CN102712429A - Device for densely loading a divided solid into a chamber - Google Patents
Device for densely loading a divided solid into a chamber Download PDFInfo
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- CN102712429A CN102712429A CN2010800476037A CN201080047603A CN102712429A CN 102712429 A CN102712429 A CN 102712429A CN 2010800476037 A CN2010800476037 A CN 2010800476037A CN 201080047603 A CN201080047603 A CN 201080047603A CN 102712429 A CN102712429 A CN 102712429A
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- Prior art keywords
- diversion member
- axis
- hollow shaft
- axle
- diversion
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G69/00—Auxiliary measures taken, or devices used, in connection with loading or unloading
- B65G69/04—Spreading out the materials conveyed over the whole surface to be loaded; Trimming heaps of loose materials
- B65G69/0458—Spreading out the materials conveyed over the whole surface to be loaded; Trimming heaps of loose materials with rotating means, e.g. tables, arms
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
- B01J8/002—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor with a moving instrument
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
- B01J8/003—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor in a downward flow
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)
- Ship Loading And Unloading (AREA)
Abstract
The invention relates to a device (1) for densely loading a divided solid (2) into a chamber (7), intended to interact with a divided-solid supply device (3) arranged to release the divided solid above an access to the chamber. The loading device comprises a shaft (4) rotated about an axis X1 at an adjustable rotational speed, a plurality of deflecting elements (5) rigidly connected in rotation with the shaft, the deflecting elements having an angle, relative to the shaft, which is separately adjustable from the rotational speed of the latter. According to a preferred embodiment, the shaft (4) is hollow in order to define a passage for the divided solid, at least some of the deflecting element (5) having an end (16) arranged at a distance from the axis X1 that is smaller than the distance separating the axis X1 from the the hollow shaft.
Description
Technical field
The present invention relates to a kind ofly with the intensive device that is loaded into container of bulk solid, this device is used to and the cooperation of the feeding device of bulk solid, and said feeding device is arranged for above the inlet of container and discharges bulk solid.
Dispersed solids is meant to be particle or particulate solid within the scope of the invention, the for example cereal-granules in grain transportation and the production field, the catalyst granules in the chemical field, or fertilizer or wood particle.
More properly, loading attachment according to the present invention preferably includes, and is actuated to the axle of adjustable rotating speed around axis X 1 rotation, and a plurality of diversion member that links to each other with the axle rotation.Therefore, dropping after on the diversion member, dispersed solids is departed from, thereby more or less is distributed in equably on all surface of its container that is written into.
Background technology
Usually be active in the enterprise of chemical field,, proposed the device of a plurality of said types about being the chemical reactor loading catalyst.
French Patent (FRP) FR 2431449 has described the exemplary device that is used to the chemical reactor loading catalyst, and it comprises and is located in the catalyst supply hopper and the axle coaxial with its maintenance.The overlapping many groups diversion member that is long and narrow band shape distributes around axle regularly, and is fixed on the said axle through attached device, and said attached device can change the angle of confirming between diversion member and the axle.
Therefore, when axle was driven in rotation, diversion member separated with axle under action of centrifugal force, thereby was convenient to the chemical reactor of the common inlet contraction of device introducing inner.The rotating speed of axle can be conditioned, and is used to control the angle between diversion member and the axle, thereby can calculates the reactor surface area that is covered by catalyst.
Yet, note, for setter, the change that the change of axle rotating speed also can bring a durchgriff.For this reason, according to the parameter that the geometric configuration of the container of treating the filling dispersed solids is regulated, can not regulate independently of one another.
Therefore, said device is particularly suitable for totally being cylindric and radius several meters the loading of chemical reactor approximately.
Yet said device not too is fit to load the cabin of bulk carrier type.The size of the stowage that the latter has is different from the volume size of chemical reactor fully.In fact, the most common bulk carrier of building now is Handymax, and its volume is between 35 tons and 50000 tons, and Panamax, and its volume is between 50 tons and 80000 tons, and the volume of Capesize is then bigger.
Note that the sea-freight of grain has the regulation of tailor-make.In fact, the bulk loading that on the ship of transportation grain, realizes traditionally makes the stability of ship in underway have actual danger.Even if cabin is filled up by commodity fully, the roll and pitch of ship in voyage can cause the sinking of particle and between particle bed course and cabin top, discharge the space.Under the situation that does not have to be filled up by goods fully at cabin, said phenomenon can strengthen.
Although realize mechanical planarization by the long shoreman, said in underway sunk and still can't avoid and still dangerous for whole ship, all hands and goods.In fact, in a single day the characteristics of grain goods are between cereal surface and cabin top, to have space freely, just can liquid mode be moved easily.
