WO2022142527A1 - Procédé de condensation pulsé pour la préparation de poudre métallique - Google Patents
Procédé de condensation pulsé pour la préparation de poudre métallique Download PDFInfo
- Publication number
- WO2022142527A1 WO2022142527A1 PCT/CN2021/120665 CN2021120665W WO2022142527A1 WO 2022142527 A1 WO2022142527 A1 WO 2022142527A1 CN 2021120665 W CN2021120665 W CN 2021120665W WO 2022142527 A1 WO2022142527 A1 WO 2022142527A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- metal powder
- cooling chamber
- preparing
- pulsed
- powder
- Prior art date
Links
- 239000000843 powder Substances 0.000 title claims abstract description 110
- 239000002184 metal Substances 0.000 title claims abstract description 82
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 82
- 238000000034 method Methods 0.000 title claims abstract description 36
- 238000009833 condensation Methods 0.000 title claims abstract description 26
- 238000002360 preparation method Methods 0.000 title abstract description 15
- 238000001816 cooling Methods 0.000 claims abstract description 87
- 230000005494 condensation Effects 0.000 claims abstract description 24
- 239000002923 metal particle Substances 0.000 claims abstract description 15
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 14
- 238000009826 distribution Methods 0.000 claims abstract description 13
- 239000002994 raw material Substances 0.000 claims abstract description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 7
- 239000007789 gas Substances 0.000 claims description 34
- 239000002245 particle Substances 0.000 claims description 27
- 239000011229 interlayer Substances 0.000 claims description 10
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 7
- 239000000498 cooling water Substances 0.000 claims description 5
- 239000010410 layer Substances 0.000 claims description 4
- 230000000694 effects Effects 0.000 abstract description 9
- 238000011010 flushing procedure Methods 0.000 abstract 2
- 239000000178 monomer Substances 0.000 abstract 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 11
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 239000002893 slag Substances 0.000 description 6
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 4
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 4
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 4
- 229910052802 copper Inorganic materials 0.000 description 4
- 239000010949 copper Substances 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 229910052759 nickel Inorganic materials 0.000 description 4
- 229910052709 silver Inorganic materials 0.000 description 4
- 239000004332 silver Substances 0.000 description 4
- 229910052718 tin Inorganic materials 0.000 description 4
- 239000011135 tin Substances 0.000 description 4
- 230000001788 irregular Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 229910001092 metal group alloy Inorganic materials 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 230000006911 nucleation Effects 0.000 description 2
- 238000010899 nucleation Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 239000011882 ultra-fine particle Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/02—Making metallic powder or suspensions thereof using physical processes
- B22F9/12—Making metallic powder or suspensions thereof using physical processes starting from gaseous material
Definitions
- the present application relates to the technical field of powder preparation, in particular to a method for preparing and condensing pulsed metal powder.
- the physical gas phase method is mostly used to produce metal nickel powder. After the metal is melted and gasified in the molten pool of the reactor, the metal vapor enters the condenser under the action of nitrogen in the system, and is cooled by nitrogen in the condenser to form powder and then enter the collection tank.
- the metal vapor is directly condensed through the condenser tube, and the inner volume of the condenser tube is small, and the gas-solid ratio of the powder in the pulse cooling chamber is only 1: (200-250), resulting in the existence of The problems of high powder concentration, high temperature and insufficient powder cooling.
- the gas flow velocity in the tube is high, and the flow state Reynolds number Re ⁇ 3000, so the system flow state is excessive flow and turbulent flow.
- the metal nickel powder obtained by the existing method is too large, the probability of collision between the powder particles and between the particles and the tube wall will increase, and then in a high temperature environment, the uncooled metal particles are sintered with each other. , it is easy to form a conjoined body, or form irregular shaped particles, resulting in a decrease in the quality of the powder.
- the purpose of the present application is to provide a method for preparing and condensing pulsed metal powder, so as to achieve the purpose of improving the distribution uniformity and yield of metal powder. Its specific plan is as follows:
- a pulsed metal powder preparation and condensation method comprises the following steps:
- Step 1 put the raw material into the reactor to melt and evaporate, so that the metal vapor enters the condensation tube to crystallize and nucleate to form a powder blank;
- Step 2 The powder blanks enter the pulse cooling chamber for cooling to form single metal particles, and the pulse cooling chamber is filled with nitrogen during the pulse cooling;
- Step 3 The single metal particles are collected in the collector under the action of air flow
- Step 4 The backflushing device in the collector blows the metal powder back into the powder collector for collection.
