Device and method for the addition of liquid additives in the form of a spray during a jet milling step in a process for the manufacture of sintered NdFeB alloy magnets
20220105522 ยท 2022-04-07
Inventors
- Yulong ZHAI (Yantai, CN)
- Sijing LYU (Yantai, CN)
- Dajun ZHAO (Yantai, CN)
- Xiaochen ZHAI (Yantai, CN)
- Kaihong DING (Yantai, CN)
Cpc classification
H01F1/0571
ELECTRICITY
B22F2999/00
PERFORMING OPERATIONS; TRANSPORTING
B22F1/107
PERFORMING OPERATIONS; TRANSPORTING
B22F2999/00
PERFORMING OPERATIONS; TRANSPORTING
B02C23/18
PERFORMING OPERATIONS; TRANSPORTING
B22F9/04
PERFORMING OPERATIONS; TRANSPORTING
B22F1/107
PERFORMING OPERATIONS; TRANSPORTING
International classification
Abstract
The present disclosure refers to a device and a method for the addition of liquid additives in the form of a spray during a jet milling step in a process for the manufacture of sintered NdFeB alloy magnets. The device includes: a storage barrel for the liquid additive; a weighing bucket which is in fluid communication with the storage barrel and is adapted for weighing a predetermined amount of the liquid additive; a powder container to accommodate NdFeB alloy material prior to or after jet milling, wherein the powder container includes an opening that is plugged with a blind flange; a connecting pipe, which is in fluid communication with the weighing bucket and passes through an opening of the blind flange into the interior of the powder container; and a fluid atomization nozzle located at the end of the connection pipe.
Claims
1. Device for the addition of liquid additives in the form of a spray during a jet milling step in a process for the manufacture of sintered NdFeB alloy magnets, wherein the device comprises: a storage barrel (1) for the liquid additive; a weighing bucket (2) which is in fluid communication with the storage barrel (1) and is adapted for weighing a predetermined amount of the liquid additive; a powder container (6) to accommodate NdFeB alloy material prior to or after jet milling, wherein the powder container (6) includes an opening (20) that is plugged with a blind flange (5); a connecting pipe (4), which is in fluid communication with the weighing bucket (2) and passes through an opening (5-2) of the blind flange (5) into the interior of the powder container (6); and a fluid atomization nozzle (19) located at the end of the connection pipe (4).
2. The device as claimed in claim 1, wherein a port to the connection pipe (4) is located at a bottom of the weighing bucket (2), the weighing bucket (2) is designed in such a way that the weighed liquid additive is collected at the port to the connection pipe (4) and the weighing bucket (2) further comprises a gas port adapted for applying a pressurized gas in a space above the collected liquid additive.
3. The device as claimed in claim 2, wherein the device comprises a switchable valve (13) adapted for opening and closing the connection tube (4), a switchable valve (15) adapted for opening and closing the gas port, and a control unit (3) which is designed to control the switchable valves (13, 15).
4. The device as claimed in claim 3, wherein the storage barrel (1) is in fluid communication with the storage barrel (1) via a liquid line (8), the device further comprises at least one switchable valve (10, 11) adapted for opening and closing the liquid line (8), and the control unit (3) is designed to control the at least one switchable valve (10, 11).
5. The device as claimed in claim 1, wherein the blind flange (5) further comprises openings (5-1) for air replacement.
6. The device as claimed in claim 1, wherein the storage barrel (1) comprises a filter screen (9) for filtering impurities.
7. The device as claimed in claim 2, wherein the blind flange (5) further comprises openings (5-1) for air replacement.
8. The device as claimed in claim 3, wherein the blind flange (5) further comprises openings (5-1) for air replacement.
9. The device as claimed in claim 4, wherein the blind flange (5) further comprises openings (5-1) for air replacement.
10. The device as claimed in claim 2, wherein the storage barrel (1) comprises a filter screen (9) for filtering impurities.
11. The device as claimed in claim 3, wherein the storage barrel (1) comprises a filter screen (9) for filtering impurities.
