CN108722152A - A kind of purifier and fluid handling system - Google Patents
A kind of purifier and fluid handling system Download PDFInfo
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- CN108722152A CN108722152A CN201810532375.0A CN201810532375A CN108722152A CN 108722152 A CN108722152 A CN 108722152A CN 201810532375 A CN201810532375 A CN 201810532375A CN 108722152 A CN108722152 A CN 108722152A
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- 239000012530 fluid Substances 0.000 title claims abstract description 98
- 239000000126 substance Substances 0.000 claims abstract description 55
- 238000000746 purification Methods 0.000 claims description 137
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 25
- 238000010438 heat treatment Methods 0.000 claims description 12
- 238000005507 spraying Methods 0.000 claims description 10
- 239000007921 spray Substances 0.000 claims description 9
- 230000003247 decreasing effect Effects 0.000 claims description 3
- 238000010521 absorption reaction Methods 0.000 abstract description 14
- 238000000034 method Methods 0.000 abstract description 10
- 238000004140 cleaning Methods 0.000 abstract description 5
- 239000002245 particle Substances 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 6
- 239000000428 dust Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- 238000005265 energy consumption Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000004891 communication Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- 238000011403 purification operation Methods 0.000 description 2
- 230000002441 reversible effect Effects 0.000 description 2
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000002144 chemical decomposition reaction Methods 0.000 description 1
- 238000009390 chemical decontamination Methods 0.000 description 1
- 230000001427 coherent effect Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
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- 230000005484 gravity Effects 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/60—Combinations of devices covered by groups B01D46/00 and B01D47/00
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- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Environmental & Geological Engineering (AREA)
- Health & Medical Sciences (AREA)
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- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
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Abstract
A kind of purifier of present invention offer and fluid handling system, wherein purifier include：First rotary barrel is provided with the first blade in the first rotary barrel, and the both ends of the first rotary barrel are respectively arranged with input port and delivery outlet；Second rotary barrel is provided with the second blade in the second rotary barrel, and the both ends of the second rotary barrel are respectively arranged with input port and delivery outlet；With the clarifier being set between the first rotary barrel and the second rotary barrel, clarifier is provided with chemical cleaning method chamber, and the input port of clarifier is connected to the delivery outlet of the first rotary barrel, and the delivery outlet of clarifier is connected to the input port of the second rotary barrel.In this way, the fluid of purifier absorbs, purifies and export the front and back efficiently undertaking of operation, absorption piece and Power Component need not be separately provided, the efficiency of less energy intensive, purified treatment is higher.
Description
Technical Field
The invention relates to the technical field of automatic control, in particular to a purification device and a fluid treatment system.
Background
Haze in the form of atmospheric pollution (aerosol such as polluted atmosphere, small liquid particles, small particle solids and the like) is harmful to human health. The haze purification problem is researched by huge investment in countries around the world. The haze components are complex, and organic chemical hazards, physical small-particle liquid particles and dust exist. The current methods are as follows: 1 electrostatic dust collection type; 2, an electronic dust collection type; 3, ozone type; 4 negative ion type; 5, a filter element type; 6 activated carbon adsorption type; 7 ultraviolet sterilization type; 8 comprehensive type and the like.
The existing atmospheric or other fluid collectors adopt axial-flow type short-stroke turbofan, and have the advantages of small pressure, large energy consumption and poor purification efficiency.
Therefore, the existing fluid treatment device has the technical problem of poor purification efficiency.
Disclosure of Invention
The embodiment of the invention provides a purification device and a fluid treatment system, which aim to solve the technical problem that the existing fluid treatment device is poor in purification efficiency.
In order to achieve the above purpose, the embodiments of the present invention provide the following specific schemes:
in a first aspect, an embodiment of the present invention provides a purification apparatus, including: the device comprises a first rotating cylinder, a second rotating cylinder and a third rotating cylinder, wherein a first blade is arranged in the first rotating cylinder, and an input port and an output port are respectively arranged at two ends of the first rotating cylinder;
the second rotating cylinder is internally provided with a second blade, and two ends of the second rotating cylinder are respectively provided with an input port and an output port; and,
the purifier is arranged between the first rotating cylinder and the second rotating cylinder and provided with a chemical purifying cavity, an input port of the purifier is communicated with an output port of the first rotating cylinder, and an output port of the purifier is communicated with an input port of the second rotating cylinder.
Optionally, the first blade extends spirally along the inner circumference of the first rotary cylinder; and/or the presence of a gas in the gas,
the second blade extends spirally along the inner circumference of the second rotary cylinder.
Optionally, the first blade extends spirally along the inner circumference of the first rotary cylinder; and/or the presence of a gas in the gas,
the second blade extends spirally along the inner circumference of the second rotary cylinder.