Because the cereal sport that the inclination of ship causes causes center of gravity big of ship to move and damage its stability.Much the analysis to the perils of the sea shows, wherein a lot of perils of the sea especially come from said sagging phenomenon.
In order to limit the said phenomenon that causes a large amount of ships to topple, the loading of grain will be followed special regulation, and the purpose of this regulation is to reduce goods sideslip risk, but can't eliminate said risk.International Maritime mechanism has confirmed that in the 1970's said standard and this standard embody a concentrated reflection of among the international treaties SOLAS (Saftey of Life At Sea); Wherein the VI chapter is clearly stipulated; Particle answers rectangular distribution belowdecks, the feasible planeness that guarantees Free Surface.It is also stipulated in addition, and the side tilt angle of the ship that the particle sideslip forms should not surpass 12 degree.
Especially, the loading attachment of ship preferably allows to reach between one hour loading flow rate between 600 tons to 2000 tons at present.Above-mentioned mention can not reach said flow rate usually to the cargo-carring device of chemical reactor.
Therefore; Present employed device is more basic, because it only meets the principle of gravity filling, for example under the situation of carrying conduit, unloading belt conveyor or scraper bowl; And it need and load in loading process when finishing by personnel's interventional procedure, to improve the degree of uniformity of distribution of particles." ship loader " type emptying equipment also is used in loading process and makes the particle flow deflection, treats in the entire container of filling thereby loading is distributed in.Yet said emptying equipment is inappropriate for the geometric configuration of the cabin of all bulk carriers.In addition, above-mentioned all devices of mentioning can not make that all the cargo-carring density of particle is optimum, and therefore can't avoid the problem of the stability of ship fully.
In the container of for example reaction vessel under the situation of loading catalyst; The stress relevant with the anisotropy of catalyst particles can cause loading section (profile of the free surface of catalytic bed for example can be observed protuberantia and depression) and load section generation deflection with respect to theoretic plane.
When loading, catalyst particles is in the location on catalytic bed surface, if words uniformly inadequately can cause the appearance of channeling when operation, just privileged way will be harmful to the efficient that institute hopes conversion.The possibility of result is multiple, can cause the too early ageing of the irregular and catalyst of temperature profile when catalytic bed is quickened puncture, changing effect reduction, differential pressure change, operation.
The result is can see and need change catalytic bed more continually, so improve catalysis cost, service expenditure, commercial unit Occupation coefficient, and also have and transform the relevant economic loss of relatively poor quality of products obtained therefrom, so become valuable inadequately.Said phenomenon is accompanied by the accelerated weathering of equipment, said aging with will corrode wallboard, cause stop up and the catalyst particles ratiometric raising of accelerated corrosion relevant.
Summary of the invention
Main purpose of the present invention is to remedy the shortcoming of known loading attachment of the prior art; And intensive cargo-carring device proposed; This device has greater flexibility when regulating the quality influence dispersed solids Particle Distribution and inhomogeneity different parameters, and can obtain the load factor of raising.
Another object of the present invention is to make and improve cargo-carring closeness optimization the transportation volume in preset volume, thereby have remarkable advantage economically with on the environment.
For this reason, the present invention relates more particularly to a kind of dispersed solids is loaded into the device of container thick and fast, and it meets the above-mentioned characteristic of mentioning, and it is characterized in that, its diversion member has the angle that can be independent of rotating speed and regulate with respect to axle.
Have benefited from said characteristic; Device according to the present invention has such condition of service; This condition of service can accurately be regulated according to the geometric configuration of treating cargo-carring container, loads desired filling condition thereby make it to meet bulk carrier, and possesses enough flow rates.
Preferably, said device has the hollow shaft of the passage that is used to limit dispersed solids, and some diversion member has the end that is located at apart from axis X1 one segment distance at least, the distance that said distance is separated less than axis X 1 and hollow shaft.
In addition; Hollow shaft preferably is the overall cylindrical shape that is, it is adjusted to and is whole feeder channel cooperation for the cylindrical shape feeding device, and has the radius that is equal to or less than the feeder channel radius basically; To be used for and the feeder channel cooperation, be unique passage of dispersed solids thereby make the passage in the axle.
According to preferred embodiment, hollow shaft has opening in the end that it is positioned at container one side, at least some diversion member have with respect to its opening be arranged on the axle extended line on the inner.
Have benefited from said characteristic, the rectangular distribution that can guarantee that dispersed solids is on all surface of the container of treating filling---extended line that comprises the axle drive shaft of diversion member---.
