CN1060229A - Make the fragmentary method of solid particle agglomerate that floats on a liquid - Google Patents
Make the fragmentary method of solid particle agglomerate that floats on a liquid Download PDFInfo
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- CN1060229A CN1060229A CN91108919A CN91108919A CN1060229A CN 1060229 A CN1060229 A CN 1060229A CN 91108919 A CN91108919 A CN 91108919A CN 91108919 A CN91108919 A CN 91108919A CN 1060229 A CN1060229 A CN 1060229A
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- venturi tube
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- 239000007788 liquid Substances 0.000 title claims abstract description 75
- 239000002245 particle Substances 0.000 title claims abstract description 42
- 238000000034 method Methods 0.000 title claims abstract description 22
- 239000007787 solid Substances 0.000 title claims abstract description 22
- 230000004087 circulation Effects 0.000 claims abstract description 12
- 230000000694 effects Effects 0.000 abstract description 9
- 239000000463 material Substances 0.000 abstract description 7
- 239000003758 nuclear fuel Substances 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 6
- 238000010008 shearing Methods 0.000 abstract description 5
- 238000003860 storage Methods 0.000 description 9
- 230000008859 change Effects 0.000 description 7
- 238000007789 sealing Methods 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 230000005855 radiation Effects 0.000 description 4
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 239000011733 molybdenum Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 210000001138 tear Anatomy 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
- B02C19/06—Jet mills
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- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Disintegrating Or Milling (AREA)
- Jet Pumps And Other Pumps (AREA)
Abstract
For the fragmentary agglomerating solid particle that floats on a liquid, for example resultant tiny material in reclaiming the nuclear fuel process makes liquid circulation in Venturi tube (44) under band press strip spare.The velocity gradient of flowing liquid produces fragmentary these shearing force in Venturi tube.A part of liquid is circulated in Venturi tube, can improve fragmentary effect, Venturi tube is at this moment used as a thrower.Preferably Venturi tube is vertically installed, and make downward liquid flow.A baffling system can be arranged on the exit of Venturi tube.
Description
The present invention relates to a kind ofly can make the fragmentary or broken diffusing method of the solid particle agglomerate that floats on a liquid and implement the used equipment of this method.
Method and apparatus of the present invention is suitable for the agglomerate of fragmentary fine particle most, promptly have in the process of nuclear fuel of radiativity in recovery, the nuclear fuel of pulverizing is decomposed in hot salpeter solution, clarify salpeter solution then and obtain have a solid material that limits granularity.These tiny materials, its chemical constitution are to be base-material with other used metal of zirconium, molybdenum, ruthenium and manufacturing nuclear fuel, behind the clarification salpeter solution, for example, in a centrifugal rotation stillpot, become the indefinite solution of mud or concentration, accumulate in together in varying degrees.With the tiny material of these intense radiations after storage tank is placed a period of time, constantly stirred, for example used palsating equipment, then by suitable pipeline transportation to carrying out the place that vitrifacation is handled, there, in order to prevent that nuclear radiation from encasing it with glass lode ore material.
In the process that mud is transported to storage tank and these mud in storage tank between the storage life, the formed caking that varies in size brings serious problem.
Thereby the agglomerate of being made up of abrasive particle weares and teares the sweep of conveyance conduit.And these agglomerates will be in the non-turbulent flow districts of conveyance conduit or the pipe line area precipitation of rough inner-surface are arranged, and stop up piece and the sweep of pipeline is blocked thereby form.This obstruction piece or deposition piece have caused the problem that is difficult to solve, because they have strong nuclear radiation, therefore make any emergence treatment scheme all be difficult to implement.Because be difficult to simulate its operating mode, the flow characteristics of change equipment and mud also can not address this problem.
Another shortcoming that agglomerate had that varies in size that is transported in the mud in the storage tank is that these agglomerates are deposited on storage tank bottom, overslaugh storage tank and palsating equipment operate as normal.Owing in storage tank, carry out emergency processing and be difficulty especially, so wished very much before mud is transported to storage tank and can open the agglomerate in the mud that will be transferred is fragmentary.
