US2018195153A1PendingUtilityA1
Method of producing alloy nanoparticles
Est. expiryJan 12, 2037(~10.5 yrs left)· nominal 20-yr term from priority
B22F 1/054C22C 12/00B22F 2302/45B22F 1/0018B22F 9/24B22F 2304/054B82Y 30/00B82Y 40/00
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Claims
Abstract
A method of producing a homogenous skutterudite compound, CoSb 3 , having a crystallite diameter of 100 nm or less, by a convenient synthesis process, which is a method of producing CoSb 3 , comprising reducing Co 2+ and Sb 3+ to Co 0 and Sb 0 , respectively, in a solution including a Co-containing compound and an Sb-containing compound using a reducing agent, wherein supplied amount of the Co-containing compound and the Sb-containing compound are adjusted in order to set a ratio of a reduction rate of Co 2+ to Co 0 to a reduction rate of Sb 3+ to Sb 0 to 1:2.9 to 1:3.1.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A method of producing CoSb 3 , comprising reducing Co 2+ and Sb 3+ to Co 0 and Sb 0 , respectively, in a solution including a Co-containing compound and an Sb-containing compound using a reducing agent, wherein supplied amounts of the Co-containing compound and the Sb-containing compound are adjusted in order to set a ratio of a reduction rate of Co 2+ to Co 0 to a reduction rate of Sb 3+ to Sb 0 to 1:2.9 to 1:3.1.
2 . The method according to claim 1 , wherein the supplied amounts of the Co-containing compound and the Sb-containing compound are adjusted in order to set the ratio of the reduction rate of Co 2+ to Co 0 to the reduction rate of Sb 3+ to Sb 0 to 1:3.
3 . The method according to claim 1 , wherein at least one weak reducing agent selected from the group consisting of oxalic acid, ascorbic acid, and citric acid is used as the reducing agent for reducing Co 2+ and Sb 3+ to Co 0 and Sb 0 , respectively.
4 . The method according to claim 2 , wherein at least one weak reducing agent selected from the group consisting of oxalic acid, ascorbic acid, and citric acid is used as the reducing agent for reducing Co 2+ and Sb 3+ to Co 0 and Sb 0 , respectively.
5 . The method according to claim 1 , which is carried out at a reaction temperature of 250° C. to 320° C. within a reaction time of 1 hour to 10 hours.
6 . The method according to claim 2 , which is carried out at a reaction temperature of 250° C. to 320° C. within a reaction time of 1 hour to 10 hours.
7 . The method according to claim 3 , which is carried out at a reaction temperature of 250° C. to 320° C. within a reaction time of 1 hour to 10 hours.
8 . The method according to claim 4 , which is carried out at a reaction temperature of 250° C. to 320° C. within a reaction time of 1 hour to 10 hours.
9 . The method according to claim 1 , wherein a total concentration of [Co 2+ ] and [Sb 3+ ] is 0.140 mol/l to 0.770 mol/l.
10 . The method according to claim 2 , wherein a total concentration of [Co 2+ ] and [Sb 3+ ] is 0.140 mol/l to 0.770 mol/l.
11 . The method according to claim 3 , wherein a total concentration of [Co 2+ ] and [Sb 3+ ] is 0.140 mol/l to 0.770 mol/l.
12 . The method according to claim 4 , wherein a total concentration of [Co 2+ ] and [Sb 3+ ] is 0.140 mol/l to 0.770 mol/l.
13 . The method according to claim 5 , wherein a total concentration of [Co 2+ ] and [Sb 3+ ] is 0.140 mol/l to 0.770 mol/l.
14 . The method according to claim 6 , wherein a total concentration of [Co 2+ ] and [Sb 3+ ] is 0.140 mol/l to 0.770 mol/l.
15 . The method according to claim 7 , wherein a total concentration of [Co 2+ ] and [Sb 3+ ] is 0.140 mol/l to 0.770 mol/l.
16 . The method according to claim 8 , wherein a total concentration of [Co 2+ ] and [Sb 3+ ] is 0.140 mol/l to 0.770 mol/l.
17 . The method according to claim 9 , wherein the total concentration of [Co 2+ ] and [Sb 3+ ] is 0.350 mol/l to 0.770 mol/l.
18 . The method according to claim 11 , wherein the total concentration of [Co 2+ ] and [Sb 3+ ] is 0.350 mol/l to 0.770 mol/l.
19 . The method according to claim 13 , wherein the total concentration of [Co 2+ ] and [Sb 3+ ] is 0.350 mol/l to 0.770 mol/l.
20 . The method according to claim 15 , wherein the total concentration of [Co 2+ ] and [Sb 3+ ] is 0.350 mol/l to 0.770 mol/l.Join the waitlist — get patent alerts
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