Optionally, the first blade and/or the second blade are spirally arranged in a centripetal manner; or,
the first and/or second vanes are three-dimensional scroll vanes.
Optionally, be provided with heating wire and heat reflection mirror surface in the clarifier, the heat reflection mirror surface encircles the heating wire forms the chemical purification chamber.
Optionally, an electric control valve plate for controlling the flow of fluid passing through the port is arranged at the port of the chemical purification cavity;
the electric control valve plate comprises a fixing plate and an adjusting plate, wherein at least one through hole is formed in each of the fixing plate and the adjusting plate, the fixing plate is fixedly arranged on the port of the chemical purification cavity, and the adjusting plate is movably covered on the fixing plate;
when the adjusting sheet rotates to the calibration position, the through hole in the adjusting sheet is communicated with the through hole in the fixing sheet.
Optionally, the first rotary cylinder is a conical cylinder;
the taper of the first rotary cylinder is gradually increased along the first direction.
Optionally, the side wall of the second rotary cylinder is a filter screen;
the outer cover of the second rotary cylinder is sleeved with an outer cover, a water spraying unit is arranged on the outer cover, and a spray head of the water spraying unit faces the filter screen.
Optionally, the purification device further comprises a deviation rotary engine, and the deviation rotary engine is used for driving the first rotary cylinder and/or the second rotary cylinder.
Optionally, the purifier is provided with a physical purification cavity;
the input port of the physical purification cavity is communicated with the output port of the first rotary cylinder, the output port of the physical purification cavity is communicated with the input port of the chemical purification cavity, and the output port of the chemical purifier is communicated with the input port of the second rotary cylinder.
In a second aspect, embodiments of the present invention provide a fluid treatment system comprising a purification apparatus as described in any one of the first aspect.
In the embodiment of the invention, the purification device comprises a first rotary cylinder, a second rotary cylinder and a purifier, wherein when a first blade arranged in the first rotary cylinder rotates along with the first rotary cylinder, the first blade absorbs fluid in the environment, the fluid is conveyed into a chemical purification cavity of the purifier for purification treatment, and then the fluid is conveyed to the second rotary cylinder, and a second blade in the second rotary cylinder rotates along with the second rotary cylinder to output the purified fluid. Therefore, the fluid absorption, purification and output operations of the purification device are efficiently carried before and after, and the purification treatment efficiency is higher. In addition, the first rotating barrel drives the rotation of the first internal blades to realize the efficient absorption of the fluid, the second rotating barrel drives the rotation of the second internal blades to realize the efficient output of the fluid, the absorption part and the power assembly do not need to be arranged independently, the energy consumption is low, and the purification efficiency is further improved.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings needed to be used in the description of the embodiments of the present invention will be briefly introduced below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained according to these drawings without inventive exercise.
Fig. 1 is a schematic structural diagram of a purification apparatus according to an embodiment of the present invention;
fig. 2 is a schematic structural diagram of a first rotary cylinder of the purification apparatus provided in the embodiment of the present invention;
FIG. 3 is a schematic view of a purifier structure of a purification apparatus according to an embodiment of the present invention;
FIG. 4 is a schematic structural diagram of a second rotary cylinder of the purification apparatus provided in the embodiment of the present invention;
fig. 5a to 5d are schematic structural views of an electric control valve plate of a purification apparatus according to an embodiment of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are some, not all, embodiments of the present invention. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1, a schematic structural diagram of a purification apparatus according to an embodiment of the present invention is shown. As shown in fig. 1, a purification apparatus 10 includes:
the first rotating cylinder 100 is provided with a first blade 110 inside, and an input port and an output port are respectively arranged at two ends of the first rotating cylinder 100;
a second rotating cylinder 200, wherein a second blade 210 is arranged in the second rotating cylinder 200, and an input port and an output port are respectively arranged at two ends of the second rotating cylinder 200; and,
a purifier 300 disposed between the first rotary cylinder 100 and the second rotary cylinder 200, the purifier 300 being provided with a chemical purifying chamber 310, an input port of the purifier 300 being communicated with the output port 140 of the first rotary cylinder 100, an output port of the purifier 300 being communicated with an input port of the second rotary cylinder 200.
The purifying device provided by the embodiment is used for purifying fluid in an environment, and the fluid for purification can include, but is not limited to, a purifying device for haze, industrial polluted gas, liquid and powdery solid particles in air. The purification device can be directly arranged in an open environment to purify the surrounding environment.