- the pulse cooling chamber includes a dish-shaped head, a cylinder, an observation hole and a gas distributor; the gas distributor is an annular gas distributor.
- the annular gas distributor is provided with a plurality of gas nozzles distributed in equal arcs, and the open ends of the gas nozzles face the center of the condensation pipe.
- the cross-sectional area ratio of the condensation tube to the pulse cooling chamber is 1:(8-15); the volume ratio of the condensation tube to the pulse cooling chamber is 1:(10-15).
- the metal powder is spherical, and the particle size is less than 100 nm.
- the pulse cooling chamber is under negative pressure; the pressure in the reactor is 70-90 kPa.
- a zirconia lining layer is provided in the condensation tube.
- the gas-solid ratio of the metal powder in the pulse cooling chamber is 1:(1500-2000).
- the condensation tube and/or the pulse cooling chamber are provided with an interlayer, and the interlayer has cooling water therein.
- step 3 the single metal particles enter the collector from the pulse cooling chamber through the inclined pipe.
- the present application provides a method for preparing and condensing pulsed metal powder, and the method for preparing and condensing pulsed metal powder has the following beneficial effects:
- the metal vapor forms less slag on the chamber wall, less waste powder, and achieves the purpose of increasing the powder yield by 15%.
- FIG. 1 is a schematic structural diagram of an embodiment of a pulsed metal powder preparation condensing device of the present disclosure.
- a pulsed metal powder preparation condensation device includes a reactor 1 , a condensation tube 2 , a pulsed cooling chamber 3 , a collector 4 and a powder collector 5 .
- the reactor 1 is used for melting and evaporating raw materials to obtain metal vapor.
- the condenser tube 2 is connected to the reactor 1 and the pulse cooling chamber 3, so that the metal vapor crystallizes and nucleates when passing through the condenser tube 2.
- the powder blanks that crystallize and nucleate The spacing between particles instantly expands, greatly reducing the collision probability of each powder blank particle, thereby effectively reducing the generation of conjoined particles and slag.
- the collector 4 is used to collect the metal powder obtained by cooling through the pulse cooling chamber 3 , and the metal powder enters the powder collector 5 under the backflushing action of the backflushing tank in the collector 4 for collection.
- a zirconia lining layer is arranged in the condenser tube 2, and an interlayer is arranged in the condenser tube 2 and/or the pulse cooling chamber 3. There is cooling water in the interlayer.
- the pulse cooling chamber 3 includes a dish-shaped head, a cylinder, a viewing hole and a gas distributor 6 .
- the dish-shaped head is used for sealing connection with the condensing pipe 2 .
- Cylinders are used for cooling and obtaining metal powders.
- the observation hole is used to observe the formation of metal powder in the cylinder.
- the gas distributor 6 is an annular gas distributor, and a plurality of gas nozzles with equal arc distribution are arranged on the gas distributor 6 .
- the open end of the gas nozzle faces the center of the condenser tube 2 to effectively slow down the gas flow rate and blow out the powder blanks.
- the cross-sectional area ratio of the condenser tube 2 and the pulse cooling chamber 3 is 1:(8-15), and the volume ratio of the condenser tube 2 and the pulse cooling chamber 3 is 1:(10-15), so as to greatly reduce the The collision probability of each powder blank particle can effectively reduce the generation of conjoined particles and slag.
- the present disclosure provides a pulsed metal powder preparation and condensation method.
- a preparation condensation device consisting of a reactor 1, a condenser tube 2, a pulsed cooling chamber 3, a collector 4 and a powder collector 5, the pulsed cooling method is used to obtain metal powder.
- the method of pulse cooling includes the following steps:
- Step 1 The raw materials are put into the reactor 1 to melt and evaporate, so that the metal vapor enters the condenser tube 2 for crystallization and nucleation to form powder blanks.
- Step 2 The powder blank enters the pulse cooling chamber 3 for cooling to form single metal particles, and the pulse cooling chamber 3 is filled with nitrogen during pulse cooling.
- Step 3 the single metal particles enter the collector 4 through the inclined pipe under the action of the air flow of the pulsed metal powder preparation condensing device for collection.
- Step 4 The backflushing device in the collector 4 backflushes the metal powder into the powder collector 5 for collection.
