Claims
- 1. A batch process for dyeing fiber material comprising the steps of first applying to the fiber material a non-thickened aqueous dye liquor, consisting essentially of
- (a) a water-soluble or water-dispersible dyestuff having affinity for the fiber material
- (b) 0.2 to 10 g/l of a non-foaming anionic dispersing agent selected from the group consisting of benzene monosulfonic acid, naphthalene monosulfonic acid, C.sub.1 -C.sub.4 -alkyl benzene monosulfonic acid, C.sub.1 -C.sub.4 -alkyl naphthalene monosulfonic acid, tetrahydro naphthalene sulfonic acid, dinaphthylmethane disulfonic acid, diphenyl-naphthylmethane sulfonic acid, a 2:1 to 2:2 adduct thereof with formaldehyde, and water-soluble salts thereof, and
- (c) water,
- at a goods-to-liquor ratio of 1:1.5 to 1:2.5 and at a temperature below the absorption temperature of the dyestuff, subsequently in a closed container subjecting the fiber material and applied aqueous dye liquor to shaking or tumbling in a rotating drum sufficient to distribute evenly the aqueous dye liquor on the fiber material while still maintaining the temperature below the absorption temperature of the dyestuff, and finally heating the fiber material and the evenly distributed aqueous dye liquor to exhaust the dyestuff onto the fiber material.
- 2. The process of claim 1, wherein the dispersing agent is used at a concentration of 2 to 5 g/l.
- 3. The process of claim 1, wherein the dispersing agent is a formaldehyde adduct of benzene monosulfonic acid, naphthalene monosulfonic acid, C.sub.1 -C.sub.4 -alkyl benzene monosulfonic acid, C.sub.1 -C.sub.4 -alkyl naphthalene monosulfonic acid, .beta.-tetrahydro naphthalene sulfonic acid, dinaphthalene methane disulfonic acid, or diphenyl naphthalene methane sulfonic acid, having an arylformaldehyde ratio of 2:1.1 to 2:1.2, or a water-soluble salt thereof.
- 4. The process of claim 1, wherein the dispersing agent is the disodium salt of di-(6-sulfonaphthyl-2)-methane.
- 5. The process of claim 4, wherein the dispersing agent is used at a concentration of 2 to 5 g/l.
- 6. The process of claim 1, wherein the aqueous dye liquor and fiber material is heated in the final step at a temperature in the range of 95.degree. to 140.degree. C.
- 7. The process of claim 6, wherein the heating is effected by the introduction of saturated steam, super heated steam, or hot air.
- 8. The process of claim 1, wherein the fiber material and applied aqueous dye liquor are shaken or tumbled in a rotating drum to evenly distribute the aqueous dye liquor on the fiber material.
Priority Claims (1)
Number |
Date |
Country |
Kind |
16260/77 |
Nov 1971 |
CHX |
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Parent Case Info
This is a continuation of application Ser. No. 551,934, filed Feb. 24, 1975, now abandoned, which is a continuation of application Ser. No. 302,697, filed Nov. 1, 1972, now abandoned.
US Referenced Citations (7)
Foreign Referenced Citations (4)
Number |
Date |
Country |
772950 |
Jan 1972 |
BEX |
7110182 |
Feb 1972 |
NLX |
7112940 |
Mar 1972 |
NLX |
7743660 |
Jan 1956 |
GBX |
Non-Patent Literature Citations (6)
Entry |
Fischer-Bobien, Lexicon Fuer die GeSamte Textilveredlung 1950, p. 189. |
Viktorov, Verfabrentechnik der Fasterstaffe 1940, pp. 223-224. |
Arbuckle, J. Soc. Dyes & Col, Oct. 1968, No. 10, pp. 497-501. |
American Dyestuff Rep., 8/17/53, pp. 540-553. |
An Introduction to Textile Printing, pp. 4-7, Pub. 1964 by Butterworths, London, Eng. |
Kein, America Dyestuff Rep., 5/15/61, pp. 368-373. |
Continuations (2)
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Number |
Date |
Country |
Parent |
551934 |
Feb 1975 |
|
Parent |
302697 |
Nov 1972 |
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