CN201375881Y - Fluid pressure difference type nano grinding installation - Google Patents
Fluid pressure difference type nano grinding installation Download PDFInfo
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- CN201375881Y CN201375881Y CN200920005735U CN200920005735U CN201375881Y CN 201375881 Y CN201375881 Y CN 201375881Y CN 200920005735 U CN200920005735 U CN 200920005735U CN 200920005735 U CN200920005735 U CN 200920005735U CN 201375881 Y CN201375881 Y CN 201375881Y
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Abstract
The utility model relates to a fluid pressure difference type nano grinding installation, which comprises a feeding tank, a discharge pipe, a liquid-supplying unit, a gas-supplying unit, an equalizer and a post-processor; wherein the discharge pipe is connected with the feeding tank; the liquid-supplying unit and the gas-supplying unit are communicated with the discharge pipe; a booster pump is arranged on the discharge pipe; the equalizer consists of a pressure-equalizing cylinder, a pressurized feeding pipe, a gas-liquid separator, a pressure meter and at least one nano grinder; the pressurized feeding pipe is connected with the pressure-equalizing cylinder, and is communicated with the discharge pipe; the nano grinder is connected with the feeding tank through a return pipe; and the post-processor is connected with the nano grinder. The utility model can ensure that substances can be uniformly mixed.
Description
Technical field
A kind of fluid differential-pressure type nanometer grinding device of the utility model, especially a kind of mode of utilizing high pressure to grind can fully mix solid or gas with fluid fluid differential-pressure type nanometer grinding device.
Background technology
In human lives's environment, difference because of temperature, and allow material present gaseous state, liquid state or three solid-state phase change, at normal temperatures, the material of gaseous state comprises element and compound etc., and liquid material also includes element and compound, and the solubility between element and the compound, between organic matter and the inorganic matter, between gas and the liquid, between liquid and the solid all can produce difference because of the different of the variation of phase and physical property, so increase its mutual solubility, then certainly will or use specific instrument to assist and just can finish with external force.
Present employed method utilizes pressing mode to promote solubility between the two-phase material mostly, pressed powder is dissolved in the liquid, or gas is dissolved in the liquid, yet, there is no instrument at present can be when being dissolved in pressed powder liquid or gas is dissolved in liquid, with pressed powder or gas nanometer, and it is dispersed in the liquid, so still have necessity of exploitation.
Summary of the invention
The inventor is any with pressed powder or gas nanometer in view of there is no at present, so that it is dispersed in the device in the liquid, therefore through after constantly studying and testing, invents out this fluid differential-pressure type nanometer grinding device finally.
The purpose of this utility model is to provide a kind of mode of utilizing high pressure to grind to make solid or the abundant fluid differential-pressure type nanometer grinding device that mix with fluid of gas energy.
For reaching above-mentioned purpose, fluid differential-pressure type nanometer grinding device of the present utility model, it comprises:
One raw material feed well, it is communicated with a feed pipe, and is connected with a raw material discharge nozzle, and this raw material discharge nozzle is provided with a pressurization pumping;
One liquid supplying unit, it is communicated in this raw material discharge nozzle;
One gas supply unit, it is communicated in this raw material discharge nozzle;
One pressure-equalizing device, it comprises an equal pressure cylinder, a pressurization material feeding tube, a gas-liquid separator, a Pressure gauge, at least one nano-milled device, one end of this pressurization material feeding tube is connected in this equal pressure cylinder, and be communicated with this raw material discharge nozzle, this equal pressure cylinder of this gas-liquid separator setting, and be communicated with this equal pressure cylinder, this Pressure gauge is arranged at this equal pressure cylinder, this nano-milled device is arranged at this equal pressure cylinder, and is communicated with this equal pressure cylinder, and is connected to this raw material feed well with a return duct;
One equipment for after-treatment, it is connected in this nano-milled device.
Wherein, the pipeline that connects each element all can be provided with valve, to control the operation of this fluid differential-pressure type nanometer grinding device.Preferably, this return duct is provided with a magnetic valve.