12. The device as claimed in claim 4, wherein the storage barrel (1) comprises a filter screen (9) for filtering impurities.
13. A method for the addition of liquid additives in the form of a spray during a jet milling step in a process for the manufacture of sintered NdFeB alloy magnets, wherein the method comprises the steps of: a) providing a device including: a storage barrel (1) for the liquid additive; a weighing bucket (2) which is in fluid communication with the storage barrel (1) and is adapted for weighing a predetermined amount of the liquid additive; a powder container (6) to accommodate NdFeB alloy material prior to or after jet milling, wherein the powder container (6) comprises an opening (20) that is plugged with a blind flange (5); a connecting pipe (4), which is in fluid communication with the weighing bucket (2) and passes through an opening (5-2) of the blind flange (5) into the interior of the powder container (6); and a fluid atomization nozzle (19) located at the end of the connection pipe (4); b) introducing liquid additive from the storage barrel (1) to the weighing bucket (2) and weighing a predetermined amount of the liquid additive; and c) spraying the weighted amount of the liquid additive via the connection pipe (4) and the fluid atomization nozzle (19) into the interior of the powder container (6).
14. The method as claimed in claim 13, wherein a port to the connection pipe (4) is located at a bottom of the weighing bucket (2), the weighing bucket (2) is designed in such a way that the weighed liquid additive is collected at the port to the connection pipe (4) and the weighing bucket (2) further comprises a gas port adapted for applying a pressurized gas in a space above the collected liquid additive, and wherein the pressurized gas is applied to the weighing bucket (2) via the gas port so as to spray the collected liquid additive into the powder container (6).
15. The method as claimed in claim 14, wherein the device comprises a switchable valve (13) adapted for opening and closing the connection tube (4), a switchable valve (15) adapted for opening and closing the gas port, and a control unit (3) which is designed to control the switchable valves (13, 15), and wherein the control unit (3) is opening the both switchable valves (13, 15) for spraying the liquid additive into the powder container (6).
16. The method as claimed in claim 15, wherein the storage barrel (1) is in fluid communication with the storage barrel (1) via a liquid line (8), the device further comprises at least one switchable valve (10, 11) adapted for opening and closing the liquid line (8), and the control unit (3) is designed to control the switchable valve (10, 11), and wherein the control unit (3) is opening the at least one switchable valve (10, 11) for introducing the liquid additive into the weighing bucket (2).
17. The method as claimed in claim 13, wherein the blind flange (5) further comprises openings (5-1) for air replacement, and wherein an inert gas is introduced into the interior of the powder container (6) via the openings (5-1) of the blind flange (5).
18. The method as claimed in claim 13, wherein a first amount of liquid additive is introduced into the powder container (6) and mixed for 0.5 to 2.5 h before starting jet milling, and a second amount of liquid additive is introduced into the powder container (6) and mixed for 2 to 4 h after jet milling.
19. The method as claimed in claim 14, wherein a first amount of liquid additive is introduced into the powder container (6) and mixed for 0.5 to 2.5 h before starting jet milling, and a second amount of liquid additive is introduced into the powder container (6) and mixed for 2 to 4 h after jet milling.
20. The method as claimed in claim 15, wherein a first amount of liquid additive is introduced into the powder container (6) and mixed for 0.5 to 2.5 h before starting jet milling, and a second amount of liquid additive is introduced into the powder container (6) and mixed for 2 to 4 h after jet milling.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0027]
[0028]
[0029]
[0030] The reference signs:
DETAILED DESCRIPTION OF THE INVENTION
[0031] To have a better understanding of the present disclosure, the examples set below provide illustrations of the present disclosure. The examples and the schematics of the device structure are only used to illustrate the present disclosure and do not limit the scope of the present disclosure.
