CN104307435A - Granulator - Google Patents
Granulator Download PDFInfo
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- CN104307435A CN104307435A CN201410599782.5A CN201410599782A CN104307435A CN 104307435 A CN104307435 A CN 104307435A CN 201410599782 A CN201410599782 A CN 201410599782A CN 104307435 A CN104307435 A CN 104307435A
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- granulating
- granulator
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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
- B01J2/00—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic
- B01J2/14—Processes or devices for granulating materials, e.g. fertilisers in general; Rendering particulate materials free flowing in general, e.g. making them hydrophobic in rotating dishes or pans
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- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention discloses a granulator which continuously and stably operates. The granulator comprises a material melting device, a material dripping mechanism, a rotary granulating and receiving plate, a material scraping mechanism and a granule collecting device, which are correspondingly arranged, wherein the material scraping mechanism comprises a scraping head; the rotary granulating and receiving plate comprises a plate body and a rotating shaft connected with the plate body; the scraping head and the plate body are placed in a sealable granulating bin; the material melting device and the material dripping mechanism are also placed in the granulating bin; a flow guide chamber communicated with a heat conducting flow medium circulating device is formed in the plate body; the rotary granulating and receiving plate can be finely adjusted up and down; the center distance and the distance between a dripping nozzle of the material dripping mechanism and the rotary granulating and receiving plate as well as the center distance and the distance between the scraping head and the rotary granulating and receiving plate can be also finely adjusted; in the normal working process, materials in the passage of the material dripping mechanism are not condensed to prevent blockage and equipment continuously and stably operates; the rotary granulating and receiving plate has the advantages of active cooling or heating functions, high material drop solidification speed and high granulating efficiency; the granulator disclosed by the invention can be suitable for granulating of various raw materials.
Description
Technical field
The present invention relates to a kind of granulator, especially a kind of granulator being suitable for high purity metal or nonmetallic materials granulation.
Background technology
At present, on the whole the technique that high purity metal or nonmetallic materials are granulated be divided into dry granulation and wet granulation two class.Dry granulation generally adopts gas shielding condition, prevents metal or nonmetal oxidation by air from affecting its purity and serviceability with inert gas.Warm therapy is granulated and general is adopted liquid medium protected mode, with water or water mixed solvent for becoming granule medium.
After the granulation device of high purity metal or nonmetallic materials usually adopts and is melted by heating raw materials, by tear drop granulating, granulation device comprises melting charge device and tear drop mechanism, the raw material of melting in melting charge device flows into gob feeder structure, oozing successively from the drip nozzle of tear drop mechanism and fall to rotate granulating receiver (dry method) or fall into fills in the splicing groove (wet method) of granule medium, be frozen into graininess, then collected by collection grain device.
Existing dry granulating machine comprises the granulation storehouse and the corresponding melting charge device arranged that are provided with melt import, tear drop mechanism, rotate granulating receiver, scraping mechanism and collection grain device, it is outside that melting charge device and tear drop mechanism are positioned at granulation storehouse, rotate the disk body of granulating receiver, the import of scraping head and collection grain device of scraping mechanism is positioned at inside, granulation storehouse, rotate the drive unit of granulating receiver, it is outside that the drive unit of scraping mechanism and the outlet of collection grain device are positioned at granulation storehouse, in the adaptive corresponding sealing in parts and granulation bulkhead junction, granulation storehouse is provided with inflation inlet or bleeding point, adaptive sealed valve.Melting charge device is the heating container that opening is arranged at bottom, and opening is by putty rod seal, and tear drop mechanism is the container with heat insulation function, container bottom is provided with one or more drip nozzle, according to the difference of raw material, different tear drop mechanisms can be changed, for regulating and controlling the speed that feed liquid is dripped.