Preferably, the feed pipe of this raw material feed well is communicated in place, the nearly top of this raw material feed well, and the raw material discharge nozzle of this raw material feed well is arranged at the bottom of this raw material feed well.
Preferably, this liquid supplying unit is connected to this raw material discharge nozzle with a liquid additive pipe, and this liquid additive pipe is provided with a fluid flowmeter.
Preferably, this gas supply unit comprises at least one gas bomb, and its quantity can decide according to required gas flow, and the kind of gas also decides according to the gas that institute's desire is mixed; Wherein, this gas supply unit is connected to this raw material discharge nozzle with a gas additive pipe, and this gas additive pipe is provided with a gas flowmeter.
Wherein, the bottom of this equal pressure cylinder is provided with a raw material pan feeding joint, to be connected with an end of this pressurization material feeding tube.
Preferably, this gas-liquid separator is arranged at the top of this equal pressure cylinder, and this pressure-equalizing device comprises one first nano-milled device and one second nano-milled device, this first nano-milled device and this second nano-milled device then are arranged at the side of this equal pressure cylinder, and can be the subtend setting, this return duct is communicated in this first nano-milled device, and this equipment for after-treatment is connected in this second nano-milled device.
Wherein, this equipment for after-treatment comprises a bottling machine, and it is connected with this nano-milled device by a bottling feeding pipe, and this bottling feeding pipe is provided with a magnetic valve.
Wherein, this equipment for after-treatment comprises a release of pressure groove, and its bottom is provided with a release of pressure delivery pipe, and this release of pressure groove is connected in this nano-milled device with a release of pressure groove feeding pipe, and this release of pressure groove feeding pipe is provided with a magnetic valve.
Preferably, this equipment for after-treatment comprise simultaneously above-mentioned bottling machine and this release of pressure groove the two.
Wherein, this raw material feed well supply liquid charging stock, and this liquid supplying unit supply liquid or be added with the liquid of pressed powder, and this gas supply unit supply gas.
Technique effect of the present utility model is, with liquid is primary raw material, in pressure process, add suitable solid, liquid or gas, after nano-milled, make pressed powder nanometer in liquid, and make gas force to dissolve in to produce nano bubble in the liquid, perhaps make inorganic liquid and organic liquid produce emulsion reaction, therefore, the utility model can provide out of phase material mixed uniformly effect.
Description of drawings
Fig. 1 is a pipeline layout drawing of the present utility model;
Fig. 2 is the stereogram of pressure-equalizing device of the present utility model;
Fig. 3 is the plane of pressure-equalizing device of the present utility model;
Fig. 4 is the cross sectional plan view of the nano-milled device of the utility model;
Fig. 5 is the cross sectional plan view of the front portion of the nano-milled device of the utility model;
Fig. 6 is the end-view of the abrasive sheet of the nano-milled device of the utility model;
Fig. 7 is the cross sectional side view that just changes abrasive sheet of the nano-milled device of the utility model;
Fig. 8 is the cross sectional side view of the counter-rotating abrasive sheet of the nano-milled device of the utility model;
Fig. 9 is the cross sectional plan view at the rear portion of the nano-milled device of the utility model.
Description of reference numerals:
10-raw material feed well; The 11-feed pipe; 111,121,122-water valve; 12-raw material discharge nozzle; The 13-pumping of pressurizeing; The 20-liquid supplying unit; 21-liquid additive pipe; The 22-fluid flowmeter; The 30-gas supply unit; 31-gas additive pipe; The 32-gas flowmeter; The 40-pressure-equalizing device; The equal pressure cylinder of 41-; 411-raw material pan feeding joint; The 42-material feeding tube that pressurizes; The 43-gas-liquid separator; The 431-exhaust outlet; The 44-Pressure gauge; The 45-first nano-milled device; The 451-return duct; 4511-mill outlet; The 452-magnetic valve; The 46-second nano-milled device; The 461-hollow shell; 4611a, 4611b-mill outlet; The 4612-near-end; The 4613-far-end; The 4614-fluid intake; The 4615-inner space; 4616-encircles stopper; The 462-lid; The 4621-central perforation; The 463-abrasive sheet; 463a-is just changeing abrasive sheet; The 463b-abrasive sheet that reverses; The 4631-central axis hole; 4632,4632a, 4632b-pod apertures; 464-axis fixed bar; The 4641-body of rod; 4642-first pad; 465-pressure regulation bar; The 4651-body of rod; 4652-second pad; The 4653-spiral tool revolves mouth; The 466-rubber seal; The 467-positioning screw cap; The 468-hold-doun nut; The 50-equipment for after-treatment; The 51-bottling machine; The 52-feeding pipe of bottling; The 521-magnetic valve; 53-release of pressure groove; 54-release of pressure groove feeding pipe; The 541-magnetic valve; 55-release of pressure delivery pipe; The 551-control valve.
