CN116282325A - Pesticide separation and extraction device in water - Google Patents
Pesticide separation and extraction device in water Download PDFInfo
- Publication number
- CN116282325A CN116282325A CN202310566644.6A CN202310566644A CN116282325A CN 116282325 A CN116282325 A CN 116282325A CN 202310566644 A CN202310566644 A CN 202310566644A CN 116282325 A CN116282325 A CN 116282325A
- Authority
- CN
- China
- Prior art keywords
- fixedly connected
- water
- crystallization
- shell
- separating
- 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.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 96
- 239000000575 pesticide Substances 0.000 title claims abstract description 32
- 238000000926 separation method Methods 0.000 title claims abstract description 29
- 238000000605 extraction Methods 0.000 title claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 69
- 238000002425 crystallisation Methods 0.000 claims abstract description 37
- 230000008025 crystallization Effects 0.000 claims abstract description 29
- 238000003756 stirring Methods 0.000 claims abstract description 15
- 239000003905 agrochemical Substances 0.000 claims abstract description 4
- 239000012535 impurity Substances 0.000 claims description 19
- 230000000087 stabilizing effect Effects 0.000 claims description 15
- 230000002265 prevention Effects 0.000 claims description 12
- 238000001802 infusion Methods 0.000 claims description 11
- 238000005119 centrifugation Methods 0.000 abstract description 7
- 238000004062 sedimentation Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 10
- 210000005056 cell body Anatomy 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 8
- 238000000151 deposition Methods 0.000 description 7
- 239000002351 wastewater Substances 0.000 description 7
- 239000007787 solid Substances 0.000 description 5
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000004615 ingredient Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000002195 synergetic effect Effects 0.000 description 3
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 2
- 235000017491 Bambusa tulda Nutrition 0.000 description 2
- 241001330002 Bambuseae Species 0.000 description 2
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 2
- 239000011425 bamboo Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005452 bending Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 150000002222 fluorine compounds Chemical class 0.000 description 1
- 150000002391 heterocyclic compounds Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
Images
Classifications
-
- 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
- C02F1/26—Treatment of water, waste water, or sewage by extraction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/50—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
- B01D29/56—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in series connection
-
- 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
- C02F1/02—Treatment of water, waste water, or sewage by heating
-
- 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
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
- C02F1/385—Treatment of water, waste water, or sewage by centrifugal separation by centrifuging suspensions
-
- 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
- C02F2101/30—Organic compounds
- C02F2101/306—Pesticides
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The invention discloses an agricultural chemical separating and extracting device in a water body, which relates to the technical field of centrifugal extraction and comprises an anti-sedimentation mechanism, wherein the anti-sedimentation mechanism is arranged in the middle of the inner side surface of an anti-crystallization mechanism and is used for stirring the water body to promote heavy liquid separation and throwing to a heat conducting shell, a first delivery pipe is fixedly connected to the upper position of the surface of the anti-crystallization mechanism, a second delivery pipe is fixedly connected to the position, close to the middle, of the top of the anti-crystallization mechanism, the first delivery pipe discharges heavy liquid, the second delivery pipe discharges light liquid, and the water body is conveyed into a tank body through a liquid inlet pipe. This pesticide separation extraction element in water, return bend are carried the conduction oil to the position that the jar body was kept away from to the water, and anti-deposition mechanism stirs the centrifugation to the water, and heavy liquid is discharged through first delivery tube, and the middle part position temperature of collection miscellaneous subassembly avoids the water is too low and crystallization causes the jam, has solved extractant or the inside composition crystallization speed of water and has accelerated the problem that leads to the drain channel to block up.
Description
Technical Field
The invention relates to the technical field of centrifugal extraction, in particular to a device for separating and extracting pesticides in a water body.
