US3871821A - Package dye process - Google Patents
Package dye process Download PDFInfo
- Publication number
- US3871821A US3871821A US428299A US42829973A US3871821A US 3871821 A US3871821 A US 3871821A US 428299 A US428299 A US 428299A US 42829973 A US42829973 A US 42829973A US 3871821 A US3871821 A US 3871821A
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- United States
- Prior art keywords
- kier
- vapors
- solvent
- dyebath
- dye
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06B—TREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
- D06B9/00—Solvent-treatment of textile materials
- D06B9/02—Solvent-treatment of textile materials solvent-dyeing
Definitions
- ABSTRACT A method for kier-dyeing packaged yarn in a discon- [451 Mar. 18, 1975 tinuous manner employing 'a chlorinated solvent as the sole fluid to evacuate the air from the kier and to heat the yarn to achieve dye fixation temperature as the principal vehicle for the dye formulation, and as the means for recovering residual solvent from the dyed yarn packages and kier.
- the method is practiced by subjecting a kier, which has been'loaded with packages of yarn to be dyed, toan initial vacuum followed by introduction of vapors of a chlorinated solvent into the bottom of the kier until the kier is filled with such vapors and substantially all air has been evacuated, discontinuing the exhaustion under vacuum but continuing the introduction of vapors to the kier until the contents achieve the temperature of the vapors, introducing a solvent dyebath into the kier and'circulating the dyebath through the kier until the dyebath is spent, removing the spent dyebath from the kier under the pressure of solvent vapors, and circulating the vapors to a heater to superheat the vapors, returning the vapors to the kier, condensing vapors in excess of those necessary to fill the kier and superheater, continuing the circulation of vapors until the solvent is substantially completely removed from the yarn in the kier. Residual solvent is removed by evacuating and pur
- the kier 1 is opened and loaded with yarn packages IE on the spindles 1A normally found in yarn package kiers.
- the kier is closed and sealed, valve V-3 opened and pressure-vacuum compressor 2 is started to begin the evacuation of air from the kier l.
- Solvent vapors are generated by drawing liquid solvent from storage tank 4 through valve V-4 with pump 5 into reboiler 6. Hot liquid and vapors exit from reboiler 6 through valve V-l into flash liquid separator 9, whence any liquid solvent is recirculated through valve V-6 to reboiler 6, while the solvent vapors exit through valve V-l2 and into kier 1.
- the kier 1 When the kier 1 has been totally evacuated of air and is full of vapors, the kier is filled with a solvent dye bath from expansion tank 7 (previously made up from solvent in storage tank 4 mixed with dye or dye-concentrate in tank 7) by introducing the solvent dye bath into the system employing valve V-7, reboiler 6 and valve V-2, which system provides for heating and circulating the solvent dye bath through the kier with the aid of pump 5.
- Item 13 is a reversing valve for the purpose of reversing the direction of flow of dye solution through the kier. One flow direction is indicated by the solid lines, the other by dotted lines.
- the reboiler 6 is used to further raise the temperature of the solvent dye bath to create vapors under pressure in the system, thus forcing the spent solvent bath from the kier and, by means of valves V-7 and V-5, into waste storage tank 12.
- the next step is drying of the dyed yarn packages in the kier. This is accomplished by operating the superheater 8 to supply superheated vapors to the kier l to heat the yarn packages 1B and vaporize liquid solvent retained thereby. Simultaneously, the blower 3 is operated to circulate the superheated vapors, and the condenser 10 and accumulator 11 are operated to remove vapors in excess of those necessary to fill the system.
- the kier When there is substantially no more liquid in the system the kier is subjected to evacuation by operating vacuum compressor 2 until the amount of the vapor has been reduced to that obtainable under the vacuum. Then an inert purge gas is introduced into the kier through valves V-9 and V-ll to sweep remaining vapors from the kier. The solvent vapors thus purgedfrom the kier are condensed by condenser 10, sent to accumulator 11 and from thence to storage tank 4.
- the inert purge gas is introduced into the kier through valves V-9 and V-ll to sweep remaining vapors from the kier.
- the solvent vapors thus purgedfrom the kier are condensed by condenser 10, sent to accumulator 11 and from thence to storage tank 4.
- spent solvent is reclaimed from storage 12 by using reboiler 6 to supply heat for flashing the solvent through valve V-l into the vapor-liquid separator 9 under forced circulation by pump 5, the vapors being carried through valve V-13, condensed in condenser 10, collected in accumulator 11 and finally sent to storage tank 4.