The specific embodiment
Please referring to shown in Figure 1, fluid differential-pressure type nanometer grinding device of the present utility model, it comprises a raw material feed well 10, a liquid supplying unit 20, a gas supply unit 30, a pressure-equalizing device 40 and an equipment for after-treatment 50.
Be loaded with liquid charging stock in this raw material feed well 10, and the position at the nearly top of side of this raw material feed well 10 is communicated with a feed pipe 11, this feed pipe 11 is provided with a water valve 111, and the bottom of this raw material feed well 10 is connected with a raw material discharge nozzle 12, and this raw material discharge nozzle 12 is provided with a pressurization pumping 13, and this raw material discharge nozzle 12 is interval with a plurality of water valves 121,122;
This liquid supplying unit 20 is connected to this raw material discharge nozzle 12 with a liquid additive pipe 21, and the position between this raw material feed well 10 and this pressurization pumping 13, and this liquid additive pipe 21 is provided with a fluid flowmeter 22, and this liquid supplying unit 20 can provide liquid or contain the liquid of pressed powder;
This gas supply unit 30 is connected to this raw material discharge nozzle 12 with a gas additive pipe 31, and the position between this raw material feed well 10 and this pressurization pumping 13, and this gas additive pipe 31 is provided with a gas flowmeter 32;
Please add referring to Fig. 2 and shown in Figure 3, this pressure-equalizing device 40 comprises an equal pressure cylinder 41, a pressurization material feeding tube 42 (not shown), a gas-liquid separator 43, a Pressure gauge 44, at least one nano-milled device.In the present embodiment, this pressure-equalizing device 40 comprises one first nano-milled device 45 and one second nano-milled device 46.The bottom of this equal pressure cylinder 41 is provided with a raw material pan feeding joint 411, one end of this pressurization material feeding tube 42 is connected in the raw material pan feeding joint 411 of this equal pressure cylinder 41, and be communicated with this raw material discharge nozzle 12, to allow the fluid in raw material discharge nozzle 12 flow in this equal pressure cylinder 41, this gas-liquid separator 43 is arranged at the top of this equal pressure cylinder 41, and be communicated with this equal pressure cylinder 41, and be provided with an exhaust outlet 431, this Pressure gauge 44 is arranged at this equal pressure cylinder 41, to make operating personnel monitor at any time to adjust the pressure of this pressure-equalizing device 40, this first nano-milled device 45 is arranged at the side of this equal pressure cylinder 41, and be communicated with this equal pressure cylinder 41 and be provided with a mill outlet 4511, this mill outlet 4511 connects a return duct 451, to be connected to the side of this raw material feed well 10, this return duct 451 is provided with a magnetic valve 452, this second nano-milled device 46 also is arranged at the side of this equal pressure cylinder 41, and be communicated with this equal pressure cylinder 41, with with these first nano-milled device 45 subtend settings, and this second nano-milled device 46 is provided with two mill outlet 4611a, 4611b;
Still see also shown in Figure 1, this equipment for after-treatment 50 comprises a bottling machine 51 and a release of pressure groove 53, this bottling machine 51 is connected with this second nano-milled device 46 by a bottling feeding pipe 52, and this bottling feeding pipe 52 is provided with a magnetic valve 521, the bottom of this release of pressure groove 53 is provided with a release of pressure delivery pipe 55, this release of pressure delivery pipe 55 is provided with a control valve 551, and this release of pressure groove 53 is connected in this second nano-milled device 46 with a release of pressure groove feeding pipe 54, and this release of pressure groove feeding pipe 54 is provided with a magnetic valve 541.
