Method for manufacturing micropore filter
10137501 · 2018-11-27
Assignee
Inventors
- Hidetoshi Nakajima (Fukushima, JP)
- Toshio Miura (Fukushima, JP)
- Miyabi Katano (Fukushima, JP)
- Nozomi Igarashi (Fukushima, JP)
Cpc classification
B01D39/2075
PERFORMING OPERATIONS; TRANSPORTING
B22F9/04
PERFORMING OPERATIONS; TRANSPORTING
B22F3/16
PERFORMING OPERATIONS; TRANSPORTING
B22F2302/45
PERFORMING OPERATIONS; TRANSPORTING
B01D39/20
PERFORMING OPERATIONS; TRANSPORTING
B22F3/11
PERFORMING OPERATIONS; TRANSPORTING
B22F3/1109
PERFORMING OPERATIONS; TRANSPORTING
B22F2998/10
PERFORMING OPERATIONS; TRANSPORTING
B22F2998/10
PERFORMING OPERATIONS; TRANSPORTING
B01D2325/02834
PERFORMING OPERATIONS; TRANSPORTING
International classification
B22F3/11
PERFORMING OPERATIONS; TRANSPORTING
B01D39/20
PERFORMING OPERATIONS; TRANSPORTING
B22F3/16
PERFORMING OPERATIONS; TRANSPORTING
B22F9/04
PERFORMING OPERATIONS; TRANSPORTING
B01D67/00
PERFORMING OPERATIONS; TRANSPORTING
B01D61/14
PERFORMING OPERATIONS; TRANSPORTING
Abstract
Provided is a method for manufacturing a micropore filter usable as SCE. Stainless steel particles having particle diameters of 3 to 60 ?m are subjected to milling in a bead mill using zirconia beads to prepare powder having a flakiness of 0.03 to 0.4. The zirconia adhered to the surface of the powder is removed by pickling. A load of 10 to 15 kN is applied to 0.5 to 1.0 g of the pickled powder, thereby compacting the powder into a columnar compact body. The compact body is kept and fired in a vacuum atmosphere of 10.sup.?5 to 10.sup.?3 Pa at a temperature of 1000 to 1300? C. for 1 to 3 hours to form a sintered body. The sintered body is pressed into a pipe having an inner diameter of 0.90 to 0.99 times of the outer diameter of the sintered body, and extruded to obtain a micropore filter.
Claims
1. A method for manufacturing a micropore filter comprising: a step of treating stainless steel particles having particle diameters in a range of 3 to 60 ?m in a bead mill using zirconia beads to prepare powder having a flakiness expressed by a ratio of a thickness with respect to a long diameter (thickness/long diameter) in a range of 0.03 to 0.4; a step of pickling the powder to remove zirconia adhered to a surface of the powder due to treatment in the bead mill; a step of applying a load of 10 to 15 kN to 0.5 to 1.0 g of the powder after the pickling, thus compacting the powder to obtain a compact body having a columnar shape; a step of keeping the compact body in a vacuum atmosphere in a range of 10.sup.?5 to 10.sup.?3 Pa at a temperature in a range of 1000 to 1300? C. for 1 to 3 hours, thus firing the compact body to obtain a sintered body; and a step of pressing the sintered body into a pipe having an inner diameter in a range of 0.90 to 0.99 times of an outer diameter of the sintered body, and extruding the sintered body.
Description
BRIEF DESCRIPTION OF DRAWINGS
(1)
(2)
(3)
(4)
DESCRIPTION OF EMBODIMENT
(5) Next, an embodiment of the present invention is explained in more details with reference to the accompanying drawings.
(6) As shown in
(7) The above treatment can be performed by feeding a slurry in which 1 kg of stainless steel particles being dispersed in 5 liters of water, at a flow rate of 0.5 kg/min to the bead mill filled with zirconia beads having a diameter of 2 mm at a ratio of approximately 80 vol. %, and then rotating the bead mill at a peripheral speed of 10 m/sec. for 30 to 120 minutes. As a result, powders composed of the stainless steel and having flakiness in a range of 0.03 to 0.4 can be obtained.