- the improvement in a method of dyeing yarn packages in a kier comprises l sealing and evacuating a dye kier, (2) introducing into the kier vapors of an organic solvent, which solvent is to be employed as thedye carrier, until the temperature of the kier and its contents are raised to the solvent boiling point, all residual air is expelled and the kier is filled with said vapors, (3) filling the kier with a solvent dyebath which is heated and circulated therethrough until the desired dye fixation temperature is reached and until said dye bath is substantially exhausted, (4) removing the exhausted dyebath and circulating solvent vapors to a superheater to provide superheated vapors to the kier in order to vaporize residual solvent in the yarn packages, (5) evacuating the kier and purging residual solvent vapors therein by means of an inert gas, (6) removing the dry dyed yarn packages and (7) recovering the solvent from the spent (exhausted) dye bath by distillation.
- an organic solvent which
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Abstract
A method for kier-dyeing packaged yarn in a discontinuous manner employing a chlorinated solvent as the sole fluid to evacuate the air from the kier and to heat the yarn to achieve dye fixation temperature as the principal vehicle for the dye formulation, and as the means for recovering residual solvent from the dyed yarn packages and kier. The method is practiced by subjecting a kier, which has been loaded with packages of yarn to be dyed, to an initial vacuum followed by introduction of vapors of a chlorinated solvent into the bottom of the kier until the kier is filled with such vapors and substantially all air has been evacuated, discontinuing the exhaustion under vacuum but continuing the introduction of vapors to the kier until the contents achieve the temperature of the vapors, introducing a solvent dyebath into the kier and circulating the dyebath through the kier until the dyebath is spent, removing the spent dyebath from the kier under the pressure of solvent vapors, and circulating the vapors to a heater to superheat the vapors, returning the vapors to the kier, condensing vapors in excess of those necessary to fill the kier and superheater, continuing the circulation of vapors until the solvent is substantially completely removed from the yarn in the kier. Residual solvent is removed by evacuating and purging the kier with an inert gas. Thereafter, the kier is cooled to enable removal of the yarn packages. Finally, solvent is recovered from the spent dyebath and returned to storage.
Description
United States Patent [191 Winn et al.
[ PACKAGE DYE PROCESS [73] Assignee: The Dow Chemical Company,
Midland, Mich.
[22] Filed: Dec. 26, 1973 [21] Appl. No.: 428,299
Related US. Application Data [63] Continuation-impart of Ser. No. 296,881, Oct. 12,
1972, abandoned.
52 us. Cl. 8/l49.1, 8/15511' 9/1972 Furness 68/l89 X Primary Examiner-Harvey C. l-lornsby Assistant Examiner-Philip R. Coe
Attorney, Agent, or FirmA. Cooper Ancona; Glwynn R. Baker [57] ABSTRACT A method for kier-dyeing packaged yarn in a discon- [451 Mar. 18, 1975 tinuous manner employing 'a chlorinated solvent as the sole fluid to evacuate the air from the kier and to heat the yarn to achieve dye fixation temperature as the principal vehicle for the dye formulation, and as the means for recovering residual solvent from the dyed yarn packages and kier. The method is practiced by subjecting a kier, which has been'loaded with packages of yarn to be dyed, toan initial vacuum followed by introduction of vapors of a chlorinated solvent into the bottom of the kier until the kier is filled with such vapors and substantially all air has been evacuated, discontinuing the exhaustion under vacuum but continuing the introduction of vapors to the kier until the contents achieve the temperature of the vapors, introducing a solvent dyebath into the kier and'circulating the dyebath through the kier until the dyebath is spent, removing the spent dyebath from the kier under the pressure of solvent vapors, and circulating the vapors to a heater to superheat the vapors, returning the vapors to the kier, condensing vapors in excess of those necessary to fill the kier and superheater, continuing the circulation of vapors until the solvent is substantially completely removed from the yarn in the kier. Residual solvent is removed by evacuating and purging the kier with an inertgas. Thereafter, thekier is cooled to enable removal of'the yarn packages. Fi-
nally, solvent is recovered from the spent dyebath and returned to storage, 7
PACKAGE DYE PROCESS CROSS-REFERENCE TO RELATED APPLICATION This application is a continuation-in-part of our copending application U.S. Ser. No. 296,881 filed Oct. 12, 1972, now abandoned.
BRIEF DESCRIPTION OF THE INVENTION The process of the present invention is readily understood from the following description with reference to the drawing.