Therefore, loading density is optimised.Like this, than the stowage of prior art, same ship can transport the dispersed solids of greater number in each voyage, thereby is bringing more superiority aspect economy and the environment.
In addition, each diversion member can comprise and interconnectively be two parts on plane basically, thereby makes cross-sectional plane V-shaped, and planar section preferably is separated in the inner end region of each diversion member, thereby limits the additional passage of dispersed solids.In addition, control apparatus can be set for the degree of dip according to orthogonal first axle A1 and second axis A2 adjusting diversion member.
Description of drawings
Reading to the detailed description of the preferred embodiment that provides with non-restricted manner of the present invention and after with reference to accompanying drawing, other features and advantages of the present invention will embody more clearly, in the accompanying drawing:
-Fig. 1 illustrates the general illustration of cabin being carried out cargo-carring principle through loading attachment according to the present invention;
-Fig. 2 is the schematic perspective view of loading attachment according to the preferred embodiment of the present invention; And
-Fig. 3 is the simplification schematic top plan view of the loading attachment of Fig. 2.
The specific embodiment
Fig. 1 illustrates the operation logic according to intensive loading attachment of the present invention with non-limitation and shows in schematic form.
For intensive loading attachment 1 provides grain 2:, with fixing flow rate, lead to hopper 3 usually via socket since the initial stage storage location.Between socket and hopper, can design and use traditional surge hopper pipe, this does not exceed the scope of the invention.
The loading attachment 1 that aligns and be provided with hopper 3 comprises the rotating mechanism 4 that begins loaded particles from socket, and has a plurality of openings (will be described in more detail with Fig. 2) that are used for rectangular distribution particle on a whole set of diversion member 5.
Preferably, the particle jet should divide as far as possible, so that it optimized the distribution of particle before being loaded by diversion member.Therefore particle drops on diversion member, and said diversion member is separated from each other particle through the geometric configuration of manufacturing, and it is distributed on all surface of treating cargo-carring container, is cabin 7 here.Preferably, particle is " rainfall " uniformly shape and is distributed in the cabin, thereby allows on all surfaces of cabin, the grain layer to be raise regularly, and guarantees to load the closeness with maximum.
When accomplishing intensive loading, the stable position of each particle is directly related with the ratio of flow rate/face area.The ratio of maximum flow rate/face area of recommending be about 5 tons/per hour/sq m.In other words, in one hour loading process, load in order to optimize particle, not being taken in drops on the face area of 1 sq m surpasses 5 tons particle.
In addition, in order to optimize loading, also need consider following additional standard:
If in loading process, stratum granulosum occurs tilting, and degree of dip should not surpass 15 degree so.Can note, be about in inclination under the situation of 37 degree, in bulk year or with to increase to zero according to the density between the loading of apparatus of the present invention realization.
Preferably, can realize loading and need not the required peripheral operation of any smooth grain layer.In fact, in case when carrying out peripheral operation, can cause the compacting again of (particle) layer, that is, make the loading density that obtains in advance reduce for smooth grain layer.
Can make that according to the cabin face area loading flow rate is optimum.Should reach about 800 tons/hour moment flow rate value.
In order to reach said target, the patent applicant has developed the intensive loading attachment that on Fig. 2, is schematically shown.
This device comprises rotating mechanism 4, and this rotating mechanism is connected on the hopper 3 of particle feeding device through cylinder strut member 9.Rotating mechanism 4 is the shape that axis is the hollow shaft of X1, and radius is equal to or less than the radius of hopper 3 basically.
Actuating device 10 is set for adjustable rotating speed and drives hollow shaft 4 rotations.Said actuating device can be processed any known shape of prior art condition.On Fig. 2, the driving engine that has driving belt 13 is shown with mode typical but not limitation, this driving engine can have gear, and said gearing is used to drive the hollow shaft rotation on the circumference of hollow shaft 4.
In a similar manner, on the one hand, the interface unit of cylinder strut member 9 and hopper 3, on the other hand, hollow shaft 4 can be the known any suitable type of prior art with the interface unit of cylinder strut member 9.Advantageously, can stipulate hollow shaft 4 rotations to be installed on the cylinder strut member 9 through ball bearing of main shaft or coro bearng (not shown).
Hollow shaft 4 is opened in the top, is used to receive the particle from hopper 3, and it also has opening 14 in the lower end, is used for particle is poured over the container of treating filling.