The purification apparatus may mainly include a first rotary cylinder 100, a second rotary cylinder 200, and a purification apparatus, and an input port of the first rotary cylinder 100 is used as an inflow port of fluid in the environment. The output port of the first rotary cylinder 100 is communicated with the input port of the purifier 300, the output port of the purifier 300 is communicated with the input port of the second rotary cylinder 200, and the output port of the second rotary cylinder 200 is used as the outlet port of the purified fluid. The input port of the first rotary cylinder 100 and the output port of the second rotary cylinder 200 can be directly connected to the environment for exchanging with the fluid in the environment, so as to achieve the purpose of purifying the fluid in the environment.
As shown in fig. 1 and 2, the first rotary cylinder 100 is an initial part of the purification apparatus, and performs an initial absorption step of the purification operation of the purification apparatus. The first vane 110 is disposed in the first rotary cylinder 100, and when the first rotary cylinder 100 rotates, the first vane 110 rotates with the first rotary cylinder to form a vortex flow entering the first rotary cylinder 100 from the outside of the input port of the first rotary cylinder 100. Thus, fluid located at the periphery of the input port of the first rotating cylinder 100, i.e., the vortex flow following the input port of the first rotating cylinder 100, enters the first rotating cylinder 100, is absorbed by the first rotating cylinder 100, and is compressed along with the vortex flow. As the first blades 110 extend in the first rotary cylinder 100, the formed vortex is directed from the input port to the output port, and the fluid entering the first rotary cylinder 100 can pass through the first rotary cylinder 100 to the output port of the first rotary cylinder 100 and enter the purifier 300. In addition, a fluid collecting net cover 120 may be further provided at the input port position of the first cylinder to improve the absorption efficiency.
As shown in fig. 1 and 3, the purifier 300 is an intermediate functional part of the purification apparatus, and performs a purification function of the purification apparatus. A chemical purifying chamber 310 is provided in the purifier 300 for performing a purifying operation of a chemical reaction on the absorbed fluid. The input port of the purifier 300 is communicated with the output port of the first rotary cylinder 100, and the output port of the purifying apparatus is communicated with the input port of the second rotary cylinder 200 to introduce the absorbed fluid, purify it, and discharge the fluid after the purification treatment into the second rotary cylinder 200 to discharge the purified air through the second rotary cylinder 200.
As shown in fig. 1 and 4, the second rotary cylinder 200 is disposed at the end of the fluid flow direction of the purification apparatus, and is used for performing a fluid discharge operation after the purification. The second blade 210 is provided in the second rotary cylinder 200, and when the second rotary cylinder 200 rotates, the second blade 210 also rotates, forming a vortex flow that is output from the output port of the second rotary cylinder 200 to the outside of the output port of the second rotary cylinder 200. As the second blades 210 extend in the second rotary cylinder 200, the formed vortex is directed from the input port of the second rotary cylinder 200 to the output port, and the fluid entering the second rotary cylinder 200 can flow out of the output port of the second rotary cylinder 200 from the input port of the second rotary cylinder 200 along the vortex, so as to achieve the discharge operation of the purified fluid.
The purification process of the purification device provided by the embodiment can be as follows: the first rotating cylinder 100 and the first blades 110 inside the cylinder rotate to absorb the fluid outside the input port of the first rotating cylinder 100, and the fluid flows into the purifier 300 through the output port of the first rotating cylinder 100, the absorbed fluid is chemically purified by the chemical purifying chamber 310 inside the purifier 300, and the purified fluid is output through the second rotating cylinder 200 and the second blades 210, which rotate, that is, the operation of purifying the fluid is completed. The purification device can realize continuous fluid operation, that is, the fluid absorbed from the first rotary cylinder 100 enters the purifier 300 randomly for purification and is discharged from the second rotary cylinder 200 for purification.
The purifier that above-mentioned this embodiment provided, purifier's fluid absorption, purification and output operation front and back high-efficient accept, and purification treatment's efficiency is higher. In addition, the first rotating barrel drives the rotation of the first internal blades to realize the efficient absorption of the fluid, the second rotating barrel drives the rotation of the second internal blades to realize the efficient output of the fluid, the absorption part and the power assembly do not need to be arranged independently, the energy consumption is low, and the purification efficiency is further improved. The integral vortex-shaped extension of the blades in the rotary cylinder enables the fluid to be absorbed and compressed in a complete period, and the rotary cylinder has high working efficiency, low energy consumption and low noise.
On the basis of the above-mentioned embodiments, the specific implementation of the first blade 110 in the first rotary cylinder 100 and the specific implementation of the second blade 210 in the second rotary cylinder 200 assist in achieving the fluid absorbing and discharging functions. The following detailed description is to be read with reference to the drawings and the accompanying detailed description.