When starting granulator, raw material is loaded melting charge device, inert gas is filled with to granulation storehouse, after completing protective gas displacement, open heating, melting sources after constant temperature, promote putty bar, feed liquid flows out in tear drop mechanism from the opening of melting charge device, to drip on the granulating receiver disk body that tear drop mechanism rotates in granulation storehouse feed liquid, near the general corresponding edge of rotating granulating receiver of melt import, scraping mechanism is provided with above the side of rotation granulating receiver, head place is scraped along with rotation granulating receiver turns to it, drop on from tear drop mechanism gob out and rotate granulating receiver and solidify granulating, the head of scraping rotated scrapes blanking grain from rotation granulating receiver, the material grain solidified is pooled in collection grain device under gravity naturally.Normally used head of scraping is that lath scraped in cross.
The defect of existing dry granulating machine is; owing to not arranging sealing between the drip nozzle of tear drop mechanism and granulation storehouse; in pelletization, material oxidation is serious; and the inert gas be filled with flows out through this place, form the cooling effect to drip nozzle, its validity of Insulation therefore for drip nozzle is poor; easily occur that drip nozzle blocks; process separately after needing to shut down the connection splitting out granulation storehouse and tear drop mechanism after blocking, therefore continuity, the reliability run of equipment is poor, and granulation efficiency is not high again.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of granulator of continuous and steady operation.
The technical solution adopted for the present invention to solve the technical problems is: granulator; comprise the melting charge device of corresponding layout, tear drop mechanism, rotate granulating receiver, scraping mechanism and collection grain device; scraping mechanism comprises it and scrapes head; rotate the rotating shaft that granulating receiver comprises disk body and is connected with disk body; scrape head and disk body is placed in sealable granulation storehouse, melting charge device and tear drop mechanism are also arranged in this granulation storehouse.
The inside of described disk body has the diversion cavity be communicated with thermal conductive fluid medium EGR.
Medium admission passage, the medium flow pass of mutually isolated setting in described rotating shaft are all communicated with described diversion cavity, rotating shaft is connected with thermal conductive fluid medium EGR by medium turnover joint, rotating shaft and medium pass in and out joint and are rotatably assorted, and the medium of the inner mutually isolated setting of described medium turnover joint enters groove and is communicated with medium spout is corresponding with the opening of medium admission passage, medium flow pass respectively.
Described disk body is made up of upper dish and lower wall, and one end of rotating shaft is connected with rack-mounted drive unit, and the other end of rotating shaft is connected with lower wall, and upper dish is connected on lower wall, is provided with sealing ring between lower wall and upper dish, forms diversion cavity between upper dish and lower wall.
The material of described upper dish is stainless steel alloy, graphite, titanium or titanium alloy.
The outlet opening of described melting charge bottom of device is truncated cone-shaped hole, and is fitted with the putty bar suitable with outlet opening, and described putty bar is connected with putty bar hoisting mechanism.
Described melting charge device is the silica crucible or the ceramic crucible that are equipped with heater and insulation construction, and putty bar adopts quartz to make, and tear drop mechanism is the silica crucible of the band drip nozzle being equipped with heater and insulation construction.
Be connected with frame by rotating shaft lifting regulating mechanism after described rotating shaft passes granulation storehouse, between rotating shaft with its drive unit, expansion fit is connected.
Described scraping mechanism to scrape head adjustable relative to the spacing distance of disk body.
Described head pivot point line of scraping is adjustable relative to the distance of the center line of disk body.
The invention has the beneficial effects as follows: product is not oxidizable, and purity is guaranteed, in tear drop mechanism passage, material not easily condenses blocking, and equipment runs continous-stable; Rotate granulating receiver and have active cooling or intensification function, gob solidifies rapidly, and granulation efficiency improves; Rotate granulating receiver can finely tune up and down, the drip nozzle of tear drop mechanism, to scrape head adjustable relative to the centre-to-centre spacing and spacing of rotating granulating receiver, can be adapted to the granulation of plurality of raw materials.
Accompanying drawing explanation
Fig. 1 is the front view (the A-A sectional view of Fig. 2) of granulator of the present invention.
Fig. 2 is the B direction view of Fig. 1.
Fig. 3 is the structure chart rotating granulating receiver in Fig. 1.