[0032]
[0033] a storage barrel 1 for the liquid additive (such as an antioxidant, for example, a liquid organic ester compound);
[0034] a weighing bucket 2 which is in fluid communication with the storage barrel 1 and is adapted for weighing a predetermined amount of the liquid additive;
[0035] a powder container 6 to accommodate NdFeB alloy material prior to or after jet milling, wherein the powder container 6 includes an opening 20 that is plugged with a blind flange 5;
[0036] a connecting pipe 4, which is in fluid communication with the weighing bucket 2 and passes through an opening 5-2 of the blind flange 5 into the interior of the powder container 6; and
[0037] a fluid atomization nozzle 19 located at the end of the connection pipe 4.
[0038] A port to the connection pipe 4 is located at a bottom of the weighing bucket 2. The weighing bucket 2 is designed in such a way that the weighed liquid additive is collected at the port to the connection pipe 4 and the weighing bucket 2 further includes a gas port adapted for applying a pressurized gas in a space above the collected liquid additive. The weighing bucket 2 further includes a weighing sensor 12 for accurately weighing the liquid additive. The load cell 12 is controlled by a controller unit 3.
[0039] The device includes a switchable valve 13 adapted for opening and closing the connection tube 4, a switchable valve 15 adapted for opening and closing the gas port, and the control unit 3 which is designed to control the switchable valves 13, 15. The device further includes a switchable valve 14 which may be used for exhausting gas from the weighing bucket 2.
[0040] The storage barrel 1 is in fluid communication with the storage barrel 1 via a liquid line 8. The device further includes a switchable valve 10 and a switchable valve 11 adapted for opening and closing the liquid line 8. The control unit 3 is also designed to control the switchable valves 10, 11. Each of the switchable vales 10, 11, and 13-15 may be a solenoid valve. The storage barrel 1 further includes a filter screen 9 for filtering impurities. The liquid line 8 may include a silicone hose, a first sleeve 8-1, and a second sleeve 8-2.
[0041] The blind flange 5 further includes openings 5-1 for air replacement, which is illustrated in
[0042] A method for the addition of liquid additives in the form of a spray during a jet milling step in a process for the manufacture of sintered NdFeB alloy magnets makes use of the above-mentioned device and includes the steps of:
[0043] a) providing the above-mentioned device;
[0044] b) introducing liquid additive from the storage barrel 1 to the weighing bucket 2 and weighing a predetermined amount of the liquid additive; and
[0045] c) spraying the weighted amount of the liquid additive via the connection pipe 4 and the fluid atomization nozzle 19 into the interior of the powder container 6.
[0046] The port to the connection pipe 4 is located at a bottom of the weighing bucket 2. The weighing bucket 2 is designed in such a way that the weighed liquid additive is collected at the port to the connection pipe 4 and the weighing bucket 2 further includes a gas port adapted for applying a pressurized gas (specifically an inert gas, like nitrogen) in a space above the collected liquid additive. The pressurized gas is applied to the weighing bucket 2 via the gas port so as to spray the collected liquid additive into the powder container 6.
[0047] The device includes the switchable valve 13 adapted for opening and closing the connection tube 4, the switchable valve 15 adapted for opening and closing the gas port, and the control unit 3 which is designed to control the switchable valves 13, 15. The control unit 3 is opening the both switchable valves 13, 15 for spraying the liquid additive into the powder container 6.
[0048] The storage barrel 1 is in fluid communication with the storage barrel 1 via the liquid line 8. The device further includes the switchable valves 10 and 11 adapted for opening and closing the liquid line 8, and the control unit 3 is designed to control the switchable valves 10, 11. The control unit 3 is opening the at least one switchable valve 10, 11 for introducing the liquid additive into the weighing bucket 2.
[0049] The blind flange 5 includes openings 5-1 for air replacement, and an inert gas is introduced into the interior of the powder container 6 via the openings 5-1 of the blind flange 5.
[0050] A first amount of liquid additive is introduced into the powder container 6 and mixed for 1 to 2 h before starting jet milling, and a second amount of liquid additive is introduced into the powder container 6 and mixed for 2 to 4 h after jet milling.