Background
In recent years, as the requirements on pesticides are higher and higher, the structure of a new variety of pesticides is more and more complex, a plurality of heterocyclic compounds, fluorine compounds and chiral compounds are introduced into the pesticide chemical structure, the structure of a pesticide intermediate is also complex, the manufacture of pesticides is more difficult and the quality requirement is higher, a large amount of organic wastewater is generated in the production process of the intermediate, pretreatment is needed, along with the maturity of the technology of treating phenol-containing wastewater by a centrifugal extractor, the phenol-containing wastewater is well applied by the centrifugal extractor in the pesticide intermediate, the phenol-containing wastewater in the pesticide intermediate manufacturing industry is treated by the centrifugal extractor, the centrifugal extractor is matched with a solvent extraction method for pretreatment of the organic wastewater, organic components in the wastewater are extracted by an extractant, COD is reduced, so that the pretreatment of the wastewater is realized, mixed liquid formed by mixing heavy phase and light phase enters a rotary drum, the mixed liquid and the rotary drum synchronously rotate at a high speed to generate centrifugal force, the heavy phase gradually moves away from the center of the rotary drum to the drum wall in an upward flow process under the centrifugal force effect, the light phase with the centrifugal force gradually moves away from the center of the drum, the light phase with the two phases gradually moves away from the center of the drum wall of the drum, and the two phases are separated from the center of the two phases respectively, and the two phases are separated from each other through respective two phase channels, and are separated from each other, and the two phase channels are collected.
The existing pesticide separation and extraction equipment has the problems that due to structural design defects, the crystallization speed of extractant or components in the water body is increased, so that a liquid discharge channel is blocked, and floccules in the water body are easily accumulated on the inner wall of a rotary drum, so that the liquid separation effect is poor.
Disclosure of Invention
The invention provides a device for separating and extracting pesticides in a water body, which solves the problems in the background technology.
In order to achieve the above purpose, the invention is realized by the following technical scheme: an agricultural chemical separating and extracting device in water body comprises
A base;
the crystallization prevention mechanism is arranged above the base, a liquid inlet pipe is fixedly connected to the middle part of the surface of the crystallization prevention mechanism, the liquid inlet pipe conveys water into the crystallization prevention mechanism, and heat conduction oil is added into the crystallization prevention mechanism to heat the water and stir the water; the device comprises a heat conduction shell, a stabilizing component and a impurity collecting component, wherein heat conduction oil is introduced into the heat conduction shell, the impurity collecting component is supported and fixed by the stabilizing component, and extends to a light liquid separation area to stir and collect impurities at a position, far away from the heat conduction shell, inside the device;
prevent depositing the mechanism, set up in the middle part position of preventing crystallization mechanism medial surface for stir the water, promote heavy liquid separation to get rid of and lead to the thermal shell, prevent the first delivery tube of upper position fixedly connected with on crystallization mechanism surface, prevent the position fixedly connected with second delivery tube that crystallization mechanism top is close to the middle part, first delivery tube discharges heavy liquid, second delivery tube discharges light liquid, and the water is carried to the jar body through the feed liquor pipe in, and the oil pump lets in the conduction oil after the heating to the inside of thermal shell, and the quantity of thermal shell is provided with a plurality ofly, heats the water through indirect heating's mode, effectively slows down the crystallization process of the ingredient in the water, avoids direct heating to lead to pesticide composition to decompose.
Preferably, the top fixedly connected with jar body of base, the medial surface of jar body is connected with the surface mounting of heat conduction shell, the surface mounting of heat conduction shell is connected with the oil pump, the surface mounting of heat conduction shell is connected with the return bend.
Preferably, the stabilizing component comprises a connecting sheet, the surface of the connecting sheet is fixedly connected with the inner side surface of the tank body, and the surface of the connecting sheet is fixedly connected with an infusion pump.
Preferably, the one end fixedly connected with casing that the connection piece was kept away from to the transfer pump, the fixed connection of position between casing and the transfer pump has the firm pole, the fixed surface of position and return bend between heat conduction shell and the transfer pump is connected, and the inside circulation of heat conduction shell flows there is the conduction oil by the heating, and the conduction oil passes through the heat conduction shell and carries out heat transfer with the water for the water is higher when the internal temperature of jar, and the return bend is with the conduction oil transport to the transfer pump in.
Preferably, the impurity collecting assembly comprises an assembly wall, the surface of the assembly wall is fixedly connected with the surface of the shell, and one side of the assembly wall is fixedly connected with a first net body.
Preferably, a second net body is fixedly connected to one side, far away from the first net body, of the assembly wall, a gap is formed in the surface of the assembly wall, and the aperture of the second net body is larger than that of the first net body.