Fig. 4 is the front view of Fig. 3 shaft.
Fig. 5 is the C direction view of Fig. 4.
Fig. 6 is the front view of lower wall in Fig. 3.
Fig. 7 is the D direction view of Fig. 6.
Fig. 8 is the front view of upper dish in Fig. 3.
Fig. 9 is the E direction view of Fig. 8.
Be labeled as in figure: melting charge device 1, granulation storehouse 2, scraping mechanism 3, tear drop mechanism 4, rotate granulating receiver 5, collection grain device 6, frame 7, putty bar 8, putty bar hoisting mechanism 9, drive unit 10, sidewall 20, upper cover plate 21, observation window 22, interface 23, casing 30, scrape 31, drip nozzle 41, shaft coupling 51, medium turnover joint 52, rotating shaft 53, rotating shaft lifting regulating mechanism 54, rotating shaft sealing 55, disk body 56, diversion cavity 57, top seal 81, connecting rod 82, medium enters groove 521, medium spout 522, medium admission passage 531, medium flow pass 532, Adjusting bolt Adjusting screw 541, nut 542, upper dish 561, lower wall 562, sealing ring 563.
Detailed description of the invention
Below in conjunction with drawings and Examples, the present invention is further described.
As Fig. 1, Fig. 2, shown in Fig. 3 ~ Fig. 9, granulator of the present invention comprises the corresponding melting charge device 1 arranged, tear drop mechanism 4, rotate granulating receiver 5, scraping mechanism 3 and collection grain device 6, scraping mechanism 3 comprises it and scrapes 31, rotate granulating receiver 5 comprise disk body 56 and be connected with disk body 56 and the rotating shaft 53 that disk body 56 can be driven to rotate, scrape 31 and disk body 56 be placed in sealable granulation storehouse 2, granulation storehouse 2 is provided with the interface 23 for inflating or bleed, interface is equipped with valve 23, and interface 23 place adaptation has corresponding sealing, melting charge device 1 and tear drop mechanism 4 are also arranged in this granulation storehouse 2, because storehouse 2 of granulating under running status is for confined space, after vacuumizing and be filled with inert gas purge, product is not oxidizable, purity is guaranteed, when melting charge device 1 heats or is incubated, its partial heat conducts to bottom, granulation storehouse 2 by thermal-radiating mode, be conducive to the temperature maintaining material in storehouse, thus avoid the appearance of tear drop mechanism drip nozzle clogging, the operation stability of granulator is improved greatly.
Due to aforesaid thermal-radiating existence, on the solidification of rotating gob on granulating receiver more or less there is some impact.If the surface tension of raw material is enough large, so its condensation granulating is influenced hardly, and for the raw material that surface tension is natively relatively little, this heat radiation just cannot be ignored the impact of particle shape.For this reason, consider with active cooling method to rotate granulating receiver and on gob cool, to offset described impact.For influenced less raw material, active cooling also improves its cooling velocity, thus suitably can increase the rotating speed and corresponding gob speed that rotate granulating receiver, improves granulation efficiency.For realizing this object, as Fig. 1, shown in Fig. 3, a kind of mode that can realize is provided with diversion cavity 57 in described disk body 56 inside, the medium admission passage 531 of mutually isolated setting in rotating shaft 53, medium flow pass 532 is all communicated with described diversion cavity 57, rotating shaft 53 is connected with thermal conductive fluid medium EGR by medium turnover joint 52, rotating shaft 53 and medium pass in and out joint 52 and are rotatably assorted, the medium of the inner mutually isolated setting of described medium turnover joint 52 enter groove 521 and medium spout 522 respectively with medium admission passage 531, the corresponding connection of opening of medium flow pass 532, thus both achieved rotating shaft 53 freely rotating together with disk body 56, achieve again being fixedly connected with of medium turnover joint 52 and thermal conductive fluid medium EGR.Certainly other can realize disk body 56 and rotates and be also fine to the mode that it cools simultaneously.