In one embodiment, as shown in fig. 1, 2 and 4, the first blade 110 extends helically along the inner circumference of the first rotating cylinder 100; and/or the presence of a gas in the gas,
the second vane 210 is spirally extended along the inner circumference of the second rotary cylinder 200.
The first blade 110 in the first rotary cylinder 100 is a blade extending continuously and in multiple periods without a shaft, and is spirally extended along the inner circumference to form a spirally extending channel communicating the input port and the output port of the first rotary cylinder 100. Thus, when the first rotary cylinder 100 rotates, the first spirally extending blade 110 drives the fluid to flow along the spirally extending channel, from the input port into the first rotary cylinder 100, and out of the first rotary cylinder 100 through the output port. The first blade 110 may include at least two elongated blades, each of which may form a helical cycle, and is connected to the wall of the first rotary cylinder 100 in the axial direction of the first rotary cylinder 100. Therefore, the friction between the blade and the fluid can be reduced, the noise is reduced, and the blade can be widely applied to fluids with different qualities and densities, such as gas, liquid, powdery particle solid and the like.
The second blade 210 is extended in a spiral shape on the inner circumference of the first rotary cylinder 100 to form a spiral extended passage communicating the input port and the output port of the second rotary cylinder 200. Thus, when the second rotary cylinder 200 rotates, the second spiral blades 210 drive the fluid to flow out from the output port of the second rotary cylinder 200 along the spiral extending channel. The second blade 210 may include at least two elongated blades, each of which may form a helical cycle, and the blades are connected to the wall of the second rotary cylinder 200 in the axial direction of the second rotary cylinder 200.
This blade setting mode sets up the blade and is the heliciform extension on the interior circumference of barrel, like this, along with the rotatory passageway that naturally forms the heliciform extension of barrel, can improve the velocity of flow of fluid, has just also improved the absorption rate or the exhaust velocity of fluid, and then has improved the purification efficiency of fluid. The blade installation method of the present embodiment may be applied to the first blade 110 in the first rotary cylinder 100, or may be applied to the second blade 210 in the second rotary cylinder 200, and is not limited.
In another specific embodiment, the pitch of the first blade 110 is gradually decreased along a first direction, which is an extending direction from the input port to the output port of the first rotary cylinder 100; and/or
The extending direction from the input port to the output port of the second rotary cylinder 200 is taken as a second direction, and the pitch of the second blade 210 gradually increases along the second direction.
Furthermore, the first blade 110 and/or the second blade 210 are arranged in a radial spiral; or,
the first blade 110 and/or the second blade 210 are three-dimensional scroll blades.
Further, the first rotating cylinder 100 may also be a conical cylinder, and the taper of the first rotating cylinder 100 gradually increases along the first direction.
In the present embodiment, the specific structure of the blade is further defined, and mainly includes the length variation trend of the blade pitch and the blade extension shape.
The extending direction of the first rotary cylinder 100 from the input port to the output port is defined as a first direction. The extending direction of the second rotary cylinder 200 from the input port to the output port is defined as a second direction.
The first blade 110 disposed on the inner circumference of the first rotary cylinder 100 extends spirally on the inner circumference of the cylinder, and the first blade 110 is disposed spirally along the axial direction of the first rotary cylinder 100, and the pitch of the first blade 110 gradually decreases along the first direction, that is, the pitch of the first blade 110 gradually decreases from the input port to the output port. In other embodiments, the first vane 110 may also be a three-dimensional scroll vane.
The second blade 210 disposed on the inner circumference of the second rotary cylinder 200 extends spirally on the inner circumference of the cylinder, and the second blade 210 may be disposed spirally along the axial direction of the second rotary cylinder 200, and the pitch of the second blade 210 increases gradually along the second direction, that is, the pitch of the second blade 210 increases gradually from the input port to the output port. In other embodiments, the second vane 210 may also be a three-dimensional scroll vane. Second blade 210 is reverse three-dimensional vortex blade to produce strong centrifugal force, impel to get into the fluid separation of the rotatory barrel 200 of second, the fluid up to standard that the proportion of separation is lighter can directly discharge, and the fluid up to standard that the proportion is great can continue to participate in purification operation, for example processing such as water purification and filter screen screening dirt, etc. with the haze purification scheme that realizes high-efficient, coherent, thorough.
The first blade 110 and/or the second blade 210 are arranged to extend spirally along the center from the input port to the output port of the cylinder, and the pitch of the first blade and the second blade gradually changes. Thus, the pitch of the first vane 110 is gradually decreased in the process of flowing from the input port to the output port of the first rotary cylinder 100, which gradually decreases the centripetal force of the first rotary cylinder 100, draws the fluid into the first rotary cylinder 100 with a large attractive force, and enables the output port of the first rotary cylinder 100 to flow into the input port of the purifier 300 with a large degree of experience.
