US2010124717A1PendingUtilityA1
Colored resin particles, manufacturing method of the colored resin particles and toner for electrostatically charged image development
Est. expiryNov 18, 2028(~2.4 yrs left)· nominal 20-yr term from priority
G03G 9/0827G03G 9/0819G03G 9/0825C08J 3/21G03G 9/0804C08J 3/16
51
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Claims
Abstract
Colored resin particles, each includes: a resin; and a colorant, wherein a value of average equivalent circle diameter A (μm) of the colored resin particles is 3≦A≦6, an average degree of circularity B of the colored resin particles satisfies the following expression (1), and 0.990−0.0083 A≦B ≦1.021−0.0117 A (1) a cumulative number frequency of particles which have degrees of circularity of less than 0.9 in the colored resin particles is 1% or less.
Claims
exact text as granted — not AI-modified1 . Colored resin particles, each comprising:
a resin; and a colorant, wherein a value of average equivalent circle diameter A (μm) of the colored resin particles is 3≦A≦6, an average degree of circularity B of the colored resin particles satisfies the following expression (1), and
0.990−0.0083 A≦B≦ 1.021−0.0117 A (1)
a cumulative number frequency of particles which have degrees of circularity of less than 0.9 in the colored resin particles is 1% or less.
2 . The colored resin particles according to claim 1 ,
wherein a variation coefficient of degree of circularity (a standard deviation of degree of circularity/the average degree of circularity B) of the colored resin particles is 0.016 or less.
3 . A manufacturing method of the colored resin particles according to claim 1 , the method comprising:
preparing a reactor that includes a first channel, a second channel, a first confluent channel where the first channel and the second channel converge and a temperature control unit that controls a temperature of the first confluent channel; feeding a coagulated particle dispersion containing coagulated particles that contain resin particles and a colorant to the first channel; stopping growth of coagulation of the coagulated particles by feeding a liquid containing a coagulation stopper from the second channel; and coalescing the coagulated particles by heating the first confluent channel.
4 . The manufacturing method according to claim 3 ,
wherein a laminar flow is formed at the first confluent channel at least in the stopping of the growth of coagulation.
5 . The manufacturing method according to claim 3 ,
wherein the coagulated particle dispersion is fed so as not to be in contact with an inner wall of the first confluent channel.
6 . The manufacturing method according to claim 3 ,
wherein a sheath flow is formed between an inner wall of the first confluent channel and a mixed solution of the coagulated particle dispersion and the liquid containing the coagulation stopper.
7 . The manufacturing method according to claim 3 ,
wherein an inner wall of the first channel and an inner wall of the first confluent channel are not continuously formed.
8 . The manufacturing method according to claim 3 ,
wherein a peripheral channel diameter of the first confluent channel is larger than a channel diameter of the first channel.
9 . The manufacturing method according to claim 3 ,
wherein a ratio of a quantity of flow of a liquid fed to the first channel and a quantity of flow of a liquid fed to the second channel is 1/0.3 to 1/100.
10 . The manufacturing method according to claim 3 ,
wherein the temperature control unit is a microwave applicator.
11 . The manufacturing method according to claim 3 ,
wherein the reactor further includes a control unit of quantity of flow that varies a quantity of flow to be fed.
12 . The manufacturing method according to claim 11 ,
wherein the control unit of quantity of flow is provided on a feeding port side of a liquid.
13 . The manufacturing method according to claim 3 ,
wherein a main component of liquid components in the coagulated particle dispersion and a main component of liquid components in the liquid containing the coagulation stopper are the same liquid.
14 . The manufacturing method according to claim 3 , further comprising:
cooling the coalesced coagulated particles.
15 . The manufacturing method according to claim 3 ,
wherein the reactor further includes a third channel and a second confluent channel where the first confluent channel and the third channel converge, and the manufacturing method further comprises: feeding a liquid containing a shape controlling agent from the third channel; and heating the second confluent channel.
16 . The manufacturing method according to claim 15 ,
wherein the coagulated particle dispersion fed from the first channel and a liquid fed from at least one of the second channel and the third channel form a concentric circle flow with the coagulated particle dispersion as a center of the concentric circle flow.
17 . The manufacturing method according to claim 15 ,
wherein a ratio of a quantity of flow of a liquid fed to the first channel and a quantity of flow of a liquid fed to the third channel is 1/0.3 to 1/100.
18 . A toner for electrostatically charged image development, comprising:
the colored resin particles according to claim 1 .Cited by (0)
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