[0051] In other words, the disclosure provides an additive atomizing device for a NdFeB magnetic powder mixing process, which includes a storage barrel 1 for storing liquid additives. The cover of the barrel 1 has a sealing ring, and inside the barrel there is a filter screen 9 for filtering impurities in the additive. Preferably, the filter screen size is 60-100 mesh. The bottom of the storage barrel 1 is provided with a solenoid valve 10 and the conical bottom outlet of the storage barrel 1 is provided with a solenoid valve 11 and is used for weighing additives. The weighing bucket 2 is softly connected. The weighing bucket 2 is equipped with a weighing sensor 12, which is electrically connected to the control unit 3 for setting the weight of additives. The weighing bucket 2 is also connected to the connecting pipe 4 by PU tubing through solenoid valve 13. The solenoid valve 14 is used for air vent while weighting. The solenoid valve 15 is connected to the gas source, for example nitrogen. The connecting pipe 4 extends into the powder container 6 through the opening 5-2 of the blind flange 5. One side of the connecting pipe 4 is provided with a quick connector 17. The length of the pipeline 18 can be adjusted according to the size of the powder container. The appropriate length of the pipeline 18 is decided by an angle of the fluid atomizing nozzle 19 at the end of the pipeline 18 and the distance from the nozzle 19 to the powder inside the container 6 and the diameter of the container 6. The blind flange 5 has two openings 5-1, which are used to replace the air in the space between the powder container 6 and the blind flange 5. This avoids the probability of oxygen contact of the powder. The blind flange 5 is sealed with the clamp 7 and connected to the powder container 6.
[0052] Further, the outlet of the storage barrel 1 and the inlet of the weighing bucket 2 are connected by a soft connection, and the operation of the storage barrel 1 will not affect the weighing process of the weighing bucket 2. Specifically, the outlet of the storage barrel 1 is connected to the solenoid valve 10. The first sleeve 8-1 extends into the second sleeve 8-2 with a larger diameter. The first sleeve 8-1 and the second sleeve 8-2 are covered with a silicone hose 8, and the first sleeve 8-1 is connected to the solenoid valve 10. The second sleeve 8-2 is connected to the solenoid valve 11 and the solenoid valve 11 is connected to the inlet of the weighing bucket 2.
[0053] The connecting pipe 4 is provided for intpipeucing the additives into the powder container 6. The connecting pipe 4 is provided with a quick connector 17, and the connecting pipe 4 can be divided into two parts by the quick connector 17, one part of which is connected with the outlet pipe of the weighing bucket 2. Thereby, it is easy to disassemble and clean the device. The other part goes deep into the powder container 6 and connects the fluid atomization nozzle 19 at its end. The length of the pipeline 18 is determined by the height of the powder in the powder container 6 and the spray coverage angle of the fluid atomization nozzle 19. In this way, the atomized additives can cover the powder to the greatest extent.
[0054] The present disclosure provides an additive atomizing adding method of a neodymium iron boron magnetic during the powder mixing process. The additive is a liquid additive. The adding device as above is used. The adding methods are as follows:
[0055] a. Set the additive weight through the control unit 3, then the controller opens the solenoid valve 10 and the solenoid valve 11, and start weighing the additives. When the set weight is reached, the solenoid valve 10 and the solenoid valve 11 are closed.
[0056] b. Connect the blind flange 5 with a clamp 7 to the powder container 6, then open the two replacement ball valves on the flange plates, use nitrogen or argon to replace the space between the blind flange 5 and the upper portion of the container 6 for 1 minute;
[0057] c. Open the powder container's butterfly valve 21, open the third valve on the blind flange 5, put the connecting pipe into the powder container 4 via the valve and keep the air replacement of step b;
[0058] d. Add additives by the control unit 3. At this time, the solenoid valve 11 and the solenoid valve 14 are closed, the solenoid valve 13 and the solenoid valve 15 are opened, and the additive is atomized by air pressure and added to the surface of the powder in the container 6.
[0059] e. After the addition is completed, remove the connecting pipe 4, to close the powder container valve 21, remove blind flange 5 and the replacement gas source.
[0060] Further, the mixing process of NdFeB magnetic powder mixture is as follows:
[0061] 1. Mixing before milling: the additive is added to the powder tank according to the method mentioned above (step a-e), and then mix the powder and the additive with a three-dimensional mixer, in some embodiments, the mixing time is 1-1.5 hours, next the jet milling process is carried out.