The first nano-milled device 45 and the second nano-milled device 46 in this pressure-equalizing device 40 have identical structure, below are that example describes with the second nano-milled device 46 promptly.
Please referring to shown in Figure 4, this second nano-milled device 46 comprises a hollow shell 461, a lid 462, a plurality of abrasive sheet 463 and a pressure regulation bar 465.
Please add referring to shown in Figure 5, this hollow shell 461 is provided with an open proximal end 4612, one open distal end 4613, an at least one mill outlet and a ring stopper 4616, in the present embodiment, this hollow shell 461 is provided with two mill outlet 4611a, 4611b, the near-end 4612 of this hollow shell 461 contacts with this equal pressure cylinder 41 and combination, this two mills outlet is arranged at the side of this hollow shell 461, this ring stopper 4616 is extended internally by the inwall of this hollow shell 461 and in the position of the near-end 4612 of this hollow shell 461, to make this ring stopper 4616 surround being communicated in the fluid inlet 4614 of this equal pressure cylinder 41, and making this ring stopper 4616 and the formed space of far-end of this hollow shell 461 is an inner space 4615, this inner space 4615 and this fluid intake 4614 and this two mills outlet 4611a, 4611b is communicated with;
This lid 462 is arranged at the far-end 4613 of this hollow shell 461, and sealing this far-end 4613, and this lid 462 is provided with a central perforation 4621 that is communicated with this inner space 4615;
Please add referring to shown in Figure 6, these a plurality of abrasive sheets 463 are arranged in this inner space 4615, and and be formed with an expansion space (label does not show) between the inwall of this hollow shell 461, and each abrasive sheet 463 forms a central axis hole 4631 in central authorities, and in these central axis hole 4631 outside annular arrangements and be formed with at interval a plurality of pod apertures 4632, this central axis hole 4631 penetrates for an axis fixed bar 464, this axis fixed bar 464 comprises first pad 4642 that penetrates the body of rod 4641 in this central axis hole 4631 and be vertically installed in the far-end of this body of rod 4641, be the T font with the cross section that makes this axis fixed bar 464, and this first pad 4642 is resisted against the abrasive sheet 463 near this lid 462, and axis horizontal by 0 to 60 degree of the pod apertures 4632 of described abrasive sheet 463, promptly, the pod apertures 4632 of this abrasive sheet 463 is parallel with horizontal plane, perhaps, this abrasive sheet one is just changeing abrasive sheet 463a, its pod apertures 4632a is tilted (as shown in Figure 7) towards this central axis hole 4631 by an end of this fluid intake 4614 direction towards other end, perhaps, this abrasive sheet one counter-rotating abrasive sheet 463b, its pod apertures 4632b is tilted (as shown in Figure 8) by an end of this fluid intake 4614 inwall direction towards the direction of other end towards this hollow shell 461, abrasive sheet 463 with pod apertures 4632 of differing tilt angles can be selected the order of serial connection arrangement according to the fluid difference of desire processing, and when fluid flows through these abrasive sheets 463, this fluid can drive these abrasive sheet 463 rotations and produce abrasive action, and the fluid after grinding can be released in this this expansion space.