Need be pointed out that although the present invention is particularly suitable for the fragmentary agglomerate that is contained in the tiny material of resulting intense radiation in the process that reclaims the radiativity nuclear fuel, the present invention is not limited to this application.The present invention can be used for fragmentary any solid particle agglomerate that floats on a liquid, and is particularly suitable for handling some trade effluent, for example chemistry and fertilizer industry.
The present invention be more particularly directed to make fragmentary method and apparatus, its purpose of solid particle agglomerate that floats on a liquid for example to be to eliminate and in the process of carrying these particles, form the danger of stopping up piece, or eliminate the danger of the agglomerating arbitrary mechanism of particle plugging, if and need, can reduce the wearing character of these particles.
More particularly, in order to realize purpose of the present invention, the present invention will make the liquid that contains agglomerating solid particle under stress circulate in Venturi tube.
Allow agglomerating solid particle enter Venturi tube, described particle is placed under the high velocity gradient that directly makes progress.In other words, with the cross section of the axis normal of pipe on, the inside circumference from the center to the pipe, the change in flow highly significant of liquid.Therefore, agglomerating solid particle is subjected to the effect with the very shearing force of the parallel axes of pipe, the fragmentary effectively agglomerate that is carried by liquid of this effect.
In two specific embodiments of the present invention, liquid is being in the vertically disposed Venturi tube basically, is recycled to the bottom from the bottom cycle to the top and from the top.Experiment shows that to the top circulation time, operating efficiency is higher in pipe for liquid.When agglomerate is big, preferably and especially Venturi tube to be made a thrower, this can guarantee the circulation of liquid.
Make flow of liquid cross a baffling system, can improve operating efficiency equally.Wherein, the effect that velocity gradient produced is to link mutually with the collision effect of agglomerate in the baffling system that is arranged in the Venturi tube exit.
The present invention also relates to be used for the equipment of the fragmentary solid particle agglomerate that floats on a liquid, it is characterized in that, it comprises that one has the liquid admission passage that contains agglomerating solid particle and the tube of passing away, a Venturi tube is installed in this tube, between admission passage and passing away.
In first embodiment of the present invention, with Venturi tube by being that vertical axis is installed in the tube basically, this Venturi tube has a lower inlet end, this entrance point is connected with admission passage by an inlet chamber that forms in the lower part of tube, this Venturi tube has a top endpiece, and this endpiece is connected with passing away by the circular passage that forms around Venturi tube.
Thereafter, Venturi tube separates effectively by nozzle and recirculation chamber and admission passage, and recirculation chamber is connected with the circular passage by the hole that forms in a dividing plate.
According to second embodiment of the present invention, with the Venturi tube edge is that vertical axis is installed in the tube basically, this Venturi tube has a upper inlet end, this entrance point is connected with admission passage by an outer annular passage that forms around this Venturi tube, this Venturi tube has a lower part outlet end, and this endpiece is connected with passing away by the discharge chamber that the lower part at tube forms.
Then, the most handy inner annular recirculation line surrounds Venturi tube, and the lower end of this passage is positioned at the top of a guide face, and guide face is positioned at the place facing to Venturi tube lower part outlet end; The upper end of this passage is between nozzle and Venturi tube.
In all cases, the baffling system can be placed on the downstream of Venturi tube
With indefiniteness embodiment embodiment of the present invention are described in more detail with reference to the accompanying drawings, wherein:
Fig. 1 is a longitudinal section, the equipment of its expression agglomerating solid particle that can fragmentaryly float on a liquid of the present invention, and among the figure, liquid flows to the top from the bottom in Venturi tube.
Fig. 2 is a longitudinal section that is similar to Fig. 1, and it represents second embodiment of equipment of the present invention, among the figure, liquid in Venturi tube from the overhead stream to the bottom.