[0062] 2. Mixing after milling, the additive is added to a mixer according to the method mentioned above (step a-e), the mixer may be a three-dimensional mixer (mixing in the powder tank of jet milling), V-type mixer, or high shear mixer, in some embodiments, the mixing time are 2-3.5 hours, 2-4 hours, 20-25 minutes, accordingly.
[0063] The present disclosure provides a neodymium iron boron powder with a smaller deviation in C content. The powder is made by jet milling and is obtained by using the device and method of the present disclosure. The powder and ester additives are mixed with a better mixture homogeneity, more specifically, when sampling from 8 different positions of the powder container. The samples C content standard deviation is 20 ppm or less, the extreme deviation is 80 ppm or less.
[0064] Using the NdFeB powder mentioned above, the present disclosure allows manufacturing a high-quality sintered NdFeB magnet by magnetic forming and sintering process. The NdFeB magnet C element content after sintering has relatively small deviation, more specifically, the C element content standard deviation in a single magnet blank is 20 ppm or less, the extreme deviation is 50 ppm or less. Sampling from 13 different positions of of the sintering furnace, the C element content standard deviation is 30 ppm or less, the extreme deviation is 100 ppm or less.
[0065] The present disclosure may provide the following advantages:
[0066] 1. The adding port is separated from the powder container and does not contact with the powder, and the space of the powder container's opening is replaced with nitrogen or argon before adding, so the reduction of magnetic properties and mechanical properties caused by the oxidation of the powder can be avoided. Thus, the yield of magnets increases. At the same time, the atomizing nozzle or the adding port will not be blocked by the powder, so the cleaning and maintenance of the device can be easily applied, and the additive residue is very small.
[0067] 2. The mixture homogeneity of the powder and additives is higher than that of traditional addition methods, and the deviation of C element content is small, which is conducive to obtaining high-performance magnets. Moreover, after powdering, the powder needs only be mixed for one time so the mixing period is significantly shortened.
[0068] The is provided an atomizing liquid adding device and an adding method of a NdFeB magnetic powder mixing process. By adopting the device and the mixing method, the adding device does not directly contact the powder, and the air replacement process in the connecting part is unpieced, which can effectively avoid the oxidation of the powder during the additive adding process, and powder aggregation and blocking in the addition port are also avoided, which makes it easy to clean and maintain. Also, the atomized additive droplets are directly sprayed on the powder during addition, and will not be sprayed on the inner wall of the container to which will cause the powder agglomerate on the wall. This will increase the accuracy of the amount of additive and the mixture homogeneity, compared with the traditional one-time funnel addition method. It can effectively avoid local oxidation of the powder, which is helpful for obtaining high-performance magnets with uniform C content, and can shorten the powder mixing period.
[0069] The device may include a storage barrel containing a sieve screen, and a weighing bucket connected to the bottom of the storage barrel via flexible connection. A load sensor may be fixed to one side of the weighing bucket to weight the additive according to manual setting. The device further includes a connection pipe with a fluid atomizing nozzle at the end and a blind flange connected with the powder container. The powder container of this application is selected as the powder tank or the mixing machine. The blind flange is provided with three outlets, wherein two of them are used for air replacement in the interior of the powder container and one is used for putting through the connecting pipe 4.
[0070] When adding additives, first connect the blind flange to the powder tank or the feeding port of the mixing machine with a gasket and connect them with a clamp. A butterfly valve is set in the opening of the powder tank or the mixing machine. The connecting part between the butterfly valves forms a displacement space. Replace the air in the connecting part with nitrogen or argon. Then, the connecting pipe is inserted into the powder tank or the mixing machine to a certain depth, and the weighed additive in the weighing bucket is atomized to the powder container through air pressure. Finally, the powder and the additive are mixed together. The device and method can obtain NdFeB powder with small deviation of C element content, which means a better mixture homogeneity of the additive and the powder; At the same time, the additive adding process is separated from the powder container body, which effectively avoids the oxidation of the powder and thus improve the mechanical properties and the consistency of the magnetic. Compared with the traditional way of adding the additive by pouring the additive into a funnel on the powder container, the additive and the powder are mixed more uniformly and the mixing cycle can be effectively shortened, particle agglomeration is also effectively avoided, which has high practical value. The solenoid valves and weighing sensor in this application are all electrically connected to the control system, and the control system can be easily implemented by conventional methods in this field, and will not be described in detail.
