CN103464016B - The device that a kind of jet group rapidly and efficiently dissolved oxygen processes - Google Patents
The device that a kind of jet group rapidly and efficiently dissolved oxygen processes Download PDFInfo
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- CN103464016B CN103464016B CN201310313675.7A CN201310313675A CN103464016B CN 103464016 B CN103464016 B CN 103464016B CN 201310313675 A CN201310313675 A CN 201310313675A CN 103464016 B CN103464016 B CN 103464016B
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Abstract
nullIt is an object of the invention to provide the method and device that a kind of jet group rapidly and efficiently dissolved oxygen processes，The jet group that it is made up of multiple ejectors，So oxygen is entered in jet group by multiple inlet ports，Thus，Greatly add suction force and well solve fluid from fluid intake entrance container，By the circulating pump in circulation line by fluid by the fluid loop exit sucking-off of container，Sprayed by the fluid loop head of container again，It is injected in jet dish，Siphon principle is used by the ejector in jet dish，Mixing tube is entered by Oxygen tube oxygen intake，So circular flow，Make the fluid in container and oxygen abundant、Efficiently、Quickly dissolve，Flowed out by hyperoxia fluid issuing again，Thus obtain hyperoxia fluid，The present invention makes up only with an ejector suction force、The phenomenon that dissolution velocity is substantially not enough，Effect when being used especially in the dissolved oxygen needing big flow becomes apparent from，Should be energetically in fluid dissolved oxygen technology penetration and promotion.
Description
Technical field:
The present invention relates to the method that a kind of jet group rapidly and efficiently dissolved oxygen processes, oxygen is inhaled by it according to jet siphon principle
In the different fluid entered, make the abundant rapid solution of oxygen in a fluid, be the side of a kind of jet group rapidly and efficiently dissolved oxygen process
Method and device, it is adaptable to the fluid such as water, liquid is carried out the technical field of quick dissolved oxygen process.
Background technology:
Along with the fast development of society, the progress of science and technology, magnetic energy is all widely used in all trades and professions, especially at fluid
Quickly the scientific and technological achievement in terms of dissolved oxygen process emerges in an endless stream especially.The fluidic oxygen-dissolving apparatus of Chinese patent: CN02240746.4, it is special
Levy and be: it is made up of compressed-air atomizer (1), trocar sheath (2), feed liquid suction tube (3) and gas-liquid mixed nozzle (4), institute
State one end bore of compressed-air atomizer (1) gradually to contract, and closing in end extends a cervical region, this compressed-air atomizer
(1) head of trocar sheath (2) it is plugged in；The tail end bore of trocar sheath (2) the most gradually to contract, this end end and gas-liquid mixed
Nozzle (4) one end is docked, and the other end bore of gas-liquid mixed nozzle (4) gradually expands outwardly；Outside liquid material suction tube (3) is arranged at
On the sidewall of sleeve pipe (2), and communicate with trocar sheath (2).A kind of jet aerator of CN201220267477.2, a kind of jet exposes
Mechanism of qi, it is characterised in that: include water pump, the aerator being connected with water pump and suction nozzle；Described aerator includes induction chamber, spray
Mouth, trunnion and anemostat；Described water pump is connected with nozzle, and described nozzle is positioned at induction chamber, and described induction chamber connects trunnion,
Described trunnion connects anemostat；Described induction chamber be arranged over air entry, air entry is connected with suction nozzle.