Please add referring to shown in Figure 9, this pressure regulation bar 465 penetrates the central perforation 4621 of this lid 462, and this pressure regulation bar 465 comprises second pad 4652 that penetrates the body of rod 4651 in this central perforation 4621 and be vertically installed in the far-end of this body of rod 4651, be the T font with the cross section that makes this pressure regulation bar 465, this body of rod 4651 comprises that one is arranged at the near-end of the inner space 4615 of this hollow shell 461, one is arranged at the far-end in the outside of this hollow shell 461, at least one rubber seal 466 that is arranged in this central perforation 4621 and is located on these body of rod 4651 outsides, it is other and be located on the hold-doun nut 468 in these body of rod 4651 outsides that one positioning screw cap 467 and that is arranged at these lid 462 outsides and is located on these body of rod 4651 outsides is arranged at this positioning screw cap 467, this far-end is formed with a spiral tool and revolves mouth 4653, inserting this spiral tool for a spiral tool revolves mouth 4653 and rotates and adjust this pressure regulation bar 465, and this second pad 4652 is arranged at the near-end of this body of rod 4651, support this first pad 4642 of pulling in this inner space 4615 to be positioned over, adjusting the tight ness rating between these abrasive sheets 463, and produce in various degree grinding effect.
The utility model is when using, liquid charging stock in the raw material feed well 10 is sent into this raw material discharge nozzle 12, and send in this pressurization material feeding tube 42 by this pressurization pumping 13, again in this raw material pan feeding joint 411 is sent to this equal pressure cylinder 41, and this liquid charging stock is sent back in this material feeding tube 11 via the mill discharge nozzle 4511 and the return duct 451 of this first nano-milled device 45, to keep circulation, owing to may contain tiny organic matter in the liquid charging stock, therefore liquid charging stock evenly can be disperseed via this first nano-milled device 45.
Afterwards, again from this liquid supplying unit 20 or gas supply unit 30 supply liquid, solid or gas are to this raw material discharge nozzle 12, be mixed into a fluid-mixing with liquid charging stock, and this fluid-mixing is sent in this equal pressure cylinder 41 through this pressurization material feeding tube 42 again, and before entering this second nano-milled device 46, as if the gas that surplus is arranged gas is overflowed by this exhaust outlet 431 in this fluid-mixing, the fluid intake 4614 that enters by this second nano-milled device 46 of this fluid-mixing enters in this second nano-milled device 46 afterwards, can adjust this pressure regulation bar 465 this moment according to this Pressure gauge 44, to control the tight ness rating between the described abrasive sheet 463, make the pod apertures 4632 of this fluid-mixing by described abrasive sheet 463, and drive 463 rotations of described abrasive sheet, and the effect that generation is ground, and the fluid-mixing after grinding is released into this expansion space, and send in this release of pressure groove 53 via this release of pressure groove feeding pipe 54 by a mill outlet 4611a wherein, to treat follow-up utilization; Perhaps, adjust suitable bottling pressure, fluid-mixing is filled in this bottling machine 51 by this bottling feeding pipe 52, to carry out the pressure filling and to seal supervisor by another mill outlet 4611a according to this Pressure gauge 44.
Raw material feed well 10 employed raw materials of the present utility model are liquid, and make whole fluid differential-pressure type nanometer grinding device can be divided into gas-liquid systems, solid-liquid system and liquid liquid systems according to purposes.
Gas-liquid systems: employed gas comes from this gas supply unit 30, can comprise but be not limited in air, nitrogen, oxygen, ozone, hydrogen, carbon monoxide, carbon dioxide, sulfur dioxide, nitrogen dioxide etc., as in waste water, dissolving in an amount of air and agglutinant, the micro-bubble that utilization disengages at high pressure, impurity in the waste water is removed by air is floating, most COD in the removable waste water, BOD and solid suspension etc., processing can add ozone as running water, beverage and drinks can add nitrogen to reach fresh-keeping effect, add oxygen in the mineral water so that oxygen content to be provided, add ozone or oxygen in the bathing pool, usefulness adding sulfur dioxide or ozone for industrial bleaching, culture and add oxygen in the water to promote dissolved oxygen amount etc.
Solid-liquid system: add an amount of pressed powder in the liquid in liquid supplying unit 20, it is transported in the raw material discharge nozzle 12, drive nano-milled device and pressed powder is ground to form nano level powder by mixed fluid, afterwards via obtaining finished product after dehydrating, for example but be not limited in algae, pollen can by grind and rapidly the release of pressure process reach breaking-wall cell and nanometer; Fineness as ceramic raw material is ground; As the emulsification of organic additive in the cosmetics and detailed-oriented etc.