Fig. 3 is a schematic sectional view that is similar to Fig. 1 and 2, and it represents the 3rd embodiment of the present invention, and the equipment among the figure has a baffling system.
Among Fig. 1, label 10 expression one horizontal concrete thickness plate, it can allow the groove 14 below upper area 12 that the people passes through and separate with one, and filling pending containing in the groove 14 will be by the liquid of fragmentary solid particle agglomerate.
To cover 24 upper ends that are fastened on garden tube 18 with bolt 25, garden tube 18 will be sealed.Sleeve pipe 26 is outstanding downwards from covering 24 lower surface, garden tube 18 in the downward extension in garden tube 18 coaxial cable ground.The thrower of using label 30 to represent is being carried in lower end at sleeve pipe 26 with bolt 28.Thrower 30 is made up of three parts 31,32 and 33, and they and garden tube 18 be axial line altogether.This three part is a lower member 31, the exterior part 33 on inside center parts 32 and top.
With bolt 34 bottom disc-shaped part 31 is fastened on the lower end of inside center 32.Parts 31 therein the heart have one with cylinder 18 nozzle 36 of the contraction of vertical axis altogether.The inlet chamber 38 that forms in the lower part of garden tube 18 is led in the major diameter lower end of nozzle 36.An admission passage 40 that forms in the thick wall part 18a of garden tube 18 also leads to inlet chamber 38, so that containing and will being incorporated into inlet chamber 38 by the liquid of fragmentary solid particle agglomerate.With a pump that does not show in the accompanying drawings pressure fluid is injected this equipment 16, injection pressure for example is at least 300KPa.
The bottom of the inside center parts 32 of thrower 30 has a bell part 43 and a top that forms Venturi tube 44, fixed installation lower member 31 below bell part 43.Between the bell part 43 of bottom and lower member 31, form a circular chamber 42.With nozzle 36 and garden tube 18 Venturi tube 44 bottoms of the axial lines circular chamber 42 that leads to nozzle 36 tops altogether.Form the lower inlet section 46 and a top outlet section 48 of short convergent than long flaring in the inside of Venturi tube 44.
A sealing O-ring 60 is housed on the outside surface of the bell part 43 in bottom, and its inside surface with the thickest part 18a of garden tube 18 above the opening of admission passage 40 has constituted sealing, and therefore, inlet chamber 38 completely cuts off with the remainder of garden tube 18.
The bottom of the exterior part 33 on the top of thrower 30 has garden annulus 49, with bolt 28 garden annulus 49 is fastened on the lower end of sleeve pipe 26, and garden annulus 49 is around around the Venturi tube 44.The garden annulus 49 of this bottom is installed on the thickest part 18a of garden tube 18 by two sealing O-rings 62.
The exterior part 33 on top also has a tubular portion 50 that forms in its upper end above the garden of bottom annulus 49, above Venturi tube 44, a cap shape part 51 is arranged.Tubular portion 50 around Venturi tube 44 around and with Venturi tube 44 coaxial inner conductors, and by the welding connecting link 53 carrying Venturi tube 44.In the circular passage 54 that forms between Venturi tube 44 and the part 33 passing away 58 that forms in the upper end of Venturi tube and the thickest part 18a at garden tube 18 is communicated with, passage 58 encircles between 60 and 62 at O-, leads to said groove.
The hole 64 that forms in the horizontal component on the top of the bell part 43 of bottom is communicated with the bottom of circular passage 54 with circular chamber 42.These holes are recycled a part of liquid and enter Venturi tube 44, will be described in greater detail below.
Contain to be preferably under the pressure of 300KPa by the liquid of fragmentary solid particle agglomerate and be admitted to this equipment through admission passage 40.The band press liquid that is introduced into inlet chamber 38 by the converging transition 46 and the divergent segment 48 of nozzle 36 and Venturi tube, flows through thrower 30 from bottom to top successively.Liquid stream in the nozzle 36 has produced high flow rate by Venturi tube 44.Therefore, if the flow of liquid that is introduced into equipment 16 near 5 meters
3/ hour, the external diameter of nozzle 36 is near 10 millimeters, and then the flow velocity of liquid can be near 18 meter per seconds.