(8) As shown in
(9) Zirconia derived from the zirconia beads is adhered to the surface of the powder obtained by the treatment with the bead mill, and if used in this state, a desired performance cannot be obtained when processed as the micropore filter.
(10) In this regard, in the method for manufacturing the micropore filter of the present embodiment, next, as shown in
(11) Next, a load of 10 to 15 kN is applied to 0.5 to 1.0 g of the powder after being pickled, thus compacting the powder to obtain a compact body having a columnar shape, for example, having a diameter in a range of 5.0 to 5.2 mm and a length in a range of 4.8 to 5.0 mm. The compacting can be performed by using, for example, a servo press device.
(12) Next, the compact body is kept in a vacuum atmosphere in a range of 10.sup.?5 to 10.sup.?3 Pa at a temperature in a range of 1000 to 1300? C. for 1 to 3 hours, thus firing the compact body to obtain a sintered body. The sintering can be performed by using, for example, a vacuum atmosphere furnace.
(13) Next, the sintered body is pressed into a pipe having an inner diameter in a range of 0.90 to 0.99 times of an outer diameter of the sintered body, and then extruded, thereby obtaining a micropore filter. The press in can be performed by using, for example, a servo press device.
(14) The conductance (m.sup.3/sec) of the micropore filter obtained by the manufacturing method of the present embodiment can be measured by using, for example, a measuring device 11 illustrated in
(15) Moreover, an oil rotary pump 19 and a diaphragm vacuum gauge 20 as the primary side vacuum gauge are connected to the conduit 14 between the micropore filter 12 and the switching valve 13. Furthermore, a turbo-molecular pump 21 and an ionization vacuum gauge 22 as the secondary side vacuum gauge are connected to the vacuum container 18. Here, both of the oil rotary pump 19 and the turbo-molecular pump 21 are vacuum pumps.
(16) Next, the method for measuring the conductance of the micropore filter 12 by the measuring device 11 is explained.
(17) When measuring the conductance of the micropore filter 12 by the measuring device 11, first, in a state in which the switching valve 13 is closed and the switching valve 16 is opened, the oil rotary pump 19 and the turbo-molecular pump 21 are activated to sufficiently decompress the primary side and the secondary side of the micropore filter 12. At this time, the atmospheric pressure at the primary side of the micropore filter 12 measured by the diaphragm vacuum gauge 20 is indicated as P1, and the atmospheric pressure at the secondary side of the micropore filter 12 measured by the ionization vacuum gauge 22 is indicated as P2.
(18) Next, while the turbo-molecular pump 21 is kept activated, the oil rotary pump 19 is stopped, and the switching valve 13 is opened to supply nitrogen gas from the nitrogen gas cylinder 15, and the atmospheric pressure at the primary side of the micropore filter 12 is gradually recovered. At this time, the atmospheric pressure at the secondary side of the micropore filter 12 measured by the ionization vacuum gauge 22 is indicated as P02 with respect to the atmospheric pressure P01 at the primary side of the micropore filter 12 measured by the diaphragm vacuum gauge 20.
(19) Then, the exhaust rate of the turbo-molecular pump 21 being indicated as A (m.sup.3/sec), the conductance of the micropore filter 12 is measured according to the following equation.
Conductance (m.sup.3/sec)={(P02?P2)/(P01?P1)?1000}?A
(20) The conductance was measured by using the measuring device 11 for 9 types of micropore filters obtained according to the manufacturing method of the present embodiment. The results are shown in
(21) From
EXPLANATION OF REFERENCE NUMERALS
(22) 11 . . . measuring device, 12 . . . micropore filter, 15 . . . nitrogen gas cylinder, 18 . . . vacuum container, 19 . . . oil rotary pump, 20 . . . diaphragm vacuum gauge, 21 . . . turbo-molecular pump, 22 . . . ionization vacuum gauge