatment facilities
CN208327490U (en) * 2018-04-17 2019-01-04 云南嘉科环保设备有限公司 Flocculant dosing blender
CN110723794A (en) * 2019-11-05 2020-01-24 安吉起航环境工程有限公司 Advanced treatment system for urban sewage
CN210313684U (en) * 2019-04-25 2020-04-14 中国长城葡萄酒有限公司 Aeration tank for sewage treatment
CN111721597A (en) * 2020-05-18 2020-09-29 杨文先 Be used for quick detection device of food heavy metal composition

Patent Citations (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2943870A1 (en) * 1979-10-30 1981-06-11 Universal Gesellschaft zur Errichtung von Umweltschutzanlagen mbH & Co, 2410 Mölln Sewage clarification - in two flock(s) precipitation stages by injecting calcium salt and iron salt in aeration up draught
CN1060453A (en) * 1990-08-27 1992-04-22 纽卡斯尔大学研究公司 The aeration of liquid
DE4143107A1 (en) * 1991-12-24 1993-07-01 Amon Hermann Dr Ing Chemical treatment of liq(s). esp. contaminated waters - comprises intimately mixing with liq. or gaseous reagent, pressure is then increased, liq. is mixed with body of untreated liq.
CN1254686A (en) * 1998-11-24 2000-05-31 梁维安 Vortex equipment for treating sewage
CN201065378Y (en) * 2007-07-27 2008-05-28 北京天灏柯润环境科技有限公司 Treatment device for caustic sludge waste water
CN101284703A (en) * 2008-04-29 2008-10-15 陈焕龙 Highly effective waste water treating method and special equipment for the treatment
CN101693580A (en) * 2009-10-16 2010-04-14 同济大学 Efficient compound biological treatment device
CN101774731A (en) * 2010-01-27 2010-07-14 四川大学 Enhanced coagulation-gas stripping-membrane integration method and device for lightening membrane pollution
CN101786712A (en) * 2010-03-05 2010-07-28 泉州师范学院 Anti-wave emergency restoration process for polluted natural water body
CN101786713A (en) * 2010-03-05 2010-07-28 泉州师范学院 Emergency restoring process for pollution of water body, substrate sludge and mud flat by heavy metal
CN204310835U (en) * 2014-12-04 2015-05-06 南京市环境保护科学研究院 Utilize the sewage defoaming device of high-voltage power supply
CN106186638A (en) * 2016-07-28 2016-12-07 上海交通大学 The method of microbubble/flocculant coupling and intensifying dewatering performance of sludge
CN108557981A (en) * 2018-01-31 2018-09-21 王志华 A kind of micro-nano bubble water treatment facilities
CN208054996U (en) * 2018-03-14 2018-11-06 乾坤环保股份有限公司 Flocculation clarification sewage disposal device
CN208151138U (en) * 2018-04-06 2018-11-27 泉州顺鑫餐饮有限公司 A kind of green building water treatment facilities
CN208327490U (en) * 2018-04-17 2019-01-04 云南嘉科环保设备有限公司 Flocculant dosing blender
CN210313684U (en) * 2019-04-25 2020-04-14 中国长城葡萄酒有限公司 Aeration tank for sewage treatment
CN110723794A (en) * 2019-11-05 2020-01-24 安吉起航环境工程有限公司 Advanced treatment system for urban sewage
CN111721597A (en) * 2020-05-18 2020-09-29 杨文先 Be used for quick detection device of food heavy metal composition

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113105778A (en) * 2021-04-14 2021-07-13 徐鹏 Efficient preparation process of thickening agent

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