The kier 1 is opened and loaded with yarn packages IE on the spindles 1A normally found in yarn package kiers. The kier is closed and sealed, valve V-3 opened and pressure-vacuum compressor 2 is started to begin the evacuation of air from the kier l. Solvent vapors are generated by drawing liquid solvent from storage tank 4 through valve V-4 with pump 5 into reboiler 6. Hot liquid and vapors exit from reboiler 6 through valve V-l into flash liquid separator 9, whence any liquid solvent is recirculated through valve V-6 to reboiler 6, while the solvent vapors exit through valve V-l2 and into kier 1. These vapors, continuously supplied to kier l, condense on the yarn packages 1B and give up heat. The vapors continue to condense until the kier and yarn packages 1B achieve the liquid boiling point of the solvent. When this occurs, the vapors, being heavier than air, commence to accumulate in the bottom of kier l and as they build up, push any remaining air to the vacuum compressor 2. Any solvent vapors drawn through vacuum compressor 2 are condensed by condenser 10, collected in accumulator tank 11 and returned to storage tank 4. When the kier 1 has been totally evacuated of air and is full of vapors, the kier is filled with a solvent dye bath from expansion tank 7 (previously made up from solvent in storage tank 4 mixed with dye or dye-concentrate in tank 7) by introducing the solvent dye bath into the system employing valve V-7, reboiler 6 and valve V-2, which system provides for heating and circulating the solvent dye bath through the kier with the aid of pump 5. Item 13 is a reversing valve for the purpose of reversing the direction of flow of dye solution through the kier. One flow direction is indicated by the solid lines, the other by dotted lines.
After sufficient time has elapsed for the yarn packages to be properly dyed and/or the dye has been substantially exhausted from the circulating solvent, the reboiler 6 is used to further raise the temperature of the solvent dye bath to create vapors under pressure in the system, thus forcing the spent solvent bath from the kier and, by means of valves V-7 and V-5, into waste storage tank 12.
The next step is drying of the dyed yarn packages in the kier. This is accomplished by operating the superheater 8 to supply superheated vapors to the kier l to heat the yarn packages 1B and vaporize liquid solvent retained thereby. Simultaneously, the blower 3 is operated to circulate the superheated vapors, and the condenser 10 and accumulator 11 are operated to remove vapors in excess of those necessary to fill the system.
When there is substantially no more liquid in the system the kier is subjected to evacuation by operating vacuum compressor 2 until the amount of the vapor has been reduced to that obtainable under the vacuum. Then an inert purge gas is introduced into the kier through valves V-9 and V-ll to sweep remaining vapors from the kier. The solvent vapors thus purgedfrom the kier are condensed by condenser 10, sent to accumulator 11 and from thence to storage tank 4. The
system is thus freed of residual solvent by the inert gas, after which the kier is opened and the dry dyed yarn packages are removed.
Following the entire operation, or, if preferred, during the drying cycle, spent solvent is reclaimed from storage 12 by using reboiler 6 to supply heat for flashing the solvent through valve V-l into the vapor-liquid separator 9 under forced circulation by pump 5, the vapors being carried through valve V-13, condensed in condenser 10, collected in accumulator 11 and finally sent to storage tank 4.
Thus, the improvement in a method of dyeing yarn packages in a kier comprises l sealing and evacuating a dye kier, (2) introducing into the kier vapors of an organic solvent, which solvent is to be employed as thedye carrier, until the temperature of the kier and its contents are raised to the solvent boiling point, all residual air is expelled and the kier is filled with said vapors, (3) filling the kier with a solvent dyebath which is heated and circulated therethrough until the desired dye fixation temperature is reached and until said dye bath is substantially exhausted, (4) removing the exhausted dyebath and circulating solvent vapors to a superheater to provide superheated vapors to the kier in order to vaporize residual solvent in the yarn packages, (5) evacuating the kier and purging residual solvent vapors therein by means of an inert gas, (6) removing the dry dyed yarn packages and (7) recovering the solvent from the spent (exhausted) dye bath by distillation.
We claim:
1. In a method for dyeing packaged yarn in a discontinuous process by stacking the packaged yarn onto spindlesin a dye kier, filling the kier under pressure with dye liquor, heating said dye liquor while circulating the-same through the kier, draining the spent dye liquor from the kier and drying the yarn packages, the improvement which comprises:
l. sealing the kier and subjecting the interior to a vacuum,
2. introducing into said evacuated kier vapors of an organic solvent which is to be employed as the sol.- vent dye vehicle, continuing the introduction of vapors into said kier until the temperature of the kier and its contents are raised to the solvent boiling point, and the kier is filled with solvent vapors thereby expelling residual air from the kierand its contents,
3. filling the kier with a solvent dyebath which is heated and circulated through the kier until the desired dye fixation, temperature is obtained,
4. removing the dyebath, now spent, and circulating vapors from the kier to a heater to raise the temperature of the kier and contents to above the boiling point of the dye vehicle, diverting a portion of the vapors from the kier to a condenser, thus removing from the cycle those vapors in excess of that necessary to fill the kier and the vapor heating system,
5. evacuating and purging the kier with an inert gas to remove residual traces of solvent vapors,
6. removing the dry dyed yarns, and
7. recovering solvent from the spent dyebath.