Preferably, the anti-deposition mechanism comprises driving equipment, the bottom of the driving equipment is fixedly connected with the top of the tank body, and the output end of the driving equipment is fixedly connected with a centrifugal assembly.
Preferably, the bottom fixedly connected with turbine of centrifugation subassembly, the surface fixedly connected with of centrifugation subassembly increases the subassembly, the top fixedly connected with guide wall of jar internal side, drive equipment drive increases the subassembly and rotate, increases the subassembly and extrudees the heavy liquid to the position that is close to the jar body through centrifugal force, and the guide wall separates liquid, and light liquid discharges through the second delivery tube.
Preferably, the centrifugal assembly comprises a rod body, the top end of the rod body is fixedly connected with the output end of the driving device, and the bottom end of the rod body is fixedly connected with the top of the turbine.
Preferably, the fixed surface of the rod body is connected with an arc-shaped sheet, a fixed ring is fixedly connected to the position, close to the edge, of the surface of the arc-shaped sheet, the surface of the arc-shaped sheet is provided with a hole, the rod body is driven to rotate by driving equipment, the arc-shaped sheet is a plate with an arc-shaped section, and when the arc-shaped sheet rotates, heavier substances are centrifugally thrown out, and light liquid is extruded to a position, close to the rod body.
Preferably, the synergy component comprises a barrel, the medial surface of barrel passes through the fixed surface connection of connecting rod and body of rod, the below position on body of rod surface is through connecting rod fixedly connected with extension section of thick bamboo, and the inside of casing lets in the conduction oil for the casing heats light liquid, and the body of rod drives the arc piece and rotates, thereby stirs the water, and the clearance on component wall surface makes the arc piece can rotate and carries out the centrifugation to the water.
Preferably, the surface of the cylinder body is provided with a liquid through hole, a separation sheet is fixedly connected to the upper position of the surface of the cylinder body, and the surface of the stabilizing component extends to the inside of the cylinder body.
The invention provides a device for separating and extracting pesticides in a water body. The beneficial effects are as follows:
1. this pesticide separation extraction element in water, return bend are carried the conduction oil to the position that the jar body was kept away from to the water, and anti-deposition mechanism stirs the centrifugation to the water, and heavy liquid is discharged through first delivery tube, and the middle part position temperature of collection miscellaneous subassembly avoids the water is too low and crystallization causes the jam, has solved extractant or the inside composition crystallization speed of water and has accelerated the problem that leads to the drain channel to block up.
2. This pesticide separation extraction element in water, conduction oil circulate to the casing through the infusion pump, and the water separates gradually into light liquid district and heavy liquid district in the jar body, and the casing heats the light liquid district of water, and the subassembly wall is close to the middle part position of jar body, strikes the subassembly wall when rivers stir, and firm pole makes casing and subassembly wall can firm be connected, avoids being impacted by rivers to damage, heat transfer between casing and the water, avoids the water local temperature too low to lead to crystallization.
3. This pesticide separation extraction element in water, centrifugal component drives and increases the rotation of subassembly, firm subassembly runs through and increases the subassembly for collect miscellaneous subassembly and extend to light liquid separation district, when centrifugal component rotated, collect miscellaneous subassembly and centrifugal component relative rotation, collect miscellaneous subassembly and separate and collect the floccule in the water, the turbine throws the material of water bottom to the medial surface of jar body, thereby promotes the inside global flow of water, has solved the floccule in the water and has piled up easily at the rotary drum inner wall and cause the problem that liquid separation effect worsens.
4. This pesticide separation extraction element in water, trompil and turbine's rotation promote the water vertical direction flow to make the heavy, the light liquid separation effect of water better, heavy liquid is thrown away and is gathered at the medial surface of jar body behind the access hole, extends a section of thick bamboo and turbine and cooperates, makes the effect that liquid divides the liquid better, and the separation piece is close to first delivery tube, obstructs the water, makes the heavy liquid of separation in the water discharge through first delivery tube.