[0071] In the following examples, a device as illustrated in
Implementing Example 1
[0072] A tank of powder before jet milling and the powder weight was 360 kg, using the device of the present disclosure to atomize and add antioxidants, and then mixed on a three-dimensional mixer for 1.5 hours. During the jet milling process, 8 samples were taken to test the deviation of C element content in the powder.
Implementing Example 2
[0073] After jet milling, two tanks of NdFeB powder weighted 700 kg, were taken into a V-type mixer, using the device of the present disclosure to atomize and add additive, and then mixed for 4 hours. During the following magnetic powder forming process, 8 samples were taken to test the deviation of C element content in the powder.
Implementing Example 3
[0074] After jet milling, two tanks of NdFeB powder weighted 700 kg, were taken into a V-type mixer, using the device of the present disclosure to atomize and add additive, and then mixed for 4 hours. After the subsequent forming and sintering process, 13 blank magnets were sampled from the sintering furnace (corners and edge centers of the upper, middle, and lower layers and the body center) to test the deviation of C element content.
Implementing Example 4
[0075] After jet milling, two tanks of NdFeB powder weighted 700 kg, were taken into a V-type mixer, using the device of the present disclosure to atomize and add additive, and then mixed for 4 hours. After the subsequent forming and sintering process, took one sample from the furnace and according to
Comparative Example 1
[0076] A tank of powder before jet milling and the powder weight was 360 kg, using a conventional method to intpipeuce the same amount of additives from the opening on the cone wall of the powder container with a funnel, and then mixed on a three-dimensional mixer for 1.5 hours. During the jet milling process, 8 samples were taken to test the deviation of C element content in the powder.
Comparative Example 2
[0077] After jet milling, two tanks of NdFeB powder weighted 700 kg, were pre-mixed in the powder tank with a three-dimensional mixer for 1.5 hours, and then took the 2 tanks of powder into a V-mixer for 4 hours. During the following magnetic powder forming process, 8 samples were taken to test the deviation of C element content in the powder.
Comparative Example 3
[0078] After jet milling, two tanks of NdFeB powder weighted 700 kg, were pre-mixed in the powder tank with a three-dimensional mixer for 1.5 hours, and then took the 2 tanks of powder into a V-mixer for 4 hours. After the subsequent forming and sintering process, 13 blank magnets were sampled from the sintering furnace (corners and edge centers of the upper, middle, and lower layers and the body center) to test the deviation of C element content.
Comparative Example 4
[0079] After jet milling, two tanks of NdFeB powder weighted 700 kg, were pre-mixed in the powder tank with a three-dimensional mixer for 1.5 hours, and then took the 2 tanks of powder into a V-mixer for 4 hours. After the subsequent forming and sintering process, took one sample from the furnace and according to
[0080] The C element content of the above examples are shown in table 1 to table 4 as follows:
TABLE-US-00001 TABLE 1 C element C element Num. Example content Example content 1 IMPLEMENTING 0.0443 COMPARATIVE 0.0497 2 EXAMPLE 1 0.0449 EXAMPLE 1 0.0502 3 0.0449 0.0510 4 0.0453 0.0485 5 0.0446 0.0480 6 0.0430 0.0504 7 0.0449 0.0481 8 0.0442 0.0490
[0081] Table 1 shows 8 results of the C content deviation of the implementing example 1 and comparative example 1 during the jet milling process.