In the embodiment that illustrates for example with non-restricted manner, hollow shaft 4 supportings are foliated three overlapping diversion members 5 (for high-visible, have a group and on Fig. 2, be blocked) for six groups.Show that in some cases it can be particularly advantageous installing eight groups, but in order to improve the visibility of accompanying drawing, show the enforcement modification that has six groups.Said group blade shroud distributes around hollow shaft regularly, and is arranged on the downstream of hollow shaft.Therefore, each blade has the inner 16 that is provided with from axis X 1 one distance, and said distance is less than the radius of hollow shaft, thereby the inner is positioned in the inner particle path that limits of hollow shaft.
Better, each is organized diversion member and begins mechanical connection on hollow shaft from the outside of hollow shaft, thereby can not hinder passing through of particle.
More properly, each is organized diversion member and is connected on the hollow shaft through the retaining element device, and this device is the shape of pole 17, and this pole has basic along directed two parts 19,20 (for clarity, a pole 17 being shown on Fig. 2) of axis X 1 direction.One of said part 19 comprises control apparatus 22; This control apparatus is set for to be regulated its length and therefore changes the fore-and-aft tilt degree of corresponding diversion member with respect to axis X 1; This is through along the first axle A1 rotation that is orthogonal to axis X 1, makes the length of another part 20 fix and realize.Control apparatus 22 can be shape or other known any suitable shape of prior art of jack, for example with the worm screw of the screw cooperation that is connected diversion member.
With preferred mode, for all diversion members of same group, even all diversion members of all groups, it is identical that the fore-and-aft tilt degree all keeps.
In addition; Second portion 20 advantageously comprises annular knurl parts 24; Said annular knurl parts be connected one group of grooved shaft 25 cooperation on the given deflecting plate, and through each said axis along the rotation that is orthogonal to the axis A2 of first axle A1, change the rate of roll of diversion member.
Identical with the fore-and-aft tilt degree is, preferably, the rate of roll of diversion member is to all diversion members of same group, even all diversion members of all groups are all identical.
With non-limitation mode for example, driving engine 26 can be set for 24 rotations of Long-distance Control annular knurl parts.
Those skilled in the art can guarantee that deflecting plate is assembled on hollow shaft through using known variation device, and can not run into special difficulty when making present explanation be fit to himself needs, can't exceed scope of the present invention.
From above-mentioned explanation; Reflect the rotating speed that the orientation of diversion member on vertical and horizontal is independent of hollow shaft, thereby making to regulate according to the character of the geometric properties of treating cartridge and relevant dispersed solids and to the operation that intensive loading attachment according to the present invention carries out has bigger flexibility ratio.
It may be noted that diversion member as shown in Figure 2 has with optimal way but not the special shape shown in the limitation mode.
In fact, each diversion member comprises two parts 28 and 29, and said two parts 28 and 29 are plane and inclination each other basically, thereby V-shaped on cross-sectional plane.In addition, part 28,29 is separated in the inner end region of corresponding diversion member, defines with this and replenishes passage 30, thereby make the dispersed solids can be from beginning to be poured onto on each diversion member of same group near the diversion member of hollow shaft.For example, each several part 28 or 29 can be trapezoidal shape, and through being positioned at maximum base, just links to each other with another part away from one of side of the length in the base near zone of axis X 1.
Those skilled in the art can not run into special difficulty when shape of regulating diversion member according to self needs and character.Said diversion member can be made into and has rectangle or interior curved cross section; And with the rigidity that does not exceed the scope of the invention, semi-rigid or flexible material---for example for example with non-limitation mode, metal, plastics, rubber, enhanced rubber or composite material---process.In addition, it is noted that two parts 28,29 can and treat that the geometric configuration of cargo-carring container processes with material different according to the character of dispersed solids.Use this device in the sea-freight field, preferably, the material of continuing to employ will have the characteristic that---for example there is a large amount of salt in the various harsh conditions of tolerance---.
Remain in order to improve loading mass, additional control apparatus preferably is set for the dispersed solids particle is toppled in adjusting to diversion member 5 from hollow shaft 4 mode.
Therefore, the opening 14 of hollow shaft advantageously has the device of regulating its size, and for example more particularly at the barrier film shown in Fig. 3 32, Fig. 3 illustrates the device of Fig. 2 with schematic top plan view.
Those skilled in the art are to making this barrier film or other any device that is equal to can not run into special difficulty.For example, the application of patent EP0482991 A1 discloses a plurality of exemplifying embodiments of barrier film.