5. This pesticide separation extraction element in water, solid fixed ring is directed the flow direction of liquid for heavy liquid flow direction jar medial surface of body, the water flows through first cell body and second cell body in proper order, and the aperture of first cell body is great makes floccule and crystalline solid get into the subassembly wall, and the second cell body obstructs floccule and crystalline solid, thereby makes floccule and crystalline solid in the extraction process in the water collected, causes the jam when avoiding impurity entering delivery tube.
Drawings
FIG. 1 is a schematic diagram of the overall structure of a device for separating and extracting pesticides in a water body;
FIG. 2 is a schematic diagram of the structure of the inside of the pesticide separating and extracting device in the water body;
FIG. 3 is a schematic diagram of an anti-crystallization mechanism according to the present invention;
FIG. 4 is a schematic view of a stability assembly according to the present invention;
FIG. 5 is a schematic view of the structure of the impurity collecting unit of the present invention;
FIG. 6 is a schematic view of the deposition preventing mechanism of the present invention;
FIG. 7 is a schematic view of the structure of the centrifuge assembly of the present invention;
FIG. 8 is a schematic structural view of the synergistic assembly of the present invention.
In the figure: 1. a base; 2. an anti-crystallization mechanism; 21. a tank body; 22. a heat conductive shell; 23. an oil pump; 24. a stabilizing assembly; 241. a connecting sheet; 242. an infusion pump; 243. a stabilizing rod; 244. a housing; 25. bending the pipe; 26. a collection assembly; 261. a component wall; 262. a first net body; 263. a gap; 264. a second net body; 3. a liquid inlet pipe; 4. a first delivery tube; 5. an anti-deposition mechanism; 51. driving equipment; 52. a centrifuge assembly; 521. a rod body; 522. an arc-shaped sheet; 523. a fixing ring; 524. opening holes; 53. a turbine; 54. a synergy component; 541. a cylinder; 542. an extension cylinder; 543. a liquid through hole; 544. a blocking sheet; 55. a deflector wall; 6. and a second delivery tube.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
As shown in fig. 1-3, the present invention provides a technical solution: an agricultural chemical separating and extracting device in water body comprises
A base 1;
the crystallization prevention mechanism 2 is arranged above the base 1, the middle part of the surface of the crystallization prevention mechanism 2 is fixedly connected with the liquid inlet pipe 3, the liquid inlet pipe 3 conveys the water body into the crystallization prevention mechanism 2, and heat conduction oil is added into the crystallization prevention mechanism 2 to heat the water body and stir the water body; the device comprises a heat conducting shell 22, a stabilizing component 24 and a impurity collecting component 26, wherein heat conducting oil is introduced into the heat conducting shell 22, the impurity collecting component 26 is supported and fixed by the stabilizing component 24, the impurity collecting component 26 extends to a light liquid separation area, and the position, far away from the heat conducting shell 22, inside the device is stirred and impurities are collected;
the anti-sedimentation mechanism 5 is arranged in the middle of the inner side surface of the anti-crystallization mechanism 2 and is used for stirring a water body, promoting heavy liquid separation and throwing to the heat conduction shell 22, a first delivery pipe 4 is fixedly connected to the upper position of the surface of the anti-crystallization mechanism 2, a second delivery pipe 6 is fixedly connected to the position, close to the middle, of the top of the anti-crystallization mechanism 2, the first delivery pipe 4 discharges heavy liquid, and the second delivery pipe 6 discharges light liquid;
the top fixedly connected with jar body 21 of base 1, the medial surface of jar body 21 and the fixed surface of heat conduction shell 22 are connected, and the fixed surface of heat conduction shell 22 is connected with oil pump 23, and the fixed surface of heat conduction shell 22 is connected with return bend 25.
During the use, the water is carried to jar body 21 through feed liquor pipe 3, oil pump 23 lets in the conduction oil after the heating to the inside of heat conduction shell 22, the quantity of heat conduction shell 22 is provided with a plurality ofly, heat the water through indirect heating's mode, effectively slow down the crystallization process of ingredient in the water, avoid direct heating to lead to pesticide composition to decompose, return bend 25 carries the conduction oil to the position that the water kept away from jar body 21, prevent that deposition mechanism 5 stirs the centrifugation to the water, heavy liquid is discharged through first delivery tube 4, collection miscellaneous subassembly 26 avoids the middle part position temperature of water too low and crystallization to cause the jam, the problem that extractant or the inside ingredient crystallization speed of water accelerates and leads to the drain channel jam has been solved.