As shown in Fig. 3, Fig. 4, Fig. 5, Fig. 6, Fig. 7, Fig. 8 and Fig. 9, described disk body 56 is made up of upper dish 561 and lower wall 562, one end of rotating shaft 53 is connected with the drive unit 10 be arranged in frame 7, the other end of rotating shaft 53 is connected with lower wall 562, lower wall 562 is provided with the hole communicated respectively with medium admission passage 531, medium flow pass 532, upper dish 561 is connected on lower wall 562, be provided with sealing ring 563 between lower wall 562 and upper dish 561, between upper dish 561 and lower wall 562, form diversion cavity 57.Disk body 56 makes subdivision combining structure, is not only convenient to the shaping of diversion cavity 57, simultaneously also conveniently makes upper dish 561 according to different raw materials with different materials, and upper dish 561 wear and tear after reparation or replacing.
As previously mentioned, for keeping the purity of material grain, can make upper dish 561 according to different raw materials with different materials, generally speaking, the material of upper dish 561 can select graphite or carbide alloy, and especially hard stainless steel, rigid titanium alloy, also can use pure titanium.
As shown in Figure 1, the outlet opening bottom described melting charge device 1 is truncated cone-shaped hole, and is fitted with the putty bar 8 suitable with outlet opening, and the upper end of described putty bar 8 is connected with putty bar hoisting mechanism 9 by connecting rod 82.Regulated by putty bar hoisting mechanism 9 and keep, between the outlet opening of putty bar 8 and melting charge device 1, there is reasonable clearance, the load in melting charge device 1 unit interval is made to equal the doses of dripping from tear drop mechanism 4, liquid level in tear drop mechanism 4 can be made to keep constant, be conducive to the stable operation of equipment.Different material, after fusing, under different state of temperatures, its surface tension is not identical.In order to the granulation operation of different raw materials can be adapted to, need to regulate the flow of melting charge device 1 to tear drop mechanism 4 according to the flow of tear drop mechanism 4, namely need to regulate the aperture of outlet opening, described putty bar hoisting mechanism 9 is the governor motion that putty bar can be driven to be elevated, and its degree of regulation General Requirements micron order is to grade.
Described melting charge device 1 is preferably chosen as the silica crucible or ceramic crucible that are equipped with heater and insulation construction, putty bar 8 also adopts quartz to make simultaneously, tear drop mechanism 4 is preferably chosen as the silica crucible being equipped with heater and insulation construction, utilize the stability of quartzy chemical property, overwhelming majority raw material all not with its reaction, be conducive to the purity ensureing product material grain.Under the less demanding situation of product purity, also can consider to be easy to mach stainless steel and make melting charge device 1 and tear drop mechanism 4.
As shown in Figure 1, described rotating shaft 53 is connected with frame 7 by rotating shaft lifting regulating mechanism 54 after passing granulation storehouse 2, be connected by shaft coupling 51 between rotating shaft 53 with its drive unit 10, between rotating shaft 53 with described shaft coupling 51, expansion fit is connected, thus can the spacing between the drip nozzle of tear drop mechanism 4 and disk body 56 be adjusted, make it to adapt with raw material to be processed.Because spacing is excessive, can falls apart after gob touches disk body 56 and spatter, not easily granulating.But spacing is too small, gob is too short again for the cool time before touching disk body 56, is also unfavorable for granulating.For simplicity, rotating shaft lifting regulating mechanism 54 generally adopts spiral lifting mechanism, such as, structure described in embodiment.Obviously, keep disk body 56 to be relatively fixing, Di Li mechanism 4 is designed to the height adjustable relative to disk body 56, and the spacing that also can realize between the two is adjustable, and such scheme is the equivalent of this section of aforementioned schemes.