The micro-nano jet aerator of CN201020608052.4 is characterized in that: micro-nano jet aerator, has submersible sewage pump, jet
Device, submersible sewage pump is arranged in pump box, and is fixed on equipment frame, and submersible sewage pump is sprayed by the jet of corrugated tube connection ejector
Mouth, air inlet pipe connects in ejector side, and ejector jet pipe connects at the ejector port of export, it is characterised in that: micro-nano gas
Bubble generator is connected on ejector jet pipe by micro-nano emitting bubbles pipe.The jet of Chinese patent: CN87214816 increases
Oxygen machine, this utility model provides a kind of Jet-flow oxygen increasing machine, it is adaptable to aquaculture and wine-making industry etc., it is by water pump, liquid
Jet flow element and some pipelines form, and water pump can be laid on the ground, put hydraulic jets element under water, hydraulic jets element
On have a breather, air from breather be inhaled into jet mixing after, with the shape of taper flow in underwater with certain pressure
Power ejects with speed, makes the oxygen in air can contact with water fully and be gradually dissolved in water, reaches the mesh of oxygen supplement
's.This device has that simple in construction, oxygen supplement speed is fast, little power consumption, low cost, feature easy to use.Chinese patent:
The high-efficient fluidic automatic aerotor of CN200520088739.9, the open a kind of high-efficient fluidic automatic aerotor of this utility model, including tube elements
With conical nozzle element, it is characterised in that the entrance point of described tube elements is provided with the water inlet being connected with water inlet pipe, inner chamber sets
Have to be fixedly connected the female thread of conical nozzle, and side pipe wall is provided with the air inlet pipe of the extended water surface, the port of export of tube elements
For gas-vapor mix district, described conical nozzle element is provided with the external screw thread can being fixedly connected with described female thread；This utility model
There is simple in construction, easily manufactured, with low cost, and have good oxygen supplement performance.
, but foregoing invention simply uses an ejector, and its suction force is the most not enough, especially needs the molten of big flow
Seem that deficiency hinders fluid dissolved oxygen technology penetration and promotion especially when solving oxygen.
Summary of the invention:
It is an object of the invention to provide the method and device that a kind of jet group rapidly and efficiently dissolved oxygen processes, it is to be penetrated by multiple
The jet group of stream device composition, such oxygen is entered in jet group by multiple inlet ports, thus, greatly add suction force fine
The fluid that solves enter container from fluid intake, by the circulating pump in circulation line, fluid is circulated by the fluid of container
Outlet sucking-off, then sprayed by the fluid loop head of container, it is injected in jet dish, the ejector in jet dish uses siphon
Principle, enters mixing tube, such circular flow so that fluid and oxygen in container are abundant, high by Oxygen tube oxygen intake
Imitate, quickly dissolve, then flowed out by hyperoxia fluid issuing, thus obtain hyperoxia fluid,
It is an object of the invention to have employed what following structure realized: by container enclosure, Oxygen tube, mixing tube, ejector
Conduit, ejector, jet dish, jet dish cover, circulation line, circulating pump, fluid oxyty display instrument, fluid level meter group
Become；Container enclosure use sludge proof stainless steel material, container enclosure one end weld oxygen inlet port joint, other end with
Soldered Oxygen tube, mixing tube, ejector conduit, install the jet dish of ejector, welded fluid loop head joint
The device of jet dish cover weld, and weld fluid intake joint, hyperoxia fluid in the corresponding position of container enclosure periphery
Outlet connection, fluid oxyty display instrument port connections, fluid loop exit joint, fluid level meter port connections；To connect
One end of the circulation line of good circulating pump is connected with fluid loop exit joint, and the other end is recycled into the fluid on jet dish cover
Mouth joint connects；Fluid oxyty display instrument is arranged at the fluid oxyty display instrument port connections of container enclosure；
Fluid level meter is arranged at fluid level meter port connections；Oxygen tube, mixing tube, ejector conduit use sludge proof not
Rust steel tubing, Oxygen tube selects diameter at 5 to 12 millimeters, and wall thickness selects at 0.8 to 2 millimeter, and length selects at 60 to 600 millis
Rice, curves one end of Oxygen tube 90 degree or is welded into the one of which of 90 degree；Mixing tube select diameter at 10 to 20 millimeters, wall