As shown in fig. 3, 4 and 5, the stabilizing assembly 24 includes a connecting sheet 241, the surface of the connecting sheet 241 is fixedly connected with the inner side surface of the tank 21, the surface of the connecting sheet 241 is fixedly connected with an infusion pump 242, one end of the infusion pump 242 away from the connecting sheet 241 is fixedly connected with a casing 244, a stabilizing rod 243 is fixedly connected between the casing 244 and the infusion pump 242, a position between the heat conducting shell 22 and the infusion pump 242 is fixedly connected with the surface of the elbow 25, the impurity collecting assembly 26 includes an assembly wall 261, the surface of the assembly wall 261 is fixedly connected with the surface of the casing 244, one side of the assembly wall 261 is fixedly connected with a first net body 262, one side of the assembly wall 261 away from the first net body 262 is fixedly connected with a second net body 264, a gap 263 is arranged on the surface of the assembly wall 261, and the aperture of the second net body 264 is larger than that of the first net body 262.
During the use, the inside circulation of heat conduction shell 22 has the conduction oil by the heating, the conduction oil carries out heat transfer through heat conduction shell 22 and water for the water is higher when inside in jar body 21, return bend 25 carries the conduction oil to transfer pump 242 in, the conduction oil circulates to casing 244 through transfer pump 242, the water is separated into light liquid district and heavy liquid district gradually in jar body 21, casing 244 heats the light liquid district of water, the middle part position that the subassembly wall 261 is close to jar body 21, the subassembly wall 261 is impacted when rivers are stirred, firm pole 243 makes casing 244 and subassembly wall 261 can be firm to be connected, avoid being damaged by the rivers impact, heat transfer between casing 244 and the water, avoid the water local temperature too low to lead to crystallization.
As shown in fig. 3 and 6, heat conduction oil is introduced into the heat conduction shell 22, the stabilizing component 24 supports and fixes the impurity collection component 26, the impurity collection component 26 extends to a light liquid separation area, the position, away from the heat conduction shell 22, inside the device is stirred and collected, the top of the base 1 is fixedly connected with the tank body 21, the inner side surface of the tank body 21 is fixedly connected with the surface of the heat conduction shell 22, the surface of the heat conduction shell 22 is fixedly connected with the oil pump 23, the surface of the heat conduction shell 22 is fixedly connected with the bent pipe 25, the deposition preventing mechanism 5 comprises a driving device 51, the bottom of the driving device 51 is fixedly connected with the top of the tank body 21, the output end of the driving device 51 is fixedly connected with a centrifugal component 52, the bottom of the centrifugal component 52 is fixedly connected with a turbine 53, the surface of the centrifugal component 52 is fixedly connected with a synergistic component 54, and the top of the inner side surface of the tank body 21 is fixedly connected with a guide wall 55.
During the use, drive equipment 51 drives the rotation of synergy subassembly 54, the synergy subassembly 54 extrudees the heavy liquid to the position that is close to jar body 21 through centrifugal force, guide wall 55 separates the liquid, the light liquid is discharged through second delivery tube 6, centrifugal assembly 52 drives the rotation of synergy subassembly 54, firm subassembly 24 runs through synergy subassembly 54, make collection miscellaneous subassembly 26 extend to the light liquid separation district, during centrifugal assembly 52 rotates, collection miscellaneous subassembly 26 and centrifugal assembly 52 relatively rotate, collection miscellaneous subassembly 26 separates and collects the floc in the water, turbine 53 throws the material of water bottom to the medial surface of jar body 21, thereby promote the inside global flow of water, the floc in the water has been solved and has been piled up easily in the problem that the rotary drum inner wall causes the liquid separation effect variation.