As shown in Figure 1, what described scraping mechanism 3 comprised casing 30 and stretched out casing 30 scrapes 31, described casing 30 is fixedly connected with the sidewall 20 in granulation storehouse 2, describedly scrape 31 relative to the scalable adjustment of casing 30, thus after the position of disk body 56 is determined, carry out corresponding adjustment to a spacing of scraping between 31 to disk body 56 as required, making it scrape 31 can normally work.Due to the lighter weight of scraping mechanism 3 own, therefore, select scraping mechanism 3 entirety can regulate relative to disk body 56 and be highly also fine, but under this mode, scraping mechanism 3 is preferably connected with the top in granulation storehouse 2, reliably and easily seals while connecting so that reliable.
As shown in Figure 1; the top in described granulation storehouse 2 is provided with upper cover plate 21 to be opened/closed; the convenient installation to interior arrangement and maintenance; certain granulation storehouse 2 also can arrange side door to be opened/closed, meanwhile, in order to observe the working condition of granulator at any time; the sidewall 20 in granulation storehouse 2 is also provided with observation window 22; observation window 22 is mainly used in observation tear drop mechanism and whether scraping mechanism can normally work, and the condensation situation of material grain, and the height of observation window setting height(from bottom) that is general and disk body 56 is suitable.
embodiment:
As Fig. 1, shown in Fig. 2, granulator of the present invention comprises the sealable granulation storehouse 2 be arranged in frame 7, granulation storehouse 2 is provided with the interface 23 for inflating or bleed, interface 23 should be equipped with valve, and interface 23 place adaptation has corresponding sealing, the corresponding melting charge device 1 arranged, tear drop mechanism 4, rotate granulating receiver 5, scraping mechanism 3 and collection grain device 6, melting charge device 1 and tear drop mechanism 4 are arranged in granulation storehouse 2, melting charge device 1 hanging is connected on the fixing top board in granulation storehouse 2, fixing top board is connected with upper cover plate 21 to be opened/closed, melting charge device 1 is for being equipped with silica crucible or the ceramic crucible of heater and insulation construction, the outlet opening of bottom is truncated cone-shaped hole, and be fitted with the putty bar 8 of the quartzy material suitable with outlet opening, tear drop mechanism 4 is for being equipped with the silica crucible of the band drip nozzle 41 of heater and insulation construction.
The upper end of described putty bar 8 is connected with one end of connecting rod 82, the other end that described connecting rod 82 passes granulation storehouse 2 is connected with putty bar hoisting mechanism 9, connecting rod 82 and junction, granulation storehouse 2 are provided with top seal 81, tear drop mechanism 4 by support installing on the base plate in granulation storehouse 2, the drip nozzle correspondence of tear drop mechanism 4 is positioned at above the edge of rotation granulating receiver 5, rotate the rotating shaft 53 that granulating receiver 5 comprises disk body 56 and is connected with disk body 56, scraping mechanism 3 comprises casing 30 and scrapes 31, scrape 31 and disk body 56 be placed in granulation storehouse 2, frame 7 is provided with the rotating shaft 53 be connected with the disk body 56 of granulating in storehouse 2, rotating shaft 53 and junction, granulation storehouse 2 are provided with rotating shaft sealing 55, one end that granulation storehouse 2 is stretched out in rotating shaft 53 is connected with shaft coupling 51 relative telescopic, but rotating shaft 53 and shaft coupling 51 can not relatively rotate, shaft coupling 51 is connected with the motor as drive unit 10, frame 7 is also provided with the medium be connected with thermal conductive fluid medium EGR and passes in and out joint 52, rotating shaft 53 and medium pass in and out joint 52 and are rotatably assorted, and multiple sealing ring is provided therebetween, the medium of the inner mutually isolated setting of described medium turnover joint 52 enter groove 521 and medium spout 522 respectively with the medium admission passage 531 of mutually isolated setting in rotating shaft 53, the corresponding connection of opening of medium flow pass 532, medium enters groove 521 and medium spout 522 is the annular groove coaxial with rotating shaft 53, the both sides of annular groove are provided with sealing ring, described disk body 56 is made up of upper dish 561 and lower wall 562, upper dish 561 is connected on lower wall 562, one end that rotating shaft 53 is positioned at granulation storehouse 2 is connected with lower wall 562, lower wall 562 is provided with and medium admission passage 531, the hole that medium flow pass 532 communicates respectively, sealing ring 563 is provided with between lower wall 562 and upper dish 561, diversion cavity 57 is formed between upper dish 561 and lower wall 562, rotating shaft 53 passes in and out between joint 52 at lower wall 562 and medium and is provided with the shaft shoulder, the nut 542 that this shaft shoulder place is fixedly connected with Adjusting bolt Adjusting screw 541 and is threaded with it, nut 542 is arranged in frame 7, thus define can telescopic adjustment again can the rotation granulating receiver 5 of active cooling or intensification.Scrape 31 and also can refer to such mode with the connection of casing 30, namely make not only flexible but can rotate scrape 31, simultaneously, scrape 31 rotary centerline adjustable relative to the distance of the center line of disk body 56, thus scrape head and can regulate in the distance at the center of the radial distance disk body 56 of disk body 56, namely scrape head slightly to adjust to center or to edge, scrape grain operation better to complete, this adjustment also can realize with reference to the connected mode of rotating shaft 53 with its drive unit.The sidewall 20 in granulation storehouse 2 is also provided with observation window 22.