The liquid liquid systems: one of them comes from this raw material feed well 10 employed liquid, another is promptly from this liquid supplying unit 20, for example but be not limited in organic oils and add an amount of water or organic solvent (profit dissolves each other), make the limited material of solubility, dissolve in mutually with convenient use by nano-milled device of the present utility model, as dissolving in water in the fuel oil, can increase efficiency of combustion, reduce air pollution; Exotic fuels add ethanol; Low calorie fuels alcohol adds the high heating value wet goods.
Therefore, the material that the utility model can mix is extensive, and can supply provides various industry utilizations, thus have industry applications, and the whence is to propose the utility model patent application.
The above specific embodiment only is preferred embodiment of the present utility model, and it is illustrative for the utility model, and nonrestrictive.Those skilled in the art carries out conversion, modification even equivalence to it under the situation that does not exceed the utility model spirit and scope, these changes all can fall into claim protection domain of the present utility model.
Claims (10)
1. a fluid differential-pressure type nanometer grinding device is characterized in that, comprising:
One raw material feed well, it is communicated with a feed pipe, and is connected with a raw material discharge nozzle, and this raw material discharge nozzle is provided with a pressurization pumping;
One liquid supplying unit, it is communicated in this raw material discharge nozzle;
One gas supply unit, it is communicated in this raw material discharge nozzle;
One pressure-equalizing device, it comprises an equal pressure cylinder, a pressurization material feeding tube, a gas-liquid separator, a Pressure gauge, at least one nano-milled device, one end of this pressurization material feeding tube is connected in this equal pressure cylinder, and be communicated with this raw material discharge nozzle, this gas-liquid separator is arranged at this equal pressure cylinder, and is communicated with this equal pressure cylinder, this Pressure gauge is arranged at this equal pressure cylinder, described nano-milled device is arranged at this equal pressure cylinder, and is communicated with this equal pressure cylinder, and is connected to this raw material feed well with a return duct;
One equipment for after-treatment, it is connected in this nano-milled device.
2. fluid differential-pressure type nanometer grinding device as claimed in claim 1 is characterized in that, described each nano-milled device comprises:
One hollow shell, it is provided with an open proximal end, one open distal end, an at least one mill outlet and a ring stopper, the near-end of this hollow shell contacts with this equal pressure cylinder and combination, this mill outlet is arranged at the side of this hollow shell, this ring stopper is extended internally by the inwall of this hollow shell and in the position of the near-end of this hollow shell, to make this ring stopper surround being communicated in the fluid inlet of this equal pressure cylinder, and the formed space of the far-end that makes this ring stopper and this hollow shell is an inner space, and this inner space is communicated with this fluid intake and described mill outlet;
One lid, it is arranged at the far-end of this hollow shell, and sealing this far-end, and this lid is provided with a central perforation that is communicated with this inner space;
A plurality of abrasive sheets, it is arranged in this inner space, and and be formed with an expansion space between the inwall of this hollow shell, and each abrasive sheet forms a central axis hole, and in the outside annular arrangement of this central axis hole and be formed with a plurality of pod apertures at interval, this central axis hole penetrates for an axis fixed bar, this axis fixed bar comprises first pad that penetrates the body of rod in this central axis hole and be vertically installed in the far-end of this body of rod, be the T font with the cross section that makes this axis fixed bar, and this first pad is resisted against the abrasive sheet near this lid;
One pressure regulation bar, it penetrates the central perforation of this lid, and this pressure regulation bar comprises second pad that penetrates the body of rod in this central perforation and be vertically installed in the far-end of this body of rod, be the T font with the cross section that makes this pressure regulation bar, this body of rod comprises that one is arranged at the near-end of the inner space of this hollow shell, one is arranged at the far-end in the outside of this hollow shell, at least one rubber seal that is arranged in this central perforation and is located on this body of rod outside, it is other and be located on the hold-doun nut in this body of rod outside that one positioning screw cap and that is arranged at this lid outside and is located on this body of rod outside is arranged at this positioning screw cap, and this second pad is arranged at the near-end of this body of rod, support this first pad of pulling in this inner space to be positioned over, to adjust the tight ness rating between described a plurality of abrasive sheet.