The first rotating cylinder 100 is a conical cylinder, and the taper of the first rotating cylinder 100 is gradually increased along the first direction, so that the variation tendency of the centripetal force of the first rotating cylinder 100 can be further improved, and the circulation of the extending passage formed by the first blade 110 through which the fluid passes can be improved.
During the process that the fluid purified by the purifier 300 flows along the input port to the output port of the second rotary cylinder 200, the pitch of the second blades 210 is gradually increased, so that the centripetal force of the second rotary cylinder 200 is gradually increased, and the fluid is concentrated on the output port portion of the second rotary cylinder 200 near the middle of the central shaft with a larger attractive force and is output in a concentrated manner.
According to the blade arrangement scheme, through the variation trend of the centripetal force, the fluid can smoothly and quickly flow in or out along the spiral channel, and the flowing speed of the fluid is improved. Further, the spirally extending blades in the first rotary cylinder 100 can increase the centripetal pressure in the cylinder to efficiently compress the air. If the blades extend in the opposite direction, the centrifugal repulsion force of the blades in the cylinder can be improved, and the separation effect of gas and solid in the fluid is improved.
In another embodiment, as shown in fig. 3, a heating wire 330 and a heat reflecting mirror 320 may be disposed in the purifier 300, and the heat reflecting mirror 320 surrounds the heating wire 330 to form the chemical purifying chamber 310.
The purifier 300 is used for purifying the fluid absorbed by the first rotary cylinder 100, and mainly eliminates the content of most harmful substances in the fluid through a chemical reaction. The fluid purified by the purifier 300 is discharged through the second rotary cylinder 200. The heating wire 330 and the heat reflecting mirror surface 320 are arranged in the purifier 300, the heating wire 330 is arranged in the purifier 300, and the heat reflecting mirror surface 320 surrounds the heating wire 330 to form a closed purifying chamber, namely a chemical purifying chamber, so as to provide a thermal environment required by the chemical reaction of fluid purification.
In addition, the purifier 300 may further include a casing, the heat reflecting mirror 320 is attached to an inner wall of the casing, the heating wire 330 is disposed in an enclosed region of the heat reflecting mirror 320, and a working surface of the heat reflecting mirror 320 faces the heating wire 330, so that heat generated by the heating wire 330 can be concentrated in the chemical purifying chamber, and a stable thermal environment required by the chemical purifying reaction is provided.
Further, the housing may be a circular spherical shell, and a plurality of heat reflecting mirrors 320 are disposed on the inner wall of the spherical shell to form a circular thermochemical cleaning chamber, so that the chemical reaction space and the heat reflecting effect can be increased. A high-temperature and high-pressure environment is formed in the chemical purification chamber 310, and the organic substances contained in the absorbed fluid are chemically decomposed, so that a chemical purification effect can be achieved.
In addition, as shown in fig. 5a to 5d, the port of the chemical purification chamber 310 may be further provided with an electrically controlled valve sheet 340 for controlling the flow rate of the fluid passing through the port;
the electric control valve plate 340 comprises a fixed plate 341 and an adjusting plate 342, at least one through hole 343 is formed on each of the fixed plate 341 and the adjusting plate 342, the fixed plate 341 is fixedly arranged at the port of the chemical purification chamber 310, and the adjusting plate 342 is movably covered on the fixed plate 341;
when the adjusting piece 342 rotates to the calibration position, the through hole 343 of the adjusting piece 342 is communicated with the through hole 343 of the fixing piece 341.
The input port of the chemical decontamination chamber 310 communicates with the output port of the first rotary cylinder 100 to receive the fluid absorbed by the first rotary cylinder 100. The output port of the chemical purifying chamber 310 communicates with the input port of the second rotary cylinder 200 to discharge the purified fluid through the second rotary cylinder 200. In order to prevent the untreated fluid absorbed in the first rotary cylinder 100 and the treated fluid in the second rotary cylinder 200 from flowing into the chemical purifying chamber 310 and affecting the normal treatment operation in the chemical purifying chamber 310, an electric control valve sheet 340 may be disposed between the output port of the first rotary cylinder 100 and the input port of the chemical purifying chamber 310, and between the output port of the chemical purifying chamber 310 and the input port of the second rotary cylinder 200, so as to control the flow rate and communication state of the fluid at the corresponding port.