As shown in fig. 6, 7 and 8, the centrifugal component 52 includes a rod 521, the top end of the rod 521 is fixedly connected with the output end of the driving device 51, the bottom end of the rod 521 is fixedly connected with the top of the turbine 53, the surface of the rod 521 is fixedly connected with an arc piece 522, a fixed ring 523 is fixedly connected to the surface of the arc piece 522 near the edge, an opening 524 is provided on the surface of the arc piece 522, the synergistic component 54 includes a cylinder 541, the inner side surface of the cylinder 541 is fixedly connected with the surface of the rod 521 through a connecting rod, the lower position of the surface of the rod 521 is fixedly connected with an extension cylinder 542 through the connecting rod, a liquid through hole 543 is provided on the surface of the cylinder 541, a blocking piece 544 is fixedly connected to the upper position of the surface of the cylinder 541, and the surface of the stabilizing component 24 extends to the inside of the cylinder 541.
During use, the rod body 521 is driven by the driving device 51 to rotate, the arc piece 522 is a plate with an arc section, when the arc piece 522 rotates, heavier substances are centrifugally thrown out, light liquid is extruded to a position close to the rod body 521, the rotation of the opening 524 and the turbine 53 promotes the vertical direction flow of water body, so that the heavy liquid and the light liquid of the water body are better in separation effect, the heavy liquid is thrown out to pass through the liquid through hole 543 and then is accumulated on the inner side surface of the tank body 21, the extension barrel 542 is matched with the turbine 53, the liquid separation effect is better, the blocking piece 544 is close to the first delivery pipe 4, the water body is blocked, and the heavy liquid separated in the water body is discharged through the first delivery pipe 4.
As shown in fig. 5 and 7, the surface of the assembly wall 261 is fixedly connected with the surface of the casing 244, one side of the assembly wall 261 is fixedly connected with the first net body 262, one side of the assembly wall 261 away from the first net body 262 is fixedly connected with the second net body 264, the surface of the assembly wall 261 is provided with a gap 263, the aperture of the second net body 264 is larger than that of the first net body 262, the top end of the rod 521 is fixedly connected with the output end of the driving device 51, the bottom end of the rod 521 is fixedly connected with the top of the turbine 53, the surface of the rod 521 is fixedly connected with the arc-shaped sheet 522, the position, close to the edge, of the surface of the arc-shaped sheet 522 is fixedly connected with the fixed ring 523, and the surface of the arc-shaped sheet 522 is provided with an opening 524.
During the use, the inside of casing 244 lets in the conduction oil for casing 244 heats light liquid, the body of rod 521 drives arc piece 522 rotation, thereby stir the water, the clearance 263 on subassembly wall 261 surface makes arc piece 522 rotatable centrifugation to the water, solid fixed ring 523 guides the flow direction of liquid, make heavy liquid flow to the medial surface of jar body 21, the water flows through first cell body 262 and second cell body 264 in proper order, the aperture of first cell body 262 is great makes floccule and crystal get into subassembly wall 261, second cell body 264 obstructs floccule and crystal, thereby floccule and crystal in the extraction process in the messenger water are collected, avoid causing the jam when impurity gets into the delivery tube.
It is noted that relational terms such as first and second, and the like are used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Moreover, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Without further limitation. The term "comprising" an element defined by the term "comprising" does not exclude the presence of other identical elements in a process, method, article or apparatus that comprises the element.
Claims (10)
1. An agricultural chemical separation and extraction device in a water body is characterized in that: comprising
A base (1);
the crystallization prevention mechanism (2) is arranged above the base (1), a liquid inlet pipe (3) is fixedly connected to the middle position of the surface of the crystallization prevention mechanism (2), the liquid inlet pipe (3) conveys water into the crystallization prevention mechanism (2), and heat conduction oil is added into the crystallization prevention mechanism (2) to heat the water and stir the water; the device comprises a heat conducting shell (22), a stabilizing component (24) and a impurity collecting component (26), wherein heat conducting oil is introduced into the heat conducting shell (22), the impurity collecting component (26) is supported and fixed by the stabilizing component (24), and the impurity collecting component (26) extends to a light liquid separation area to stir and collect impurities at a position, far away from the heat conducting shell (22), inside the device;
prevent deposit mechanism (5), set up in the middle part position of preventing crystallization mechanism (2) medial surface for stir the water, promote heavy liquid separation to get rid of heat conduction shell (22), prevent the first delivery tube (4) of upper position fixedly connected with on crystallization mechanism (2) surface, prevent that the position fixedly connected with second delivery tube (6) near the middle part in crystallization mechanism (2) top, the heavy liquid of first delivery tube (4) discharge, the light liquid of second delivery tube (6) discharge.