Enter flow through the from bottom to top then liquid of initial flow of Venturi tube 44 of nozzle 36, and by being superimposed by the carried under one's arms flow of the injection that comes of hole 64 by the liquid of the said initial flow that enters circular chamber 42.Experiment shows that the flow of injection is very near initial flow.Subsequently, the liquid that is superimposed is with near 10 meters
3/ hour flow pass Venturi tube 44, said as following example.
For example bump against on the bell part 51 with the liquid that flows out at a high speed from its diameter, turn back again by circular passage 54 near the upper end of 40 millimeters Venturi tube 44.Then, a part of liquid flows out through passing away 58 slave units 16, and remaining liquid enters circular chamber 42 circulations by hole 64.
Enter flow through the then liquid of Venturi tube 44 of nozzle 36 and have very big radial velocity gradient, promptly be far longer than along the flow velocity of the wall flowing liquid of nozzle and Venturi tube along the flow velocity of vertical axis at this near axis flowing liquid.Flowing liquid and solid particle agglomerate are subjected to very big shearing force continuously in nozzle 36 and Venturi tube 44, make these agglomerates by fragmentary.
Be subjected to the particle of above-mentioned shearing force effect to be subdivided into smaller particles,, no longer can be enough to till fragmentary these particles for quite little the shearing force that causes by the radial velocity gradient of the liquid that enters nozzle 36 and Venturi tube 44 until its size of these smaller particles.
For example, the mean diameter of the particle that suspending liquid contained of passage of having found to enter equipment 16 of the present invention is near 30 microns, by behind the passage, the mean diameter of particle is reduced between 10 to 15 microns first, and the mean diameter of process circulation back particle is reduced near 5 microns.
In another experiment, make by the diameter of particles suspended greater than 100 microns.The liquid of initial access arrangement 16 contains 4% this particle, flow through passage first after, from the liquid that Venturi tube 44 flows out, only contain 3% particle, through after the circulation once, said percentage is reduced to 1.5%, after twice circulation, is reduced to 0.7%.
Owing to exist abrasive particle in processed liquid, and this liquid also has corrosivity, and therefore, the part that is acted on of equipment 16 promptly mainly is nozzle 36 and Venturi tube 44, obviously can damage quickly.Thereby, to equipment shown in Figure 1, can thrower be split out by the top zone 12 that allows the people pass through, so as need the time it is more changed.
In order to change, operating personnel can pull down bolt 25 in zone 12, unload lower cover 24, and lid 24 is being with thrower 30 to be removed together by sleeve pipe 26.As the case may be, said thrower can be replaced whole or in part.Thereby thrower 30 is installed on the sleeve pipe 26, so that dismantle it by bolt 28.When on parts 31, forming nozzle 36, can parts 31 be detachably fixed on the parts 32 with Venturi tube 44 by bolt 34.
With reference in the described equipment of Fig. 1, processed liquid flows to the top from the bottom in by nozzle 36 and Venturi tube 44 formed throwers in front.In fact, experiment shows, makes liquid flow to the top from the bottom in said thrower, can obtain high-level efficiency.In second embodiment of equipment of the present invention, downward liquid flow is passed through thrower.Below, be described in greater detail with reference to Fig. 2.
In the equipment of Fig. 2, the different parts of realizing the described identical function of relative Fig. 1 increase by 100 simultaneously with identical label and represent.And those different features of feature of the only relative described equipment of Fig. 1 just are described in detail.