- the raw material is one or more metals selected from iron, nickel, copper, tin, silver, etc.
- the obtained metal powder is one or more of iron, nickel, copper, tin, silver, etc. Metal alloy powder.
- the metal powder is spherical, and the particle size is less than 100nm.
- the pulse cooling chamber 3 is under negative pressure, the pressure in the reactor 1 is 70-90kPa, and the gas-solid ratio of the metal powder in the pulse cooling chamber 3 is 1:(1500-2000), with To achieve the effect of effectively improving the distribution uniformity and yield of metal powder.
- the pulsed metal powder preparation condensation device includes a reactor 1 , a condensation tube 2 , a pulsed cooling chamber 3 , a collector 4 and a powder collector 5 .
- the reactor 1 is used for melting and evaporating raw materials to obtain metal vapor.
- the condenser tube 2 is connected to the reactor 1 and the pulse cooling chamber 3, so that the metal vapor crystallizes and nucleates when passing through the condenser tube 2.
- the powder blanks that crystallize and nucleate The spacing between particles instantly expands, greatly reducing the collision probability of each powder blank particle, thereby effectively reducing the generation of conjoined particles and slag.
- the collector 4 is used to collect the metal powder obtained by cooling through the pulse cooling chamber 3 , and the metal powder enters the powder collector 5 under the backflushing action of the backflushing tank in the collector 4 for collection.
- a zirconia lining layer is arranged in the condenser tube 2, and an interlayer is arranged in the condenser tube 2. There is cooling water in the interlayer.
- the pulse cooling chamber 3 includes a dish-shaped head, a cylinder, a viewing hole and a gas distributor 6 .
- the dish-shaped head is used for sealing connection with the condensing pipe 2 .
- Cylinders are used for cooling and obtaining metal powders.
- the observation hole is used to observe the formation of metal powder in the cylinder.
- the gas distributor 6 is an annular gas distributor, and a plurality of gas nozzles with equal arc distribution are arranged on the gas distributor 6 .
- the open end of the gas nozzle faces the center of the condenser tube 2 to effectively slow down the gas flow rate and blow out the powder blanks.
- the cross-sectional area ratio of the condenser tube 2 and the pulse cooling chamber 3 is 1:8, and the volume ratio of the condenser tube 2 and the pulse cooling chamber 3 is 1:10, so as to greatly reduce the collision of each powder blank particle probability, thereby effectively reducing the generation of conjoined particles and slag.
- the pulsed metal powder preparation and condensation method provided in this example uses a preparation condensation device composed of a reactor 1, a condenser tube 2, a pulsed cooling chamber 3, a collector 4 and a powder collector 5 to obtain metal by a pulsed cooling method. powder.
- the method of pulse cooling includes the following steps:
- Step 1 The raw materials are put into the reactor 1 to melt and evaporate, so that the metal vapor enters the condenser tube 2 for crystallization and nucleation to form powder blanks.
- Step 2 The powder blank enters the pulse cooling chamber 3 for cooling to form single metal particles, and the pulse cooling chamber 3 is filled with nitrogen during pulse cooling.
- Step 3 the single metal particles enter the collector 4 through the inclined pipe under the action of the air flow of the pulsed metal powder preparation condensing device for collection.
- Step 4 The backflushing device in the collector 4 backflushes the metal powder into the powder collector 5 for collection.
- the raw material is one or more metals selected from iron, nickel, copper, tin, silver, etc.
- the obtained metal powder is one or more of iron, nickel, copper, tin, silver, etc. Metal alloy powder.
- the metal powder is spherical, and the particle size is less than 100nm.
- the pulse cooling chamber 3 is under negative pressure, the pressure in the reactor 1 is 70kPa, and the gas-solid ratio of the metal powder in the pulse cooling chamber 3 is 1:1500, so as to effectively improve the metal powder. The effect of distribution uniformity and yield.
- the difference between the second embodiment and the first embodiment is that the cross-sectional area ratio of the condenser tube 2 to the pulse cooling chamber 3 in the second embodiment is 1:12, and the volume ratio of the condenser tube 2 to the pulse cooling chamber 3 is 1:13.
- the difference between the third embodiment and the first embodiment is that the cross-sectional area ratio of the condenser tube 2 to the pulse cooling chamber 3 in the third embodiment is 1:15, and the volume ratio of the condenser tube 2 to the pulse cooling chamber 3 is 1:15.