Claims (14)
1. SEALING THE KIER AND SUBJECTING THE INTERIOR TO A VACUUM,
1. IN A METHOD FOR DYEING PACKAGED YARN IN A DISCONTINUOUS PROCESS BY STACKING THE PACKAGED YARN ONTO SPINDLES IN A DYE KIER, FILLING THE KIER UNDER PRESSURE WITH DYE LIQUOR, HEATING SAID DYE LIQUOR WHILE CIRCULATING THE SAME THROUGH THE KIER, DRAINING THE SPENT DYE LIQUOR FROM THE KIER AND DRYING THE YARN PACKAGES, THE IMPROVEMENT WHICH COMPRISES:
2. INTRODUCING INTO SAID EVACUATED KIER VAPORS OF AN ORGANIC SOLVENT WHICH IS TO BE EMPLOYED AS THE SOLVENT DYE VEHICLE, CONTINUING THE INTRODUCTION OF VAPORS INTO SAID KIER UNTIL THE TEMPERATURE OF THE KIER AND ITS CONTENTS ARE RAISED TO THE SOLVENT BOILING POINT,AND THE KIER IS FILLED WITH SOLVENT VAPORS THEREBY EXPELLING RESIDUAL AIR FROM THE KIER AND ITS CONTENTS,
2. introducing into said evacuated kier vapors of an organic solvent which is to be employed as the solvent dye vehicle, continuing the introduction of vapors into said kier until the temperature of the kier and its contents are raised to the solvent boiling point, and the kier is filled with solvent vapors thereby expelling residual air from the kier and its contents,
3. filling the kier with a solvent dyebath which is heated and circulated through the kier until the desired dye fixation temperature is obtained,
3. FILLING THE KIER WITH A SOLVENT DYEBATH WHICH IS HEATED AND CIRCULATED THROUGH THE KIER UNTIL THE DESIRED DYE FIXATION TEMPERATURE IS OBTAINED,
4. REMOVING THE DYEBATH NOW SPENT, AND CIRCULATING VAPORS FROM THE KIER TO A HEATER TO RAISE THE TEMPERATURE OF THE KIER AND CONTENTS TO ABOVE THE BOILING POINT OF THE DYE VEHICLE, DIVERTING A PORTION OF THE VAPORS FROM THE KIER TO A CONDENSER, THUS REMOVING FROM THE CYCLE THOSE VAPORS IN EXCESS OF THAT NECESSARY TO FILL THE KIER AND THE VAPOR HEATING SYSTEM,
4. removing the dyebath, now spent, and circulating vapors from the kier to a heater to raise the temperature of the kier and contents to above the boiling point of the dye vehicle, diverting a portion of the vapors from the kier to a condenser, thus removing from the cycle those vapors in excess of that necessary to fill the kier and the vapor heating system,
5. evacuating and purging the kier with an inert gas to remove residual traces of solvent vapors,