Described in first embodiment, equipment 116 shown in Figure 2 has and is hung in the garden tube 118 of the axis normal on the horizontal slab 110 and removably is contained in the interior thrower 130 of tube 118.Thrower 130 can be changed from the zone 112 of slab 110 tops.Thrower 130 is made up of three parts 131,132 and 133, they and garden tube 118 vertical axis coaxial lines, shown in the embodiment of Fig. 1 like that, exterior part 133 has following annulus 149, is installed on the thickest part 118a of tube 118 by two sealing O-rings 162.Part 149 extends upward by tubular portion 150, is sealed by a horizontal component 151 in its upper end, and horizontal component 151 is fixed to from 112 lids that get at 124 of zone.By means of the bolt on the upper flange that for example is screwed in garden tube 118 121, the ring 120 that covers 124 tops will be fixing on the throne by the assembly that lid 124 and exterior part 133 constitute.
The admission passage that is used for processed liquid 140 that forms in the thickest part 118a of garden cylindrical shell 118 is between O- ring 160 and 162, this passage is preferably tangential, so that make the liquid in the outer annular chamber 170 that forms between the parts 133 and central module 131 outside produce rotational flow.The upper end of outer annular passage 170 is communicated with the upper inlet end of nozzle, and nozzle 136 is communicated with Venturi tube 144.
The lower end of Venturi tube 144 is located at the place ahead of the guide face 172 that forms in the lower part of intermediate member 131.The shape of guide face should make it can avoid particle to gather herein, makes liquid radially outward earlier, and then makes liquid upwards, carries out such change and just can achieve the goal.The lower end by the passage 174 of its lower end from the upper end of guide face 172 that forms in the lower part of parts 131 enters the discharge chamber 156 that forms in the bottom of the cylinder 118 below O-ring 160.Passage 174 has a common lower part, and it and cylinder 18 coaxial lines are located immediately at the top of the passing away 158 that forms along the said axis of the bottom of cylinder 118.
Inner annular circulation passage 176 also forms between the central module 132 of intermediate member 131 and formation Venturi tube 144.The lower end of passage 176 is positioned at the top of guide face 172, and the upper end is between nozzle 136 and Venturi tube 144.
With reference in the described equipment 116 of Fig. 2, the with pressure pending liquid that is injected by admission passage 140 at first passes through outer annular passage 170 to the upper reaches in thrower 130, then downwards in turn by nozzle 136 and Venturi tube 144 in front.In the lower end of Venturi tube, a part of liquid is directly discharged by passage 174 and 158, and remaining liquid is entered Venturi tube by annular circulation passage 176 circulations.
The front all is the non-recessed round-robin that revolves with reference to the thrower in the described equipment of Fig. 1 and 2 in both cases, and experiment shows that this thrower is obtaining to have best performance aspect the desired fragmentary particle.
In order to change technological parameter, can have said thrower instead and revolve recessed round-robin nozzle.This improves the efficient of equipment exponentially, but the danger of damage equipment is also bigger.In the time exactly need reducing the running time of liquid to be processed, can adopt this scheme.
As a kind of conversion, can adopt does not have the round-robin venturi apparatus yet, and it is applicable to the occasion of just having been tied piece by the entrained solid particle of liquid slightly.When need be fragmentary in large quantities during agglomerating particle, the occasion as particularly using at nuclear preferably adopts the cyclic spray device.
Fig. 3 very clearly expresses a kind of modification equipment 216 of the present invention.This equipment has a thrower 230 that has the baffling system.As the described embodiment of relative Fig. 1, thrower 230 removably is contained in the tube 218.Thrower 230 is to be provided with like this, makes pending liquid from the top to the bottom, in turn by nozzle 236 and Venturi tube 244.And, make the outlet of Venturi tube 244 enter baffling system 280, baffling system 280 reduces the height of Venturi tube 244, and diameter increases.Baffling system 280 is formed by the passage 282 between the contour surface 284,286 of two coaxial cables.
In equipment shown in Figure 3 216, enter into the pending liquid of thrower 230 by the admission passage 240 that in tube 218, forms, in turn at nozzle 236, circulation in the passage 282 of Venturi tube 244 and baffling system 280.Therefore, in nozzle and Venturi tube with foregoing mode by shear the resulting fragmentary effect that agglomerating particle is produced with the impact effect of the wall of baffling system 280 under produced auxilliaryly add fragmentary effect and be superimposed.