- Example 4 The difference between Example 4 and Example 1 is that the pressure in the reactor 1 in Example 4 is 80 kPa, and the gas-solid ratio of the metal powder in the pulse cooling chamber 3 is 1:1800.
- Example 5 The difference between Example 5 and Example 1 is that the pressure in the reactor 1 in Example 5 is 90 kPa, and the gas-solid ratio of the metal powder in the pulse cooling chamber 3 is 1:2000.
- the difference between the sixth embodiment and the first embodiment is that the condensation pipe 2 and the pulse cooling chamber 3 in the sixth embodiment are both provided with an interlayer, and the interlayer has cooling water.
- the pulse cooling chamber 3 by setting the pulse cooling chamber 3 with a large cross-sectional area, the flow rate of the gas in the tube is reduced, the flow state Reynolds number Re ⁇ 3000, and the flow state of the condensation system is excessive flow and laminar flow.
- the pulse cooling chamber 3 By setting the pulse cooling chamber 3 with a large volume, the cooling space of the metal powder is effectively enlarged, the density of the metal powder in the pulse cooling chamber 3 is reduced, and the gap between the powder particles and between the particles and the tube wall is effectively reduced. Collision probability, to achieve the purpose of avoiding the conjoined metal particles and the generation of irregular shaped particles.
- the pulse cooling chamber 3 With uniform temperature field distribution, metal powder with uniform particle distribution can be obtained, and the effect of less super-large and ultra-fine particles and narrow particle size distribution of the powder can be achieved.
- the metal vapor forms less slag and less waste powder on the chamber wall, and achieves the purpose of improving the powder yield by 15%. Therefore, there is less slagging on the inner wall of the condenser pipe 2, the condenser pipe 2 is not easily blocked, and the production cycle is shortened by 20%.
- references in this application to "first”, “second”, “third”, “fourth”, etc. are used to distinguish similar objects and are not necessarily used to describe a specific order or sequence. It is to be understood that the data so used are interchangeable under appropriate circumstances so that the embodiments described herein can be practiced in sequences other than those illustrated or described herein. Furthermore, the terms “comprising” and “having”, and any variations thereof, are intended to cover non-exclusive inclusion, for example, a process, method or apparatus comprising a series of steps or elements is not necessarily limited to those steps or elements expressly listed , but may include other steps or elements not expressly listed or inherent to these processes, methods or apparatus.
Abstract
Procédé de condensation pulsé pour la préparation de poudre métallique. Ledit procédé comprend les étapes suivantes : étape 1, introduire, dans un réacteur (1), d'une matière première à faire fondre et évaporer, et amener la vapeur de métal à entrer dans un tube de condensation (2) pour qu'elle y soit cristallisée et nucléée, de manière à former une ébauche de poudre ; étape 2, introduire l'ébauche de poudre dans une chambre de refroidissement pulsé (3) pour être refroidie de manière à former des particules métalliques monomères, la chambre de refroidissement pulsé (3) étant remplie d'azote pendant le refroidissement pulsé ; étape 3, introduire des particules de métal monomères dans un collecteur (4) sous l'effet d'un flux d'air pour être collectées ; et étape 4, renvoyer, au moyen d'un dispositif de renvoi dans le collecteur (4), une poudre métallique dans un collecteur de poudre (5) pour être collectée. Le procédé de condensation a pour effet d'améliorer significativement l'uniformité de distribution et le rendement d'une poudre métallique.
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JP2023528288A JP2023550716A (ja) | 2020-12-29 | 2021-09-26 | パルス式金属粉末調製凝縮方法 |
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CN202011602571.4A CN112846206A (zh) | 2020-12-29 | 2020-12-29 | 一种脉冲式金属粉制备冷凝方法 |
CN202011602571.4 | 2020-12-29 |
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CN (1) | CN112846206A (fr) |
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Cited By (1)
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CN115770882A (zh) * | 2022-11-02 | 2023-03-10 | 杭州新川新材料有限公司 | 超细球形金属粉末的制造方法及装置 |
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CN112846206A (zh) * | 2020-12-29 | 2021-05-28 | 江苏博迁新材料股份有限公司 | 一种脉冲式金属粉制备冷凝方法 |
CN115383124A (zh) * | 2022-09-02 | 2022-11-25 | 杭州新川新材料有限公司 | 超细金属粉末的冷却设备 |
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2020
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CN112846206A (zh) | 2021-05-28 |
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