Specifically, the electronic control valve plate 340 may include a fixed plate 341 and an adjusting plate 342, at least one through hole 343 is formed in each of the fixed plate 341 and the adjusting plate 342, and the fixed plate 341 and the adjusting plate 342 may move relatively to each other, that is, whether the through hole 343 in the fixed plate 341 and the through hole 343 in the adjusting plate 342 are aligned to achieve the communication and blocking states of the electronic control valve plate 340.
The fixed plate 341 of the electric control valve plate 340 is fixedly arranged at the port of the chemical purification chamber 310, the adjusting plate 342 is movably covered on the fixed plate 341, the adjusting plate 342 can be rotated to change the angle of the adjusting plate 342 covered on the fixed plate 341, and then whether the through hole 343 arranged on the adjusting plate 342 is aligned with the through hole 343 arranged on the fixed plate 341 is controlled.
In a specific implementation, the fixing plate 341 may be welded to the port of the chemical purification chamber 310, or fixed to the port of the chemical purification chamber 310 by a connector such as a bolt. The rotating shaft corresponding to the port can be extended from the port of the chemical purification chamber 310, and the other rotating shaft can be nested on the adjusting piece 342, so that the adjusting piece 342 can rotate to cover the connecting piece of the angle. Thus, the adjusting plate 342 covers the fixing plate 341, and the adjusting plate 342 can rotate in the covering area corresponding to the fixing plate 341 to adjust the angle of the through hole 343 formed in the adjusting plate 342.
The number of the through holes 343 formed in the fixing plate 341 and the number of the through holes 343 formed in the adjusting plate 342 may be at least one, and the size, shape, etc. of the through holes 343 may not be limited. As long as the adjusting sheet 342 can rotate, the through hole 343 formed in the adjusting sheet 342 can be communicated with and isolated from at least one through hole 343 formed in the fixing sheet 341, so as to open and block the electric control valve sheet 340.
When the cylinder needs to be controlled to be communicated with the chemical purification cavity 310, the adjusting sheet 342 is rotated by a certain angle, so that the through hole 343 on the adjusting sheet 342 is communicated with the through hole 343 on the fixing sheet 341, and fluid interaction between the cylinder and the chemical purification cavity 310 is realized. When the cylinder body and the chemical purification cavity 310 are not communicated with each other, the adjusting sheet 342 is rotated by a certain angle, so that the through hole 343 formed in the adjusting sheet 342 is not communicated with the through hole 343 formed in the fixing sheet 341, and fluid interaction between the cylinder body and the purification cavity cannot occur, thereby achieving a good isolation effect.
The electric control valve plate 340 can further comprise a processor, the processor can be connected with or integrated with the master control end of the purification device, and the rotation of the cylinder body and the automatic control of the communication state between the cylinder body and the chemical purification cavity 310 and the like can be realized by the master control end of the purification device. In the actual use process, the adjusting sheet 342 can be periodically adjusted to control the opening and closing of the electrically controlled valve sheet 340, so as to realize continuous and automatic fluid absorption, purification and output operations.
On the basis of the above embodiments, as shown in fig. 1 and 4, the side wall of the second rotary cylinder 200 may be a filter screen;
an outer cover 230 is sleeved outside the second rotary cylinder 200, a water spraying unit 220 is arranged on the outer cover 230, and a spray head of the water spraying unit 220 faces the filter screen.
In the embodiment, in order to further improve the fluid purification effect, relevant water purification components are additionally arranged. The side wall of the second rotary cylinder 200 is provided with a filter screen, and a water spraying unit 220 is arranged outside the second rotary cylinder 200. Specifically, the outer cover 230 is sleeved outside the second rotary cylinder 200, at least two water spraying units 220 are arranged on the outer cover 230, and the spray heads of the water spraying units 220 face the filter screen, so that a water purification layer surrounding the outer side wall of the second rotary cylinder 200 can be formed. In order to ensure the tidiness of the fluid purification site, a water collection tank 240, a water inlet pipe 250 and a water outlet pipe 260 may be further provided to ensure the water purification function of the water spraying unit 220 and the water recycling.
Like this, second rotatory barrel 200 is at rotatory in-process, and the fluid receives centrifugal repulsion separation, and the part that the proportion is lighter shows that the purification is up to standard, can directly discharge through the delivery outlet of second rotatory barrel 200, and the great part of proportion shows that the purification is not up to standard yet, and this part fluid is permeated through near the outer wall that the filter screen reaches second rotatory barrel 200 by centrifugal repulsion effect, and at this moment, the water spray unit 220 that sets up on the dustcoat 230 towards the fluid water spray near second rotatory barrel 200 lateral wall is water purification treatment to effectively wash the filter screen. The additional water purification process can further purify fluid, especially inorganic medium particles and dust contained in gas, and further improve the purification efficiency of the fluid.