As previously described, liquid is by after the Venturi tube 244, and a part flows out these equipment by passing away 258, and remaining liquid is recycled by the passage 264 that forms on the seat of Venturi tube and enters Venturi tube 244.
As already noted, equipment of the present invention is particularly suitable for handling through salpeter solution and decomposes the tiny material that is obtained behind the nuclear fuel, and this equipment also is suitable for handling and contains any liquid of wanting by the fragmentary solid particle that clumps together, particularly industrial sewage.
Obviously, the invention is not restricted to the front with the described embodiment of way of example, in fact, it comprises all modification of these embodiments.Thereby the baffling system that is arranged on the Venturi tube exit with rising liquid stream of embodiment as shown in Figure 3 can be arranged on the outlet of the Venturi tube with decline liquid stream.And the liquid admission passage that forms in the tube of equipment and the direction and the position of passing away can change, and this change does not exceed scope of the present invention.
Claims (12)
1, be used for the method for the fragmentary agglomerating solid particle that floats on a liquid, it is characterized in that, this method comprises flows the liquid that contains agglomerating solid particle in Venturi tube (44,144,244) under band press strip spare.
By the method for claim 1, it is characterized in that 2, this method comprises that making said liquid is to flow from the bottom to the top in the vertical Venturi tube (42,244) at one substantially.
By the method for claim 1, it is characterized in that 3, this method comprises that making said liquid is mobile to the bottom from the top in the vertical Venturi tube (144) at one basically.
By the method for one of claim 1 to 3, it is characterized in that 4, this method comprises flows said liquid in forming the Venturi tube (44,144,244) that obtains liquid round-robin thrower.
By the method for one of aforesaid right requirement, it is characterized in that 5, this method comprises flows said liquid in the baffling system (280) in the exit of Venturi tube (244).
6, the equipment that is used for the fragmentary agglomerating solid particle that floats on a liquid, it is characterized in that, this equipment comprises a tube (19,118,218), admission passage of the liquid that contains agglomerating solid particle that forms on tube (40,140,240) and passing away (58,158,258) are installed in a Venturi tube (44,144,244) in this between admission passage and passing away.
7, press the equipment of claim 6, it is characterized in that, Venturi tube (44,244) is installed in the tube, its axial line is vertical basically, it has a lower inlet end and top endpiece, the lower inlet end is communicated with admission passage by the inlet chamber (38) that the lower part at tube forms, and the top endpiece is communicated with passing away by the circular passage (54) that forms around Venturi tube.
8, by the equipment of claim 7, it is characterized in that Venturi tube (44) and inlet chamber are separated by a nozzle (36) and a circular chamber (42) that is connected with circular passage (54) by several holes (64).
9, press the equipment of claim 6, it is characterized in that, Venturi tube 144 is installed in the tube, its axial line is vertical basically, it has a upper inlet end and lower part outlet end, the upper inlet end is communicated with admission passage 140 by an outer annular passage (170) that forms around Venturi tube, and the lower part outlet end is communicated with passing away by a discharge chamber (156) that forms in the lower part of tube.
10, press the equipment of claim 9, it is characterized in that, Venturi tube (144) is surrounded by an inner annular circulation passage (176), and its lower end is positioned at the top of the guide face (172) that is arranged on Venturi tube lower part outlet end front, and its upper end is between nozzle and Venturi tube.
11, by the equipment of one of claim 6 to 10, it is characterized in that baffling system (280) is positioned at the downstream of Venturi tube (244).
12, by the equipment of one of claim 6 to 11, it is characterized in that Venturi tube (44,144,244) is installed in the removable thrower (30,130,230).