Claims (10)
1. granulator; comprise the melting charge device (1) of corresponding layout, tear drop mechanism (4), rotate granulating receiver (5), scraping mechanism (3) and collection grain device (6); scraping mechanism (3) comprises it and scrapes head (31); rotate the rotating shaft (53) that granulating receiver (5) comprises disk body (56) and is connected with disk body (56); it is characterized in that: scrape head (31) and disk body (56) is placed in sealable granulation storehouse (2), melting charge device (1) and tear drop mechanism (4) are also arranged in this granulation storehouse (2).
2. granulator as claimed in claim 1, is characterized in that: the inside of described disk body (56) has the diversion cavity (57) be communicated with thermal conductive fluid medium EGR.
3. granulator as claimed in claim 2, it is characterized in that: the medium admission passage (531) of the upper mutually isolated setting of described rotating shaft (53), medium flow pass (532) is all communicated with described diversion cavity (57), rotating shaft (53) passes in and out joint (52) by medium and is connected with thermal conductive fluid medium EGR, rotating shaft (53) and medium pass in and out joint (52) and are rotatably assorted, the medium of described medium turnover joint (52) inner mutually isolated setting enter groove (521) and medium spout (522) respectively with medium admission passage (531), the corresponding connection of opening of medium flow pass (532).
4. granulator as claimed in claim 2; it is characterized in that: described disk body (56) is made up of upper dish (561) and lower wall (562); one end of rotating shaft (53) is connected with the drive unit (10) be arranged in frame (7); the other end of rotating shaft (53) is connected with lower wall (562); upper dish (561) is connected on lower wall (562); be provided with sealing ring (563) between lower wall (562) and upper dish (561), between upper dish (561) and lower wall (562), form diversion cavity (57).
5. granulator as claimed in claim 4, is characterized in that: the material of described upper dish (561) is stainless steel, graphite, titanium or titanium alloy.
6. granulator as claimed in claim 1, is characterized in that: the outlet opening of described melting charge device (1) bottom is truncated cone-shaped hole, and is fitted with the putty bar (8) suitable with outlet opening, and described putty bar (8) is connected with putty bar hoisting mechanism (9).
7. granulator as claimed in claim 6; it is characterized in that: described melting charge device (1) is for being equipped with silica crucible or the ceramic crucible of heater and insulation construction; putty bar (8) adopts quartz to make, and tear drop mechanism (4) is for being equipped with the silica crucible of the band drip nozzle (41) of heater and insulation construction.
8. as the granulator in claim 1 ~ 7 as described in any one claim; it is characterized in that: described rotating shaft (53) is passed granulation storehouse (2) and is connected with frame (7) by rotating shaft lifting regulating mechanism (54) afterwards, and between rotating shaft (53) with its drive unit (10), expansion fit is connected.