TABLE-US-00002 TABLE 2 C element C element Num. Example content Example content 1 IMPLEMENTING 0.0453 COMPARATIVE 0.0330 2 EXAMPLE 2 0.0438 EXAMPLE 2 0.0341 3 0.0430 0.0352 4 0.0424 0.0335 5 0.0405 0.0477 6 0.0411 0.0345 7 0.0409 0.0364 8 0.0441 0.0341
[0082] Table 2 shows 8 results of the C content deviation of the implementing example 2 and comparative example 2 during the magnetic forming process.
TABLE-US-00003 TABLE 3 C element C element Num. Example content Example content 1 IMPLEMENTING 0.0746 COMPARATIVE 0.0623 2 EXAMPLE3 0.0768 EXAMPLE 3 0.0580 3 0.0771 0.0547 4 0.0766 0.0587 5 0.0759 0.0589 6 0.0764 0.0542 7 0.0766 0.0555 8 0.0768 0.0606 9 0.0770 0.0610 10 0.0772 0.0617 11 0.0837 0.0580 12 0.0770 0.0688 13 0.0741 0.0634
[0083] Table 3 shows the C content deviation of implementing example 3 and comparative example 3.
TABLE-US-00004 TABLE 4 C element C element Num. Example content Example content 1 IMPLEMENTING 0.0557 COMPARATIVE 0.0725 2 EXAMPLE 4 0.0525 EXAMPLE 4 0.0677 3 0.0525 0.0755 4 0.0535 0.0666 5 0.0558 0.0816 6 0.0542 0.0695 7 0.0526 0.0699 8 0.0571 0.0686 9 0.0542 0.0682
[0084] Table 4 shows the deviation of C content results of the implementing example 4 and comparative example 4 according to
[0085] The deviation results of the above examples and comparative examples are shown in table 5:
TABLE-US-00005 TABLE 5 Example Standard deviation/ppm [max-min]/ppm COMPARATIVE EXAMPLE1 11 30 IMPLEMENTING EXAMPLE 1 7 23 COMPARATIVE EXAMPLE2 48 147 IMPLEMENTING EXAMPLE2 17 48 COMPARATIVE EXAMPLE3 40 146 IMPLEMENTING EXAMPLE3 22 96 COMPARATIVE EXAMPLE4 47 150 IMPLEMENTING EXAMPLE4 16 45
[0086] For implementing example 1 and comparative example 1: The accuracy of the amount of additive and the mixture homogeneity is increased, compared with the traditional one-time funnel addition method, it can effectively avoid local oxidation of the powder, which is helpful for obtaining high-performance magnets with uniform C content, and can shorten the powder mixing period 7 ppm and 11 ppm respectively. The [max-min] value of the C content are 7 ppm and 23 ppm. It's clear that the implementing of this present disclosure has a smaller C element content deviation, which means a better mixture homogeneity and conventional uniformity, besides, implementing example has a lower mixing cycle.
[0087] For implementing example 2 and comparative example 2 after jet milling: the standard deviation of the C content are 17 ppm and 48 ppm respectively, the [max-min] value of the C content are 48 ppm and 147 ppm, the implementing example of this present disclosure has a much smaller C content deviation and a obviously shorter mixing cycle.
[0088] For implementing example 3, implementing example 4 and comparative example 3, comparative example 4: after powder magnetic forming and sintering process, the C element content deviation of the magnets made by the present disclosure are much smaller to magnets made by the conventional way. Which means a better consistency in magnetic performance.
[0089] In addition, according to the statistics on the yield of magnets, the defects of foreign matter in the magnets caused by the oxidation of the powder have been reduced from 0.15% to 0.07%.
[0090] In summary, by using the device and method of the present disclosure, the chance of powder oxidation is effectively avoided, thus reduction of magnetic properties and mechanical properties caused by powder oxidation is also reduced, so the yield rate of the magnets is improved, and since the powder will not block the adding port and the atomizing nozzle, the cleaning and maintenance process is simple and the additive residue is less. In addition, the mixture homogeneity of the powder is much better than that of the traditional way, which is good for obtaining uniform, stable and consistent NdFeB magnets, besides, the mixing cycle is significantly shortened.