3. fluid differential-pressure type nanometer grinding device as claimed in claim 2 is characterized in that, the axis of the pod apertures of described abrasive sheet horizontal by 0 to 60 degree.
4. fluid differential-pressure type nanometer grinding device as claimed in claim 1 is characterized in that this equipment for after-treatment comprises a bottling machine, and it is connected with this nano-milled device by a bottling feeding pipe, and this bottling feeding pipe is provided with a magnetic valve.
5. as each described fluid differential-pressure type nanometer grinding device in the claim 1 to 4, it is characterized in that, this equipment for after-treatment comprises a release of pressure groove, its bottom is provided with a release of pressure delivery pipe, this release of pressure groove is connected in this nano-milled device with a release of pressure groove feeding pipe, and this release of pressure groove feeding pipe is provided with a magnetic valve.
6. fluid differential-pressure type nanometer grinding device as claimed in claim 5 is characterized in that, this liquid supplying unit is connected to this raw material discharge nozzle with a liquid additive pipe, and this liquid additive pipe is provided with a fluid flowmeter.
7. fluid differential-pressure type nanometer grinding device as claimed in claim 5 is characterized in that, this gas supply unit is connected to this raw material discharge nozzle with a gas additive pipe, and this gas additive pipe is provided with a gas flowmeter.
8. fluid differential-pressure type nanometer grinding device as claimed in claim 6 is characterized in that, this gas supply unit is connected to this raw material discharge nozzle with a gas additive pipe, and this gas additive pipe is provided with a gas flowmeter.
9. fluid differential-pressure type nanometer grinding device as claimed in claim 5 is characterized in that, the feed pipe of this raw material feed well is communicated in place, the nearly top of this raw material feed well, and the raw material discharge nozzle of this raw material feed well is arranged at the bottom of this raw material feed well.
10. fluid differential-pressure type nanometer grinding device as claimed in claim 5, it is characterized in that, this pressure-equalizing device comprises one first nano-milled device and one second nano-milled device, and this return duct is communicated in this first nano-milled device, and this equipment for after-treatment is connected in this second nano-milled device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920005735U CN201375881Y (en) | 2009-02-17 | 2009-02-17 | Fluid pressure difference type nano grinding installation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN200920005735U CN201375881Y (en) | 2009-02-17 | 2009-02-17 | Fluid pressure difference type nano grinding installation |
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| Publication Number | Publication Date |
|---|---|
| CN201375881Y true CN201375881Y (en) | 2010-01-06 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200920005735U Expired - Lifetime CN201375881Y (en) | 2009-02-17 | 2009-02-17 | Fluid pressure difference type nano grinding installation |
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| CN (1) | CN201375881Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101804377B (en) * | 2009-02-17 | 2012-05-09 | 罗莎国际有限公司 | Fluid differential-pressure type nanometer grinding device |
| CN102806028A (en) * | 2011-05-31 | 2012-12-05 | 日本斯频德制造株式会社 | Dispersing method and dispersing system |
| CN115155763A (en) * | 2022-08-17 | 2022-10-11 | 杭州汉承生物科技开发有限公司 | Anthocyanin refining equipment and method |
-
2009
- 2009-02-17 CN CN200920005735U patent/CN201375881Y/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101804377B (en) * | 2009-02-17 | 2012-05-09 | 罗莎国际有限公司 | Fluid differential-pressure type nanometer grinding device |
| CN102806028A (en) * | 2011-05-31 | 2012-12-05 | 日本斯频德制造株式会社 | Dispersing method and dispersing system |
| CN102806028B (en) * | 2011-05-31 | 2015-06-24 | 日本斯频德制造株式会社 | Dispersing method and dispersing system |
| CN115155763A (en) * | 2022-08-17 | 2022-10-11 | 杭州汉承生物科技开发有限公司 | Anthocyanin refining equipment and method |
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