Get back to Fig. 2, demonstrate hollow shaft 4 and also have a plurality of lateral openings 34, said opening is provided with many group diversion members along the direction of axis X 1 with aliging.Each said lateral openings 34 can be through the size of valve 35 adjusting openings, and the degree of dip that the degree of dip of said valve can be independent of other valve is conditioned.
Said whole adjustment feature by means of foregoing description; Special shape and distribution in conjunction with diversion member; Intensive loading attachment according to the present invention will bring very large flexibility ratio; With according to treating the geometric properties of cartridge, and regulate its operation characteristic according to the character of treating cargo-carring dispersed solids.
In addition, adjustment feature can allow to be adjusted at the operational factor of the device in the loading process, thus the rising degree of reference particles layer especially.In fact, stratum granulosum rises more, and the height of particle landing is more little, thereby must change the fore-and-aft tilt degree of diversion member so that it is risen again.In this case, opposite with one type of prior art syringe is can advantageously change the fore-and-aft tilt degree of diversion member according to device of the present invention, and not change its rotating speed.
Based on being similar to described just now device, with the version of less size, the patent applicant tests, and can be observed with bulk loading to compare, and (of the present invention) particle loading density obtains about 11% raising.In view of the raising of the transported cargo capacity in given volume, said result clearly demonstrates the benefit of device according to the present invention in the safety of grain transport field and on economy.Except the economy advantage of bringing by the present invention,, also demonstrate its significant advantage on the feature of environmental protection by the fact that given ship can transport many as far as possible grains.
When relating to when using intensive loading attachment by the end user; The adjusting that can be used by user data form can be provided; This form is used to it and illustrates how (especially to consider for example a kind of density of given grain according to the geometric configuration of treating cartridge and the specific nature of treating cargo-carring dispersed solids; Because said density value also can influence the mode of carrying out of loading), the different parameters (size of the vertical and horizontal degree of dip of diversion member, central opening 14 and lateral openings 34 of coming setting device.
Foregoing description is preferred embodiment of the present invention corresponding to what describe with non-limitation mode.Especially, be not to be circumscribed for the expression of the different composed components of intensive loading attachment and the shape of description.
Can for example use the less axle of radius to come the instead of null axle, and the fore-and-aft tilt degree that guarantees diversion member can be independent of the rotating speed of axle and is conditioned.Yet, preferably use hollow shaft because it can eliminate all stress of treating on the cargo-carring dispersed solids passage, up to said dispersed solids with till diversion member contacts.In addition, note also,, on particle drops diversion member, can give speed one rotative component of its particle before in hollow shaft, reduced said friction of granule risk thus because dispersing solid flows.
In addition, those skilled in the art can not run into special difficulty yet when the instruction with this paper is adapted to needing of himself, especially when the suitable groups of the diversion member of axle is counted, (are preferably 3 in selection; 4; 5,6,7 or 8); And during the diversion member quantity of every appropriate (be preferably 1,2 or 3, even greater than 3).
In addition; Under the situation that does not exceed the scope of the invention; Can be described adjusted design automated installation, and the removal device of the recording apparatus of Supervision Loading progress dust that produces when loading, for example be positioned near the water droplet mist atomising installation of loading attachment opening.
To notice that as noted above, the present invention also is used for oil, chemistry and pharmaceutical industries, be used for that for example catalyst is loaded in the container of reaction vessel for example with particle.
Claims (16)
1. one kind is loaded into the device (1) in the container (7) thick and fast with dispersed solids (2); Be used for feeding device (3) cooperation with dispersed solids; Said feeding device (3) is arranged to said dispersed solids is released in the said container; The rainfall shape that on all surfaces of said container, is evenly distributed, said loading attachment comprises
-driven around the axle (4) of axis X 1 with adjustable rotating speed rotation,
-rotate a plurality of diversion members (5) that link to each other with said axle, it is characterized in that said diversion member has the angle that can be independent of said speed adjustment with respect to said axle.
2. device according to claim 1 (1); It is characterized in that; Said axle (4) is hollow, is used to define the passage of said dispersed solids (2), and; At least some said diversion member (5) has the end (16) that is located at apart from axis X1 one segment distance, the distance that said distance is separated less than said axis X 1 and said hollow shaft.
3. device according to claim 2 (1); It is characterized in that; Said hollow shaft (4) is whole cylindrical, and it is conditioned feeder channel (3) cooperation that is used for whole cylindrical circular feeding device, and has the radius that is equal to or less than the feeder channel radius basically; Being used for and said feeder channel cooperation, is unique passage of said dispersed solids thereby make said passage.