Thick selection is at 1 to 2 millimeter, and length selects at 10 to 60 millimeters；Ejector conduit selects diameter at 16 to 35 millimeters, and wall thickness selects
At 1 to 3 millimeter, length selects consistent with ejector length, and holes in ejector conduit circumferential surface centre, and aperture is selected
Select at 3 to 8 millimeters, the Oxygen tube curving 90 degree or the one of which that is welded into 90 degree is welded with ejector conduit, Oxygen tube
Pore must be interconnected with the boring of ejector conduit circumferential surface centre；Jet dish uses sludge proof stainless steel tube
Material, jet dish selects diameter at 20 to 300 millimeters, and wall thickness selects at 1 to 3 millimeter, and length selects longer by 10 than ejector conduit
To 20 millimeters, the welding of the stainless steel materials of one end of jet dish material identical with jet dish, sheet material size select with jet dish
Diameter is consistent, and sheet metal thickness selects consistent with jet dish wall thickness, and bores macropore and aperture on sheet material, and macropore diameter size is selected
Selecting less than ejector catheter diameter 3 to 6 millimeters, small aperture selects consistent at the external diameter with Oxygen tube, and drilling hole amount selects
At 2 to 30, macropore is consistent with the quantity of aperture；Mixing tube is welded to jet plate material outer end, must with the macropore on sheet material
Must be interconnected；Being welded with jet plate material the inner with ejector conduit tube component by the Oxygen tube welded, Oxygen tube must be worn
Small holes, ejector conduit must be interconnected with the macropore on sheet material；Ejector employing oxidation resistant material: rustless steel, plastics
One of which, ejector is filled in a specified direction in ejector conduit, the hole on ejector circumferential surface must be with suction
The endoporus connection of oxygen pipe；Jet dish cover uses sludge proof stainless steel material, be fabricated to hemispherical, wherein the one of polygon arch
Kind, jet dish cover outer diameter is consistent with container enclosure external diameter, and holes on jet dish cover, and pore size selects 12 to 50
Millimeter, by weld to jet dish cover drill hole, coupler bore must connect with the boring of jet dish cover；Jet dish cover and container
The one of which of the method being connected by welding, screw thread, Flange joint of outer housing；Fluid circulating line uses sludge proof stainless
Steel tubing, the one of which of sludge proof plastic pipe, flowed out from fluid loop exit by fluid, fluid loop head enter
Specific direction, in fluid circulating line connect circulating pump, pipeline is connected by the method for welding, screw thread, Flange joint
One of which.Joint is female thread, external screw thread, flange resistance to oxidation rustless steel hot-water heating part.Outside fluid oxyty display instrument uses
Purchasing the fluid oxyty display instrument matched with fluid, be necessary for oxidation resistant material with hyperoxia fluid contact position, it connects
Use the one of which of the method for screw thread, Flange joint；Fluid level meter uses the fluid level meter that outsourcing matches with fluid,
Being necessary for oxidation resistant material with hyperoxia fluid contact position, it is connected by the one of which of method of screw thread, Flange joint；Circulation
Pump uses the circulating pump machine that outsourcing matches with fluid, and is necessary for oxidation resistant material with hyperoxia fluid contact position；
Due to the fact that and use the device of said structure to make installation simple, cheap, easily it is easily accepted by a user, facilitates general
And promote.
Accompanying drawing illustrates:
The present invention is further described with embodiment below in conjunction with the accompanying drawings:
Fig. 1 is that a kind of jet group rapidly and efficiently dissolved oxygen processing means of the present invention implements schematic diagram.
Fig. 2 is Figure 1A-A profile, and a kind of jet group rapidly and efficiently dissolved oxygen processing means of the main display present invention is implemented
Structural profile schematic diagram.
Fig. 3 is axonometric drawing, main the display Oxygen tube of jet group, mixing tube, jet dish, jet dish cover region of interest.
In figure: 1, oxygen inlet port, 2, Oxygen tube, 3, mixing tube, 4, ejector, 5, jet dish, 6, jet dish cover, 7A,
Fluid loop head, 7B, fluid loop exit, 8, container enclosure, 9, fluid intake, 10, hyperoxia fluid issuing, 11, fluid molten
Oxygen concentration display instrument, 12, ejector conduit, 13, fluid circulation tubes, 14, circulating pump, 15 fluid level meters.