2. The device for separating and extracting pesticide in water according to claim 1, wherein: the top fixedly connected with jar body (21) of base (1), the medial surface of jar body (21) is connected with the surface mounting of heat conduction shell (22), the surface mounting of heat conduction shell (22) is connected with oil pump (23), the surface mounting of heat conduction shell (22) is connected with return bend (25).
3. The device for separating and extracting pesticide in water according to claim 2, wherein: the stabilizing assembly (24) comprises a connecting sheet (241), the surface of the connecting sheet (241) is fixedly connected with the inner side surface of the tank body (21), and the surface of the connecting sheet (241) is fixedly connected with an infusion pump (242).
4. A device for separating and extracting pesticides in a water body according to claim 3, wherein: one end of the infusion pump (242) far away from the connecting sheet (241) is fixedly connected with a shell (244), a fixing rod (243) is fixedly connected at a position between the shell (244) and the infusion pump (242), and the position between the heat conducting shell (22) and the infusion pump (242) is fixedly connected with the surface of the bent pipe (25).
5. The device for separating and extracting pesticide in water according to claim 4, wherein: the impurity collection assembly (26) comprises an assembly wall (261), the surface of the assembly wall (261) is fixedly connected with the surface of the shell (244), and one side of the assembly wall (261) is fixedly connected with a first net body (262).
6. The device for separating and extracting pesticide in water according to claim 5, wherein: one side of the assembly wall (261) far away from the first net body (262) is fixedly connected with a second net body (264), a gap (263) is formed in the surface of the assembly wall (261), and the aperture of the second net body (264) is larger than that of the first net body (262).
7. The device for separating and extracting pesticide in water according to claim 6, wherein: the anti-deposition mechanism (5) comprises driving equipment (51), the bottom of the driving equipment (51) is fixedly connected with the top of the tank body (21), and the output end of the driving equipment (51) is fixedly connected with a centrifugal assembly (52).
8. The device for separating and extracting pesticide in water according to claim 7, wherein: the bottom of centrifugal subassembly (52) is fixedly connected with turbine (53), the surface fixedly connected with of centrifugal subassembly (52) increases efficiency subassembly (54), the top of jar body (21) medial surface is fixedly connected with guide wall (55).
9. The device for separating and extracting pesticide in water according to claim 8, wherein: the centrifugal assembly (52) comprises a rod body (521), the top end of the rod body (521) is fixedly connected with the output end of the driving device (51), and the bottom end of the rod body (521) is fixedly connected with the top of the turbine (53).
10. The device for separating and extracting pesticide in water according to claim 9, wherein: the surface of the rod body (521) is fixedly connected with an arc-shaped sheet (522), a fixing ring (523) is fixedly connected to the position, close to the edge, of the surface of the arc-shaped sheet (522), and an opening (524) is formed in the surface of the arc-shaped sheet (522).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310566644.6A CN116282325A (en) | 2023-05-19 | 2023-05-19 | Pesticide separation and extraction device in water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202310566644.6A CN116282325A (en) | 2023-05-19 | 2023-05-19 | Pesticide separation and extraction device in water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN116282325A true CN116282325A (en) | 2023-06-23 |
Family
ID=86836289
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202310566644.6A Pending CN116282325A (en) | 2023-05-19 | 2023-05-19 | Pesticide separation and extraction device in water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN116282325A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6426010B1 (en) * | 1997-11-18 | 2002-07-30 | Total | Device and method for separating a heterogeneous mixture |