4. according to claim 2 or 3 described devices (1); It is characterized in that; Said hollow shaft (4) has opening (14) in its end that is positioned at said container (7) one sides, and some said diversion member (5) has with respect to said opening and is arranged on the inner (16) on the extension of said axle at least.
5. device according to claim 4 (1) is characterized in that, it comprises the regulating mechanism (32) of said opening (14).
6. device according to claim 5 (1) is characterized in that, said regulating mechanism (32) is a barrier film.
7. require each described device (1) in 4 to 6 according to aforesaid right, it is characterized in that said hollow shaft (4) also has a plurality of lateral openings (34), said lateral openings is along the setting of aliging with said diversion member (5) of the direction of said axis X 1.
8. require each described device (1) in 4 to 7 according to aforesaid right; It is characterized in that; It comprises a plurality of retaining elements (17) of diversion member (5); The week that each retaining element part is connected said hollow shaft (4) makes progress, and another part is connected on one of said diversion member, outside said the inner (16).
9. require 8 described devices (1) according to aforesaid right, it is characterized in that, each said retaining element (17) has adjustable length.
10. each described device (1) in requiring according to aforesaid right is characterized in that each said diversion member (5) comprises two parts (28,29), and said two parts (28,29) are interconnective plane basically, thereby make cross-sectional plane V-shaped.
11. require 10 described devices (1), it is characterized in that said planar section (28,29) is separated in the zone, the inner (16) of each said diversion member (5), thereby limit the additional passage (30) that is used for said dispersed solids (2) according to aforesaid right.
12., it is characterized in that it comprises along the first rotation axis A1 that is orthogonal to said axis X 1 regulates at least one first regulating mechanism (22) of the degree of dip of said diversion member (5) according to each described device (1) in the aforesaid right requirement.
13. device according to claim 12 (1) is characterized in that, it comprises along the second rotation axis A2 that is orthogonal to the said first rotation axis A1 regulates at least one second regulating mechanism (24) of the degree of dip of said diversion member (5).
14. according to each described device (1) in the aforesaid right requirement, it is characterized in that said diversion member (5) is arranged in the group of overlapped diversion member, said group centers on said hollow shaft (4) and is distributed regularly.
15. device according to claim 14 (1); It comprises along the first rotation axis A1 that is orthogonal to said axis X 1 regulates at least one first regulating mechanism (22) of the degree of dip of said diversion member; It is characterized in that said first mechanism (22) constitutes same group a whole set of diversion member (5) with identical acting at least with mode simultaneously.
16. device according to claim 15 (1); It comprises along the second rotation axis A2 that is orthogonal to said first axle A1 regulates at least one second regulating mechanism (24) of the degree of dip of said diversion member (5); It is characterized in that said second mechanism (24) constitutes same group a whole set of diversion member (5) with identical acting at least with mode simultaneously.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0956129 | 2009-09-09 | ||
| FR0956129A FR2949755B1 (en) | 2009-09-09 | 2009-09-09 | DEVICE FOR LOADING DENSE OF A DIVIDED SOLID IN AN ENCLOSURE |
| PCT/EP2010/063100 WO2011029815A1 (en) | 2009-09-09 | 2010-09-07 | Device for densely loading a divided solid into a chamber |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102712429A true CN102712429A (en) | 2012-10-03 |
Family
ID=42112008
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010800476037A Pending CN102712429A (en) | 2009-09-09 | 2010-09-07 | Device for densely loading a divided solid into a chamber |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US20120205007A1 (en) |