9., as the granulator in claim 1 ~ 7 as described in any one claim, it is characterized in that: described in scrape head (31) adjustable relative to the spacing distance of disk body (56).
10., as the granulator in claim 1 ~ 7 as described in any one claim, it is characterized in that: described in scrape the rotary centerline of head (31) adjustable relative to the distance of the center line of disk body (56).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410599782.5A CN104307435B (en) | 2014-10-31 | 2014-10-31 | Granulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410599782.5A CN104307435B (en) | 2014-10-31 | 2014-10-31 | Granulator |
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| Publication Number | Publication Date |
|---|---|
| CN104307435A true CN104307435A (en) | 2015-01-28 |
| CN104307435B CN104307435B (en) | 2016-09-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410599782.5A Active CN104307435B (en) | 2014-10-31 | 2014-10-31 | Granulator |
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| Country | Link |
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| CN (1) | CN104307435B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112122618A (en) * | 2020-09-25 | 2020-12-25 | 广东先导稀材股份有限公司 | Scattered metal granulating equipment |
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| US3778044A (en) * | 1971-07-13 | 1973-12-11 | C Brown | Method and apparatus for recovery and refining of zinc |
| SU1301804A1 (en) * | 1985-11-22 | 1987-04-07 | Донецкий Филиал Научно-Исследовательского И Проектного Института По Очистке Технологических Газов,Сточных Вод И Использованию Вторичных Энергоресурсов Предприятий Черной Металлургии | Arrangement for granulating slag melt |
| JPH03284342A (en) * | 1990-03-30 | 1991-12-16 | Kawasaki Heavy Ind Ltd | Method and apparatus for granulation & coloring treatment of molten sludge |
| SU1775949A1 (en) * | 1990-12-29 | 1995-05-20 | Всесоюзный институт легких сплавов | Installation for production of metal powder from melt |
| CN201445946U (en) * | 2009-08-14 | 2010-05-05 | 陕西省轻工业研究设计院 | Oval granulator |
| CN102248169A (en) * | 2011-04-28 | 2011-11-23 | 尉氏中州有色金属材料有限公司 | Comprehensive crushing machine for waste aluminum and aluminum alloy sheet, swing knife and crushing method |
| CN204193882U (en) * | 2014-10-31 | 2015-03-11 | 四川鑫龙碲业科技开发有限责任公司 | Granulator |
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Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3778044A (en) * | 1971-07-13 | 1973-12-11 | C Brown | Method and apparatus for recovery and refining of zinc |
| SU1301804A1 (en) * | 1985-11-22 | 1987-04-07 | Донецкий Филиал Научно-Исследовательского И Проектного Института По Очистке Технологических Газов,Сточных Вод И Использованию Вторичных Энергоресурсов Предприятий Черной Металлургии | Arrangement for granulating slag melt |
| JPH03284342A (en) * | 1990-03-30 | 1991-12-16 | Kawasaki Heavy Ind Ltd | Method and apparatus for granulation & coloring treatment of molten sludge |
| SU1775949A1 (en) * | 1990-12-29 | 1995-05-20 | Всесоюзный институт легких сплавов | Installation for production of metal powder from melt |
| CN201445946U (en) * | 2009-08-14 | 2010-05-05 | 陕西省轻工业研究设计院 | Oval granulator |
| CN102248169A (en) * | 2011-04-28 | 2011-11-23 | 尉氏中州有色金属材料有限公司 | Comprehensive crushing machine for waste aluminum and aluminum alloy sheet, swing knife and crushing method |
| CN204193882U (en) * | 2014-10-31 | 2015-03-11 | 四川鑫龙碲业科技开发有限责任公司 | Granulator |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112122618A (en) * | 2020-09-25 | 2020-12-25 | 广东先导稀材股份有限公司 | Scattered metal granulating equipment |
| CN112122618B (en) * | 2020-09-25 | 2023-04-07 | 江苏先导微电子科技有限公司 | Scattered metal granulating equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104307435B (en) | 2016-09-21 |
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