| CN208799862U (en) * | 2018-09-25 | 2019-04-30 | 龙岩市华众机械有限公司 | A kind of novel main degreasing filter vat |
| CN210875807U (en) * | 2019-10-14 | 2020-06-30 | 西安艾沃特环境科技有限公司 | Old emulsified oil centrifugal separation device |
| CN111793522A (en) * | 2020-08-03 | 2020-10-20 | 内蒙古农业大学 | Edible linseed oil extraction debitterizing separator |
| CN112755588A (en) * | 2021-01-13 | 2021-05-07 | 常州机电职业技术学院 | Extraction centrifugal mixing system based on bio-pharmaceuticals and centrifugal method thereof |
| CN214158804U (en) * | 2020-09-23 | 2021-09-10 | 安庆辰步药物科技有限公司 | High-efficient centrifugal device is used in anthranilamide processing |
| CN215996654U (en) * | 2021-09-07 | 2022-03-11 | 南通亿能防腐科技工程有限公司 | Structure for preventing crystallization and blockage at kettle bottom outlet of glass lining kettle |
-
2023
- 2023-05-19 CN CN202310566644.6A patent/CN116282325A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6426010B1 (en) * | 1997-11-18 | 2002-07-30 | Total | Device and method for separating a heterogeneous mixture |
| CN208799862U (en) * | 2018-09-25 | 2019-04-30 | 龙岩市华众机械有限公司 | A kind of novel main degreasing filter vat |
| CN210875807U (en) * | 2019-10-14 | 2020-06-30 | 西安艾沃特环境科技有限公司 | Old emulsified oil centrifugal separation device |
| CN111793522A (en) * | 2020-08-03 | 2020-10-20 | 内蒙古农业大学 | Edible linseed oil extraction debitterizing separator |
| CN214158804U (en) * | 2020-09-23 | 2021-09-10 | 安庆辰步药物科技有限公司 | High-efficient centrifugal device is used in anthranilamide processing |
| CN112755588A (en) * | 2021-01-13 | 2021-05-07 | 常州机电职业技术学院 | Extraction centrifugal mixing system based on bio-pharmaceuticals and centrifugal method thereof |
| CN215996654U (en) * | 2021-09-07 | 2022-03-11 | 南通亿能防腐科技工程有限公司 | Structure for preventing crystallization and blockage at kettle bottom outlet of glass lining kettle |
Non-Patent Citations (1)
| Title |
|---|
| 刘章现等: "《环境管理与污染治理实用技术》", 华中科技大学出版社, pages: 337 - 229 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN116282325A (en) | Pesticide separation and extraction device in water | |
| JP3310629B2 (en) | Coagulation sedimentation equipment | |
| CN211097589U (en) | Convenient 3000L's of collecting stills | |
| CN1286737C (en) | Aggregation precipitation method and apparatus | |
| CN109809641B (en) | Sewage treatment system and method | |
| CN113735317B (en) | Special efficient wastewater treatment system for extracting N-methyl pyrrolidone | |
| CN205887395U (en) | A sorting machine and trench oil processing equipment for kitchen garbage | |
| CN209848342U (en) | Rosin continuous distillation system | |
| CN112028362A (en) | Industrial wastewater secondary utilization and purification device with solid-liquid separation mechanism | |
| CN117361666B (en) | Food processing sewage treatment equipment and treatment method | |
| CN220609133U (en) | Ethylene carbonate purification device | |
| CN220078673U (en) | Self-circulation evaporation type industrial wastewater treatment equipment | |
| CN218485232U (en) | A deposit device for sewage | |
| CN115477459B (en) | Fatlute processing system | |
| CN113402071B (en) | Dirty oil treatment device for oil refinery | |
| CN220738986U (en) | Desalination device for household garbage incineration fly ash | |
| CN118145862A (en) | Environment-friendly efficient centrifugal water treatment sludge drying device | |
| CN220939205U (en) | Original reverse-flow ultrasonic extraction device for tannic acid | |
| CN218810727U (en) | Precipitation device for wastewater treatment | |
| CN218529858U (en) | Sodium acetate solid-liquid mixture centrifugal separation recrystallization equipment | |
| CN216934817U (en) | Sedimentation device for herbicide production | |
| CN219836136U (en) | Butyl oleate processing and collecting machine | |
| CN217939152U (en) | Evaporation equipment is used in production of crystallization fructose | |
| CN218665476U (en) | Brine separation device | |
| CN211625964U (en) | Raw material drying device for lamp pole coating manufacturing |
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 | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20230623 |
|
| RJ01 | Rejection of invention patent application after publication |