| EP (1) | EP2475602A1 (en) |
| CN (1) | CN102712429A (en) |
| BR (1) | BR112012005429A2 (en) |
| CA (1) | CA2772819A1 (en) |
| FR (1) | FR2949755B1 (en) |
| WO (1) | WO2011029815A1 (en) |
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Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3599878A (en) * | 1969-06-10 | 1971-08-17 | Dale Corp Van | Distributor apparatus |
| US4040529A (en) * | 1976-05-17 | 1977-08-09 | Wurdeman Marion E | Grain flow propelled grain spreader |
| EP0007854A1 (en) * | 1978-07-20 | 1980-02-06 | COMPAGNIE FRANCAISE DE RAFFINAGE Société anonyme dite: | Device for the distribution of bulk material in an enclosure |
| FR2508612A1 (en) * | 1981-06-27 | 1982-12-31 | Ulrich Beckenbach | LOADING DEVICE FOR A TANK OVEN |
| US4564328A (en) * | 1982-12-30 | 1986-01-14 | Compagnie Francaise De Raffinage | Apparatuses for the loading of an enclosure with a particulate solid |
| CN1061940A (en) * | 1990-10-22 | 1992-06-17 | 法国石油公司 | The equipment that filling bulk products into container is used |
| CN1976853A (en) * | 2004-07-02 | 2007-06-06 | 道达尔法国公司 | Device and method for loading a chamber with a divided solid |
| FR2923816A1 (en) * | 2007-11-15 | 2009-05-22 | Total France Sa | DEVICE AND METHOD FOR LOADING SOLID PARTICLES IN AN ENCLOSURE |
Family Cites Families (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3880300A (en) * | 1974-03-28 | 1975-04-29 | Atlantic Richfield Co | Apparatus for distributing particulate material over a zone |
| US4300725A (en) * | 1979-09-13 | 1981-11-17 | Moherek Edward F | Apparatus for uniformly dispensing and distributing material |
| US4433707A (en) * | 1981-09-25 | 1984-02-28 | Chevron Research Company | Method and apparatus for level loading of vessels using catalyst oriented packing |
| US4611965A (en) * | 1984-06-29 | 1986-09-16 | Dixon Carl R | Gravity-feed grain spreader |
| US4972884A (en) * | 1984-12-07 | 1990-11-27 | Chevron Research & Technology Company | Method and apparatus for uniformly loading particulate material into cylindrical beds |
| US5296202A (en) * | 1984-12-07 | 1994-03-22 | Chevron Research And Technology Co. | Apparatus for uniformly loading particulate material into cylindrical beds |
| US4902185A (en) * | 1985-08-01 | 1990-02-20 | Dixon Carl R | Grain spreader |
| NO175579B1 (en) * | 1991-12-20 | 1994-11-03 | Unidense Technology Gmbh | Method and apparatus for loading particulate material into vertical rudders |
| US5280813A (en) * | 1992-08-07 | 1994-01-25 | Kraft General Foods Canada Inc. | Particle loading system and method |
| US5421379A (en) * | 1993-09-24 | 1995-06-06 | Ctb Inc. | Method and apparatus for distributing granular material within a container |
| US5603359A (en) * | 1993-09-24 | 1997-02-18 | Ctb, Inc. | Method and apparatus for storing material within a container which is exposed to rain |
| GB2287016A (en) * | 1994-03-04 | 1995-09-06 | Technivac Ltd | Charging a container with particulate solids material |
| US5687780A (en) * | 1995-02-14 | 1997-11-18 | Idemitsu Engineering Co., Ltd | Method of feeding catalyst and apparatus for the same |
| FR2740123B1 (en) * | 1995-10-20 | 1998-01-02 | Total Raffinage Distribution | METHOD AND DEVICE FOR THE UNIFORM DISTRIBUTION OF A SOLID IN DIVIDED FORM IN AN ENCLOSURE |
| FR2747937B1 (en) * | 1996-04-26 | 1998-07-17 | Total Raffinage Distribution | METHOD AND DEVICE FOR THE HOMOGENEOUS LOADING OF PARTICLES FROM A SOLID CATALYST INTO A TUBULAR REACTOR |
| US5950694A (en) * | 1998-03-04 | 1999-09-14 | Uop Llc | Apparatus for dispensing particulate material |
| JP2000237577A (en) * | 1998-12-25 | 2000-09-05 | Toyo Eng Corp | Catalyst packing method and device therefor |
| FR2812824B1 (en) * | 2000-08-10 | 2003-05-30 | Total Raffinage Distribution | NEW PROCESS FOR HOMOGENEOUS LOADING OF SOLID PARTICLES INTO AN ENCLOSURE |
| PL1626801T3 (en) * | 2003-04-24 | 2019-08-30 | Cat Tech International Ltd. | Method and apparatus for loading catalyst |
| FR2882029B1 (en) * | 2005-02-14 | 2011-03-11 | Commissariat Energie Atomique | DEVICE FOR DISPENSING AT LEAST ONE GRANULAR MATERIAL IN A CONTAINER, FILLING DEVICE AND FILLING METHOD USING SUCH A DEVICE |