Detailed description of the invention:
Process and the embodiment of manufacture method with reference to the quick dissolved oxygen of a kind of jet group that Fig. 1 is the present invention: high-oxygen water is fast
The structural representation of speed oxygen-dissolving apparatus, it is illustrated that be the profile of 6 groups of jet group installations, by oxygen inlet port-1, Oxygen tube-2, mix
Conjunction pipe-3, ejector-4, jet dish-5, jet dish cover-6, fluid loop head-7A, fluid loop exit-7B, container enclosure-
8, fluid intake-9, hyperoxia fluid issuing-10, fluid oxyty display instrument-11, ejector conduit-12, fluid circulation tubes-
13, circulating pump-14, fluid level meter-15 forms, the present embodiment use bore 6 macropores on jet dish-5 end face sheet material and 6 little
Hole, is welded to mixing tube-3 fluid dish-5 outside, Oxygen tube-2 and ejector conduit-12 is welded, Oxygen tube-2 interior
Hole must connect with the hole on ejector conduit-12 periphery, then by little through on jet dish-5 end face sheet material of Oxygen tube-2
Hole, is welded to fluid dish-5 ejector conduit-12 internal, then Oxygen tube-2 and jet dish-5 are welded, and is filled in by ejector-4
In incident flow device conduit-12, the hole on ejector-4 periphery must be with the endoporus of Oxygen tube-2 and ejector conduit-12 circumference
Hole connection on face, is carried out the soldered jet dish cover-6 of fluid loop head-7A joint with the other end of jet dish-5
Welding, then the container enclosure-8 having welded oxygen inlet port-1 joint is welded with jet dish cover-6, by dense for fluid dissolved oxygen
Degree display instrument-11 is installed to the position that container enclosure-8 is specified, and according to fluid loop direction, circulating pump is arranged on fluid circulation
In fluid circulation tubes-13 between entrance-7A and fluid loop exit-7B.Oxygen inlet port-1 joint, fluid loop head-
7A joint, fluid loop exit-7B joint, fluid intake-9 joint, hyperoxia fluid issuing-10 joint, fluid oxyty are aobvious
Show that instrument-11 joint, fluid level meter-15 joint are respectively adopted 4 external threads joints of resistance to oxidation stainless steel standard；Oxygen tube-2
Use external diameter 6 millimeters, wall thickness 0.8 millimeter, the resistance to oxidation stainless steel tube of length 180 millimeters；Mixing tube-3 employing external diameter 12 millimeters,
Wall thickness 1 millimeter, the resistance to oxidation stainless steel tube of length 60 millimeters；Ejector-4 uses external diameter 16 millimeters, the oxytolerant of length 48 millimeters
Change plastic production；Ejector conduit-12 uses external diameter 18.4 millimeters, wall thickness 1.2 millimeters, the resistance to oxidation rustless steel of length 50 millimeters
Pipe；Jet dish-5 uses external diameter 89 millimeters, wall thickness 1.5 millimeters, the resistance to oxidation stainless steel tube of length 60 millimeters, jet dish-5 end face
Circumferentially 6 macropores, 10 millimeters of aperture, 6 apertures, 6.1 millimeters of aperture are bored in arrangement；Jet dish cover-6 employing external diameter 89 millimeters,
The resistance to oxidation rustless steel hemisphere of wall thickness 1.5 millimeters, the boring of hemisphere top, bore dia 16 millimeters, hemisphere external diameter position welding ring circle,
Ring internal diameter 89 millimeters, external diameter 102 millimeters, thickness 1.5 millimeters；Container enclosure-8 uses external diameter 102 millimeters, wall thickness 1.5 millimeters,
The resistance to oxidation stainless steel tube of length 200 millimeters, the boring of container enclosure-8 end face, bore dia 16 millimeters, container enclosure-8 circumference refers to
Determining position and bore fluid loop exit-7B, fluid intake-9, hyperoxia fluid issuing-10, fluid oxyty display instrument-11 is installed
Hole, aperture is respectively adopted 16 millimeters；Fluid circulation tubes-13 uses external diameter 20 millimeters, the resistance to oxidation stainless steel tube of wall thickness 2 millimeters,
In order to effect is attractive in appearance, outer surface is processed by shot blasting.