5. EVACUATING AND PURGING THE KIER WITH AN INERT GAS TO REMOVE RESIDUAL TRACES OF SOLVENT VAPORS,
6. removing the dry dyed yarns, and
6. REMOVING THE DRY DYED YARNS, AND
7. RECOVERING SOLVENT FROM THE SPENT DYEBATH.
7. recovering solvent from the spent dyebath.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US428299A US3871821A (en) | 1972-10-12 | 1973-12-26 | Package dye process |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US29688172A | 1972-10-12 | 1972-10-12 | |
US428299A US3871821A (en) | 1972-10-12 | 1973-12-26 | Package dye process |
Publications (1)
Publication Number | Publication Date |
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US3871821A true US3871821A (en) | 1975-03-18 |
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ID=26969863
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US428299A Expired - Lifetime US3871821A (en) | 1972-10-12 | 1973-12-26 | Package dye process |
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US (1) | US3871821A (en) |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0022572A1 (en) * | 1979-07-11 | 1981-01-21 | Karrer System AG | Process and apparatus for the wet treatment of fibrous material |
US4543676A (en) * | 1982-08-25 | 1985-10-01 | Fritz Karrer | Method of liquid treatment of textile fiber material |
EP0159878A2 (en) * | 1984-04-13 | 1985-10-30 | Frank G. Clifford | An apparatus for dyeing shaped articles |
US4828571A (en) * | 1984-04-13 | 1989-05-09 | Pensa Ildo E | Non-aqueous process for the dyeing of dyable materials at an elevated temperature in a non-reactive environment and in a non-aqueous dye solvent |
US4928338A (en) * | 1986-03-15 | 1990-05-29 | Mtm Obermaier Gmbh & Co. Kg | Process for the wet treatment of textile material |
US5121517A (en) * | 1989-12-28 | 1992-06-16 | Palitex Project Company Gmbh | Method of setting and dyeing yarn |
US5172443A (en) * | 1989-09-20 | 1992-12-22 | Then Maschinen Und Apparatebau Gmbh | Method and apparatus for wet-finishing textile goods |
US10280542B2 (en) * | 2016-05-27 | 2019-05-07 | Nantong Textile & Silk Industrial Technology Research Institute | Proofing dyeing cup for supercritical fluid dyeing and finishing |
US10294598B2 (en) * | 2016-05-30 | 2019-05-21 | Nantong Textile & Silk Industrial Technology Research Institute | Multi-pipe quantitative medium filling system of supercritical fluid dyeing machine |
US10294599B2 (en) * | 2016-05-27 | 2019-05-21 | Nantong Textile & Silk Industrial Technology Research Institute | Mobile dyeing cup for supercritical fluid dyeing and finishing |
US10344414B2 (en) * | 2016-05-30 | 2019-07-09 | Nantong Textile & Silk Industrial Technology Research Institute | Separation, recycling and self-cleaning system of supercritical fluid dyeing machine |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3692464A (en) * | 1970-10-26 | 1972-09-19 | Pegg S & Son Ltd | Solvent treatments of textiles |
-
1973
- 1973-12-26 US US428299A patent/US3871821A/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3692464A (en) * | 1970-10-26 | 1972-09-19 | Pegg S & Son Ltd | Solvent treatments of textiles |
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0022572A1 (en) * | 1979-07-11 | 1981-01-21 | Karrer System AG | Process and apparatus for the wet treatment of fibrous material |
WO1981000266A1 (en) * | 1979-07-11 | 1981-02-05 | Karrer System Ag | Method and plant for the processing of fiber materials by means of liquids |
US4369035A (en) * | 1979-07-11 | 1983-01-18 | Fritz Karrer | Process and apparatus for liquid treatment of fiber material |
US4543676A (en) * | 1982-08-25 | 1985-10-01 | Fritz Karrer | Method of liquid treatment of textile fiber material |
US4828571A (en) * | 1984-04-13 | 1989-05-09 | Pensa Ildo E | Non-aqueous process for the dyeing of dyable materials at an elevated temperature in a non-reactive environment and in a non-aqueous dye solvent |
EP0159878A3 (en) * | 1984-04-13 | 1987-10-14 | Frank G. Clifford | An apparatus for dyeing shaped articles |
EP0159878A2 (en) * | 1984-04-13 | 1985-10-30 | Frank G. Clifford | An apparatus for dyeing shaped articles |
US4928338A (en) * | 1986-03-15 | 1990-05-29 | Mtm Obermaier Gmbh & Co. Kg | Process for the wet treatment of textile material |
US5172443A (en) * | 1989-09-20 | 1992-12-22 | Then Maschinen Und Apparatebau Gmbh | Method and apparatus for wet-finishing textile goods |
US5121517A (en) * | 1989-12-28 | 1992-06-16 | Palitex Project Company Gmbh | Method of setting and dyeing yarn |
US10280542B2 (en) * | 2016-05-27 | 2019-05-07 | Nantong Textile & Silk Industrial Technology Research Institute | Proofing dyeing cup for supercritical fluid dyeing and finishing |
US10294599B2 (en) * | 2016-05-27 | 2019-05-21 | Nantong Textile & Silk Industrial Technology Research Institute | Mobile dyeing cup for supercritical fluid dyeing and finishing |
US10294598B2 (en) * | 2016-05-30 | 2019-05-21 | Nantong Textile & Silk Industrial Technology Research Institute | Multi-pipe quantitative medium filling system of supercritical fluid dyeing machine |
US10344414B2 (en) * | 2016-05-30 | 2019-07-09 | Nantong Textile & Silk Industrial Technology Research Institute | Separation, recycling and self-cleaning system of supercritical fluid dyeing machine |
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