On the basis of the above embodiment, the purification apparatus further includes an eccentric rotary motor for driving the first rotary cylinder 100 and/or the second rotary cylinder 200.
The purification device provided by the embodiment uses the eccentric rotary engine as a power component for driving the first rotary cylinder 100 and the second rotary cylinder 200 to rotate, and does not need traditional fuel and energy as power sources. Specifically, the output power of the eccentric rotary engine can be 14 kilowatts, the power is provided by relying on the gravity action instead of transmission energy, and the eccentric rotary engine is green, environment-friendly and sustainable.
On the basis of the above embodiment, the purifier 300 can also be provided with a physical purification chamber;
the input port of the physical cleaning chamber is communicated with the output port of the first rotary cylinder 100, the output port of the physical cleaning chamber is communicated with the input port of the chemical cleaning chamber 310, and the output port of the chemical cleaner 300 is communicated with the input port of the second rotary cylinder 200.
Considering that the fluid may contain more oil impurities, the purification pressure of the chemical purification chamber 310 is only higher, so a physical purification chamber may be added before the chemical purification chamber 310. Set up the physics purifies the chamber and is located between first rotatory barrel 100 and the chemical purification chamber 310, like this, through the absorptive fluid of first rotatory barrel 100, firstly gets into the physics and purifies the chamber and carry out the physics and purify, reentrant chemical purification chamber 310 carries out chemical purification and handles, and it purifies or directly discharges to get into second rotatory barrel 200 at last.
The physical purification room can mainly carry out evolution treatment, such as macromolecule filtration, distillation filtration treatment etc. to the oil impurity in the fluid, can reduce impurity content to a certain extent, alleviates chemical purification chamber 310's purification pressure to further promote evolution efficiency.
In summary, the specific process of the purification device for purifying haze provided by the invention can be as follows:
first, the transmission gear 130 is mounted outside the first rotary cylinder 100 and rotated by the eccentric rotary engine. The first rotating cylinder 100 is provided with a positive three-dimensional vortex blade, which generates centripetal high-pressure compression on air, and the high-pressure compressed air passes through an electric control valve plate 340 and enters a purification process. The positive three-dimensional vortex blade is a plurality of strip-shaped trapezoidal blades which are axially curved in a centripetal manner, the pitch is self-large and self-small, the positive three-dimensional vortex blade is connected with the wall of the cylinder body in a multi-periodic surrounding manner, and the high-efficiency and high-silence pressure can be generated by the change of the radius of the blades in the cone shape.
Secondly, the air compressed by the first rotary cylinder 100 enters the chemical purification cavity 310, the high-temperature combustion reaction in the chemical purification cavity 310 eliminates organic impurities, and the high-temperature and high-pressure differential chemical reaction efficiently promotes the chemical decomposition of organic hazards and enters the second rotary cylinder 200. When the two ends of the chemical purification chamber 310 are closed, the high temperature and the high pressure difference are achieved in the chamber, and then the high-efficiency chemical purification can be implemented.
Then, the gas enters the second rotary cylinder 200 through program control, and the reverse vortex blades arranged on the inner wall of the second cylinder rotate to centrifugally separate dust. The separation result comprises two parts, wherein one part of the separation result precesses in a vortex rotation mode, and the center of the longitudinal shaft is light purified air which reaches the standard; the other part of the heavy air centrifuged at the lateral boundary contains high density dust particles, and goes to the filter screen at the edge of the second rotary cylinder 200, and the air goes to the water spray unit 220 at the outer side wall of the cylinder.
Finally, the high pressure water spray unit 220 provided outside the sidewall of the second rotary cylinder 200 sprays water toward the filter screen to finally purify the air, and the purified air is discharged to the environment.
The purification device provided by the invention integrates chemical purification and physical purification, has high efficiency, high capacity and low noise, and achieves ultrahigh air purification rate. The purification element is wide, the application range is wide, the purification of harmful organic compounds and inorganic particles such as hydrogen-sulfur compounds, partial heavy metal pollution and the like can be efficiently eliminated, and the emission standard can be reached.
In addition, the purification device has a wide purification range, and can effectively purify polluted air within a range of 10 kilometers to reach a standard rate. The system has the advantages of high strength, high work efficiency, high purification rate, no need of electric power and traditional energy sources, low cost, small occupied area, compact and flexible layout, and is suitable for being arranged in haze urban squares, green belts, urban communities, public spaces or urban high-rise roofs, and places such as marginal areas with inconvenient traffic and electric power. The device does not use electric power and traditional energy, is green, low in cost, low in noise, high in efficiency, high in capacity, long-term in use, safe in monitoring, flexible in setting, small in site arrangement and the like, and can purify air pollution.
