US2009205143A1PendingUtilityA1
Process of bleaching
Est. expiryMay 27, 2025(expired)· nominal 20-yr term from priority
C11D 3/3932B01J 2531/72B01J 31/22D21C 9/163B01J 31/182D06L 4/12D21C 9/1036B01J 2231/70
55
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Claims
Abstract
The present invention concerns bleaching of substrates with an aqueous solution of a water soluble salt of a preformed transition metal catalyst together with hydrogen peroxide.
Claims
exact text as granted — not AI-modified1 . A method of catalytically treating a substrate, the substrate being a cellulose-containing substrate or starch containing substrate, with a preformed transition metal catalyst salt, the preformed transition metal catalyst salt having a non-coordinating counter ion, the method comprising the following steps:
(i) optionally dissolving a concentrate or solid form of a preformed transition metal catalyst salt in an aqueous medium to yield an aqueous solution of the preformed transition metal catalyst salt; (ii) adding the aqueous solution of the preformed transition metal catalyst salt to a reaction vessel; and, (iii) adding hydrogen peroxide to the reaction vessel,
wherein the preformed transition metal catalyst salt is a mononuclear or dinuclear complex of a Mn(III) or Mn(IV) transition metal catalyst for catalytically treating the substrate with hydrogen peroxide, the non-coordinating counter ion of said transition metal selected to provide a preformed transition metal catalyst salt that has a water solubility of at least 30 g/l at 20° C. and wherein the ligand of the transition metal catalyst is of formula (I):
wherein:
p is 3;
R is independently selected from: hydrogen, C1-C6-alkyl, CH2CH2OH, and CH2COOH, or one of R is linked to the N of another Q via an ethylene bridge;
R1, R2, R3, and R4 are independently selected from: H, C1-C4-alkyl, and C1-C4-alkylhydroxy, and the substrate is brought into contact with a mixture of the aqueous solution of the preformed transition metal catalyst salt and the hydrogen peroxide.
2 . A method according to claim 1 , wherein R is independently selected from: CH 3 , C 2 H 5 , CH 2 CH 2 OH and CH 2 COOH.
3 . A method according to claim 1 , wherein R1, R2, R3, and R4 are independently selected from: H and Me.
4 . A method according to claim 1 , wherein the catalyst is derived from a ligand selected from the group consisting 1,4,7-Trimethyl-1,4,7-triazacyclononane (Me 3 -TACN) and 1,2,-bis-(4,7,-dimethyl-1,4,7,-triazacyclonon-1-yl)-ethane (Me 4 -DTNE).
5 . A method according to claim 1 , wherein the preformed transition metal catalyst salt is a dinuclear Mn(III) or Mn(IV) complex with at least one O 2− bridge.
6 . A method according to claim 1 , wherein the preformed transition metal catalyst salt has a water solubility of at least 50 g/l at 20° C.
7 . A method according to claim 6 , wherein the salt is that selected from the group consisting of chloride, acetate, sulphate, and nitrate.
8 . A method according to claim 7 , wherein the salt is acetate.
9 . A method according to claim 1 , wherein the aqueous solution of the preformed transition metal catalyst salt is in a buffer system that maintains the solution in the pH range 2 to 7.
10 . A method according to claim 1 , wherein the preformed transition metal catalyst salt is present at a concentration in the range from 0.1 to 10 wt % in the aqueous solution in step (ii).
11 . A method according to claim 9 , wherein the concentration is in the range from 0.5 to 8 wt %.
12 . A method according to claim 1 , wherein during treatment of the substrate the aqueous solution comprises at least 80 wt % water.
13 . A method according to claim 12 , the aqueous solution comprises at least 90 wt % water.
14 . A method according to claim 13 , wherein the aqueous solution comprises at least 95 wt % water.
15 . A method according to claim 1 , wherein the pH of the aqueous solution of the preformed transition metal catalyst salt aqueous solution in step (ii) in the range from 2 to 7.
16 . A method according to claim 15 , wherein the pH is in the range from 4 to 6.
17 . A method according to claim 16 , wherein the pH is in the range from 4.5 to 5.5.
18 . A method according to claim 1 , wherein the substrate is selected from the group consisting of woven or knitted cotton cloths, industrial laundering and wood pulp.
19 . A method according to claim 1 , wherein the substrate is wood pulp.
20 . A method according to claim 1 , wherein the preformed transition metal catalyst salt has been formed by a contact and oxidation step that is carried out at least 24 hours before use.
21 . Use of a preformed transition metal catalyst salt in an aqueous medium to bleach a substrate, the substrate being a cellulose-containing substrate or starch containing substrate, with hydrogen peroxide, wherein the preformed transition metal catalyst salt is a dinuclear Mn(III) or Mn(IV) complex with at least two O 2− bridges for catalytically treating the substrate with hydrogen peroxide, said transition metal catalyst a salt, wherein the preformed transition metal catalyst salt has a water solubility of at least 30 g/l at 20° C. and wherein the ligand of the transition metal catalyst is of formula (I):
wherein:
p is 3;
R is independently selected from: hydrogen, C1-C6-alkyl, CH 2 CH 2 OH, and CH 2 COOH, or one of R is linked to the N of another Q via an ethylene bridge;
R1, R2, R3, and R4 are independently selected from: H, C1-C4-alkyl, and C1-C4-alkylhydroxy.
22 . Use according to claim 21 , wherein R is independently selected from: CH 3 , C 2 H 5 , CH 2 CH 2 OH and CH 2 COOH.
23 . Use according to claim 21 , wherein R1, R2, R3, and R4 are independently selected from: H and Me.
24 . Use according to claim 23 , wherein the catalyst is derived from a ligand selected from the group consisting 1,4,7-Trimethyl-1,4,7-triazacyclononane (Me3-TACN) and 1,2,-bis-(4,7,-dimethyl-1,4,7,-triazacyclonon-1-yl)-ethane (Me4-DTNE).
25 . A cellulose-containing substrate or a starch containing substrate, wherein the cellulose-containing substrate or the starch containing substrate has been treated by the method defined in claim 1 .Cited by (0)
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