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR9010476 | 1990-08-20 | ||
| FR9010476A FR2665845B1 (en) | 1990-08-20 | 1990-08-20 | PROCESS FOR DISAGGRATING AGGLOMERATED SOLID PARTICLES, SUSPENDED IN A LIQUID. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1060229A true CN1060229A (en) | 1992-04-15 |
Family
ID=9399738
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN91108919A Pending CN1060229A (en) | 1990-08-20 | 1991-08-19 | Make the fragmentary method of solid particle agglomerate that floats on a liquid |
Country Status (7)
| Country | Link |
|---|---|
| EP (1) | EP0472458B1 (en) |
| JP (1) | JP3138293B2 (en) |
| KR (1) | KR920004036A (en) |
| CN (1) | CN1060229A (en) |
| CA (1) | CA2049090A1 (en) |
| DE (1) | DE69106277T2 (en) |
| FR (1) | FR2665845B1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1669937B (en) * | 2003-12-03 | 2010-05-26 | 株式会社御池铁工所 | Apparatus for ultrafinely shattering organic granular substances |
| CN116445183A (en) * | 2023-03-14 | 2023-07-18 | 中国石油化工股份有限公司 | Reaction device and method for jet mixing and reinforcing waste alkali liquid oxidation |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AUPN829796A0 (en) * | 1996-02-23 | 1996-03-21 | Bengold Holdings Pty Ltd | Improved grinding method and apparatus for performing same |
| DE10343748B4 (en) * | 2003-08-29 | 2005-11-10 | BIONIK GmbH - Innovative Technik für die Umwelt | Process for comminuting particulate organic substances in suspensions of microorganisms |
| CN113333191B (en) * | 2021-05-31 | 2022-07-05 | 武汉大学 | Rotating shearing cavitation nozzle |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB591921A (en) * | 1944-04-08 | 1947-09-02 | Inst Gas Technology | Improvements in or relating to apparatus for and method of comminuting a permeable material |
| US3348778A (en) * | 1966-03-04 | 1967-10-24 | Mineral Ind Corp Of America | Reducing particle size of clay and rheology control of clay-water systems |
| GB1329941A (en) * | 1972-01-05 | 1973-09-12 | Texaco Development Corp | Fluid energy grinding method and system |
| FR2311588A1 (en) * | 1975-05-23 | 1976-12-17 | Inst Francais Du Petrole | Venturi device for disintegrating agglomerated powders - for rapid, complete sepn. of e.g. polyfluorocarbon polymers |
| US4619406A (en) * | 1976-12-22 | 1986-10-28 | Can-Am Engineering Corporation | Hydraulic system and method of improving the working properties thereof |
-
1990
- 1990-08-20 FR FR9010476A patent/FR2665845B1/en not_active Expired - Lifetime
-
1991
- 1991-08-13 CA CA002049090A patent/CA2049090A1/en not_active Abandoned
- 1991-08-19 CN CN91108919A patent/CN1060229A/en active Pending
- 1991-08-19 DE DE69106277T patent/DE69106277T2/en not_active Expired - Fee Related
- 1991-08-19 EP EP91402260A patent/EP0472458B1/en not_active Expired - Lifetime
- 1991-08-20 JP JP03208230A patent/JP3138293B2/en not_active Expired - Lifetime
- 1991-08-20 KR KR1019910014289A patent/KR920004036A/en not_active IP Right Cessation
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1669937B (en) * | 2003-12-03 | 2010-05-26 | 株式会社御池铁工所 | Apparatus for ultrafinely shattering organic granular substances |
| CN116445183A (en) * | 2023-03-14 | 2023-07-18 | 中国石油化工股份有限公司 | Reaction device and method for jet mixing and reinforcing waste alkali liquid oxidation |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2049090A1 (en) | 1992-02-21 |
| DE69106277T2 (en) | 1995-07-06 |
| EP0472458B1 (en) | 1994-12-28 |
| EP0472458A1 (en) | 1992-02-26 |
| FR2665845B1 (en) | 1995-01-20 |
| JP3138293B2 (en) | 2001-02-26 |
| DE69106277D1 (en) | 1995-02-09 |
| FR2665845A1 (en) | 1992-02-21 |
| JPH04250859A (en) | 1992-09-07 |
| KR920004036A (en) | 1992-03-27 |
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