| GB0520088D0 (en) * | 2005-10-04 | 2005-11-09 | Johnson Matthey Plc | Catalyst loading apparatus |
-
2009
- 2009-09-09 FR FR0956129A patent/FR2949755B1/en not_active Expired - Fee Related
-
2010
- 2010-09-07 EP EP10760281A patent/EP2475602A1/en not_active Withdrawn
- 2010-09-07 US US13/395,144 patent/US20120205007A1/en not_active Abandoned
- 2010-09-07 WO PCT/EP2010/063100 patent/WO2011029815A1/en active Application Filing
- 2010-09-07 BR BR112012005429A patent/BR112012005429A2/en not_active Application Discontinuation
- 2010-09-07 CN CN2010800476037A patent/CN102712429A/en active Pending
- 2010-09-07 CA CA2772819A patent/CA2772819A1/en not_active Abandoned
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3599878A (en) * | 1969-06-10 | 1971-08-17 | Dale Corp Van | Distributor apparatus |
| US4040529A (en) * | 1976-05-17 | 1977-08-09 | Wurdeman Marion E | Grain flow propelled grain spreader |
| EP0007854A1 (en) * | 1978-07-20 | 1980-02-06 | COMPAGNIE FRANCAISE DE RAFFINAGE Société anonyme dite: | Device for the distribution of bulk material in an enclosure |
| FR2508612A1 (en) * | 1981-06-27 | 1982-12-31 | Ulrich Beckenbach | LOADING DEVICE FOR A TANK OVEN |
| US4564328A (en) * | 1982-12-30 | 1986-01-14 | Compagnie Francaise De Raffinage | Apparatuses for the loading of an enclosure with a particulate solid |
| CN1061940A (en) * | 1990-10-22 | 1992-06-17 | 法国石油公司 | The equipment that filling bulk products into container is used |
| CN1976853A (en) * | 2004-07-02 | 2007-06-06 | 道达尔法国公司 | Device and method for loading a chamber with a divided solid |
| FR2923816A1 (en) * | 2007-11-15 | 2009-05-22 | Total France Sa | DEVICE AND METHOD FOR LOADING SOLID PARTICLES IN AN ENCLOSURE |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105246583A (en) * | 2013-05-30 | 2016-01-13 | 道达尔炼油化学公司 | Supplying a dispensing device for loading a refinery and/or petrochemical reactor with solid particles |
| CN104355133B (en) * | 2014-10-15 | 2016-08-17 | 长沙中联重科环卫机械有限公司 | Storage bin, storage control method and control device and material loading and unloading equipment |
| CN104355133A (en) * | 2014-10-15 | 2015-02-18 | 长沙中联重科环卫机械有限公司 | Storage bin, storage control method and control device and material loading and unloading equipment |
| CN105615458A (en) * | 2016-04-02 | 2016-06-01 | 邹燕燕 | Dish for distributing vegetables |
| CN105691652A (en) * | 2016-04-02 | 2016-06-22 | 邹燕燕 | Dish-distributing plate |
| CN109051890B (en) * | 2018-09-17 | 2024-05-03 | 涟源市拓鼎科技新材料有限公司 | Anti-segregation dry-mixed mortar storage bin |
| CN109051890A (en) * | 2018-09-17 | 2018-12-21 | 贵州砂浆博士科技有限公司 | A kind of anti-isolation dry-mixed mortar storage silo |
| CN109987262A (en) * | 2019-03-08 | 2019-07-09 | 南安市柳信光电科技有限公司 | A kind of plastic pellet subpackage apparatus fallen using centrifugal drying |
| CN109987262B (en) * | 2019-03-08 | 2021-07-30 | 义乌市亚威机械设备有限公司 | Utilize centrifugation to get rid of plastic granules that falls with partial shipment device |
| US11383836B2 (en) * | 2019-11-22 | 2022-07-12 | Zsm Holdings Llc | Systems and methods for homogeneous cargo or payload space reservation with heterogeneous cargos and payloads |
| US11873115B2 (en) | 2019-11-22 | 2024-01-16 | Zsm Holdings Llc | Systems and methods for homogeneous cargo or payload space reservation with heterogeneous cargos and payloads |
| CN111453081B (en) * | 2020-04-09 | 2021-08-13 | 湖南省天天来米业有限公司 | Rice processing device |
| CN111453081A (en) * | 2020-04-09 | 2020-07-28 | 济南圆纯设计有限公司 | Rice processing device |
| CN111977413A (en) * | 2020-09-02 | 2020-11-24 | 中国计量大学 | Open range adjustable flat storehouse actuating device |
| CN111977413B (en) * | 2020-09-02 | 2022-01-07 | 中国计量大学 | Open range adjustable flat storehouse actuating device |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2011029815A1 (en) | 2011-03-17 |
| EP2475602A1 (en) | 2012-07-18 |
| US20120205007A1 (en) | 2012-08-16 |
| CA2772819A1 (en) | 2011-03-17 |
| BR112012005429A2 (en) | 2016-04-12 |
| FR2949755B1 (en) | 2012-09-28 |
| FR2949755A1 (en) | 2011-03-11 |
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Application publication date: 20121003 |