Claims (5)
1. the device that jet group rapidly and efficiently dissolved oxygen processes, is characterized in that: oxygen is sucked by it according to jet siphon principle
In different fluid, the jet group that it is made up of multiple ejectors, thus it is greatly improved oxygen dissolved, make oxygen the fastest
Instant solution in a fluid, needs to use oxygen to be entered in container by oxygen inlet port, and fluid enters container from fluid intake, logical
Cross the circulating pump in circulation line by fluid by the fluid loop exit sucking-off of container, then sprayed by the fluid loop head of container
Go out, be injected in jet dish, the ejector in jet dish use siphon principle, enter mixing by Oxygen tube oxygen intake
Pipe, such circular flow so that fluid in container and oxygen fully, efficiently, quickly dissolve, then by hyperoxia fluid issuing stream
Go out；By container enclosure, Oxygen tube, mixing tube, ejector conduit, jet dish, jet dish cover, circulation line, circulating pump, it be by
The jet group of multiple ejectors composition, fluid oxyty display instrument, fluid level meter composition；Container enclosure uses sludge proof
Stainless steel material, welds oxygen inlet port joint in container enclosure one end, other end and soldered Oxygen tube, mixing tube,
Ejector conduit, the jet dish installing ejector, the device of jet dish cover that welded fluid loop head joint weld
Connect, and show in container enclosure periphery corresponding position welding fluid intake joint, hyperoxia fluid outlet connection, fluid oxyty
Show instrument port connections, fluid level meter port connections, fluid loop exit joint；One end of the circulation line of circulating pump will be connected
Being connected with fluid loop exit joint, the other end is connected with the fluid loop head joint on jet dish cover.
The device that a kind of jet group rapidly and efficiently dissolved oxygen the most according to claim 1 processes, is characterized in that: Oxygen tube, mixed
Close pipe, ejector conduit uses sludge proof stainless steel pipe, and Oxygen tube selects diameter at 5 to 12 millimeters, and wall thickness selects 0.8
To 2 millimeters, length selects at 60 to 600 millimeters, one end of Oxygen tube curves 90 degree or is welded into the one of which of 90 degree；Mixed
Closing pipe selects diameter at 10 to 20 millimeters, and wall thickness selects at 1 to 2 millimeter, and length selects at 10 to 60 millimeters；Ejector conduit selects
Selecting diameter at 16 to 35 millimeters, wall thickness selects at 1 to 3 millimeter, and length selects consistent with ejector length, and at ejector conduit
Holing in circumferential surface centre, aperture selects at 3 to 8 millimeters, will curve 90 degree or is welded into the suction of one of which of 90 degree
Oxygen pipe welds with ejector conduit, and Oxygen tube pore must be interconnected with the boring of ejector conduit circumferential surface centre.
The device that a kind of jet group rapidly and efficiently dissolved oxygen the most according to claim 1 processes, is characterized in that: jet dish uses
Sludge proof stainless steel pipe, jet dish selects diameter at 20 to 300 millimeters, and wall thickness selects at 1 to 3 millimeter, and length selects
Longer 10 to 20 millimeters than ejector conduit, the stainless steel materials welding of one end of jet dish material identical with jet dish, sheet material is big
Little selection is consistent with jet dish diameter, and sheet metal thickness selects consistent with jet dish wall thickness, and brill macropore and little on sheet material
Hole, macropore diameter size selects less than ejector catheter diameter 3 to 6 millimeters, and small aperture selects at the external diameter with Oxygen tube
Unanimously, drilling hole amount selects at 2 to 30, and macropore is consistent with the quantity of aperture；Mixing tube is welded to jet plate material outer end,
Must be interconnected with the macropore on sheet material；The Oxygen tube welded is welded with jet plate material the inner with ejector conduit tube component
Connecing, Oxygen tube has to pass through aperture, and ejector conduit must be interconnected with the macropore on sheet material.