Embodiments of the present invention also relate to a fluid treatment system including a purification apparatus as described above with reference to fig. 1.
The fluid treatment system that this embodiment provided for the purifier of purification fluid includes first rotatory barrel, the rotatory barrel of second and clarifier, and the first blade that sets up in the first rotatory barrel is along with first rotatory barrel when rotatory, absorbs the fluid in the environment to carry to the chemical purification intracavity purification treatment of clarifier, then transmits to the rotatory barrel of second again, and the second blade in the rotatory barrel of second rotates along with the rotatory barrel of second, exports the fluid after the purification. Therefore, the fluid absorption, purification and output operations of the purification device are efficiently carried before and after, and the purification treatment efficiency is higher. In addition, the first rotating barrel drives the rotation of the first internal blades to realize the efficient absorption of the fluid, the second rotating barrel drives the rotation of the second internal blades to realize the efficient output of the fluid, the absorption part and the power assembly do not need to be arranged independently, the energy consumption is low, and the purification efficiency is further improved. The specific implementation process of the fluid treatment system provided by the embodiment of the present invention may refer to the specific implementation process of the purification apparatus provided by the above embodiment, and details are not repeated here.
The above description is only for the specific embodiments of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art can easily conceive of the changes or substitutions within the technical scope of the present invention, and all the changes or substitutions should be covered within the scope of the present invention. Therefore, the protection scope of the present invention shall be subject to the protection scope of the claims.
Claims (11)
1. A purification apparatus, comprising:
the device comprises a first rotating cylinder, a second rotating cylinder and a third rotating cylinder, wherein a first blade is arranged in the first rotating cylinder, and an input port and an output port are respectively arranged at two ends of the first rotating cylinder;
the second rotating cylinder is internally provided with a second blade, and two ends of the second rotating cylinder are respectively provided with an input port and an output port; and,
the purifier is arranged between the first rotating cylinder and the second rotating cylinder and provided with a chemical purifying cavity, an input port of the purifier is communicated with an output port of the first rotating cylinder, and an output port of the purifier is communicated with an input port of the second rotating cylinder.
2. The purification apparatus of claim 1, wherein the first blades extend helically along the inner circumference of the first rotating cylinder; and/or the presence of a gas in the gas,
the second blade extends spirally along the inner circumference of the second rotary cylinder.
3. The purification apparatus according to claim 2, wherein the pitch of the first blade is gradually decreased in a first direction, which is an extending direction from the input port to the output port of the first rotary cylinder; and/or
And the extending direction from the input port to the output port of the second rotary cylinder is taken as a second direction, and the pitch of the second blade is gradually increased along the second direction.
4. The purification apparatus of claim 3, wherein the first and/or second blades are arranged in a radial spiral; or,
the first and/or second vanes are three-dimensional scroll vanes.
5. The purification apparatus of claim 1, wherein a heating wire and a heat reflecting mirror are disposed within the purifier, the heat reflecting mirror forming the chemical purification chamber around the heating wire.
6. The purification device of claim 5, wherein the port of the chemical purification chamber is provided with an electrically controlled valve plate for controlling the flow rate of fluid through the port;
the electric control valve plate comprises a fixing plate and an adjusting plate, wherein at least one through hole is formed in each of the fixing plate and the adjusting plate, the fixing plate is fixedly arranged on the port of the chemical purification cavity, and the adjusting plate is movably covered on the fixing plate;
when the adjusting sheet rotates to the calibration position, the through hole in the adjusting sheet is communicated with the through hole in the fixing sheet.
7. The purification apparatus of claim 3, wherein the first rotating cylinder is a conical cylinder;
the taper of the first rotary cylinder is gradually increased along the first direction.
8. The purification apparatus of claim 1, wherein the side wall of the second rotary cylinder is a filter screen;
the outer cover of the second rotary cylinder is sleeved with an outer cover, a water spraying unit is arranged on the outer cover, and a spray head of the water spraying unit faces the filter screen.
9. The purification device according to any one of claims 1 to 8, further comprising a biased rotary motor for driving the first and/or second rotary cylinder.
10. The purification apparatus of claim 1, wherein the purifier is provided with a physical purification chamber;
the input port of the physical purification cavity is communicated with the output port of the first rotary cylinder, the output port of the physical purification cavity is communicated with the input port of the chemical purification cavity, and the output port of the chemical purification cavity is communicated with the input port of the second rotary cylinder.
11. A fluid treatment system comprising a purification apparatus as claimed in any one of claims 1 to 10.
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| CN201810532375.0A CN108722152A (en) | 2018-05-29 | 2018-05-29 | A kind of purifier and fluid handling system |
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