The device that a kind of jet group rapidly and efficiently dissolved oxygen the most according to claim 1 processes, is characterized in that: ejector uses
Oxidation resistant material: rustless steel, the one of which of plastics, fills in ejector in ejector conduit, ejector in a specified direction
Hole on circumferential surface must connect with the endoporus of Oxygen tube.
The device that a kind of jet group rapidly and efficiently dissolved oxygen the most according to claim 1 processes, is characterized in that: jet dish cover is adopted
Use sludge proof stainless steel material, be fabricated to hemispherical, the one of which of polygon arch, outside jet dish cover outer diameter is with container
Cover external diameter is consistent, and holes on jet dish cover, and pore size selects at 12 to 50 millimeters, by fluid loop head weld
To jet dish cover drill hole, fluid loop head coupler bore must connect with the boring of jet dish cover；Outside jet dish cover is with container
The one of which of the method being connected by welding, screw thread, Flange joint of cover.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310313675.7A CN103464016B (en) | 2013-07-24 | 2013-07-24 | The device that a kind of jet group rapidly and efficiently dissolved oxygen processes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310313675.7A CN103464016B (en) | 2013-07-24 | 2013-07-24 | The device that a kind of jet group rapidly and efficiently dissolved oxygen processes |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103464016A CN103464016A (en) | 2013-12-25 |
| CN103464016B true CN103464016B (en) | 2016-12-28 |
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| CN201310313675.7A Active CN103464016B (en) | 2013-07-24 | 2013-07-24 | The device that a kind of jet group rapidly and efficiently dissolved oxygen processes |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104525012B (en) * | 2015-01-09 | 2016-05-25 | 赵卓维 | Gas-liquid or liquid liquid mixing nano-bubble generating apparatus |
| CN105441950A (en) * | 2015-02-13 | 2016-03-30 | 叶涛 | Regeneration and recycling technology for acid copper chloride etching waste liquid |
| CN106119852B (en) * | 2015-08-31 | 2019-09-03 | 叶旖婷 | A kind of electrolytic recovery and regeneration technology of acid copper chloride etching liquid |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203007003U (en) * | 2012-07-30 | 2013-06-19 | 西藏创源水资源科技有限责任公司 | Nonelectric equipment for producing high-oxygen water |
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2013
- 2013-07-24 CN CN201310313675.7A patent/CN103464016B/en active Active
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203007003U (en) * | 2012-07-30 | 2013-06-19 | 西藏创源水资源科技有限责任公司 | Nonelectric equipment for producing high-oxygen water |
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| CN103464016A (en) | 2013-12-25 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Application publication date: 20131225 Assignee: Foshan Guozhong Intelligent Technology Engineering Co. Ltd. Assignor: Zhu Zhenai|Huang Guangzhi Contract record no.: 2014440000179 Denomination of invention: Apparatus for rapid high-efficiency dissolution of oxygen through jet group License type: Common License Record date: 20140423 |
|
| LICC | Enforcement, change and cancellation of record of contracts on the licence for exploitation of a patent or utility model | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20161118 Address after: Three, No. six, building 13, building No. 528000, Renmin West Road, Chancheng District, Guangdong, Foshan Applicant after: Foshan Guozhong Intelligent Technology Co Ltd Address before: 528251 Guangdong Province Nanhai District of Foshan City, Guicheng City Taihe garden in North D101 Plaza. Applicant before: Zhu Zhenai Applicant before: Huang Guangzhi |
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| C14 | Grant of patent or utility model | ||
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