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US2934448A - Spun dyed yarn - Google Patents

Spun dyed yarn Download PDF

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Publication number
US2934448A
US2934448A US430813A US43081354A US2934448A US 2934448 A US2934448 A US 2934448A US 430813 A US430813 A US 430813A US 43081354 A US43081354 A US 43081354A US 2934448 A US2934448 A US 2934448A
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US
United States
Prior art keywords
stream
viscose
solution
spinning solution
supply
Prior art date
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.)
Expired - Lifetime
Application number
US430813A
Inventor
Theodore E Patton
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Akzona Inc
Original Assignee
American Enka Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority to BE526558D priority Critical patent/BE526558A/xx
Priority to BE535477D priority patent/BE535477A/xx
Priority to NL78571D priority patent/NL78571C/xx
Priority to NLAANVRAGE7907437,A priority patent/NL177639B/en
Priority to DEA19722A priority patent/DE1086851B/en
Priority to GB532954A priority patent/GB756590A/en
Priority to US430813A priority patent/US2934448A/en
Application filed by American Enka Corp filed Critical American Enka Corp
Priority to GB455555A priority patent/GB777990A/en
Priority to ES0220793A priority patent/ES220793A2/en
Priority to ES0220792A priority patent/ES220792A1/en
Priority to US65500457 priority patent/US2929731A/en
Application granted granted Critical
Publication of US2934448A publication Critical patent/US2934448A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D1/00Treatment of filament-forming or like material
    • D01D1/06Feeding liquid to the spinning head
    • D01D1/065Addition and mixing of substances to the spinning solution or to the melt; Homogenising
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • B01F35/712Feed mechanisms for feeding fluids
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/8593Systems
    • Y10T137/85978With pump
    • Y10T137/86131Plural
    • Y10T137/86139Serial
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T137/00Fluid handling
    • Y10T137/8593Systems
    • Y10T137/87571Multiple inlet with single outlet
    • Y10T137/87652With means to promote mixing or combining of plural fluids

Definitions

  • Thisinvention relates to a method for adding an adjustable amount of a liquid to a viscous spinning solution and is an improvement in the invention described in Serial Number 417,196, filed March 18, 1954, now abancloned in favor of continuation application Serial No. 655,004, filed August 25, 1957.
  • Figure 1 is a schematic layout of an'additive supply system in which the present invention is incorporated.
  • Figure 2 is a side view to an enlarged scale partly in section showing an additive introduction arrangement according to the present invention.
  • the aboveidentified system of providing a shunt stream of viscose and introducing a predetermined quantity of additive thereto prior to combining with a main stream is improved upon by installing at the point of additive introduction a special T-connection having a noule which insures that all of said dispersion is introduced coaxially or centrally of the shunt stream in a direction toward the high capacity pump.
  • This improved system has been found to result in much more homogeneous mixing without the necessity of additional elaborate equipment.
  • a viscous spinning solution is supplied through a pipeline 1 to a spinning machine 2 through a mixer 12.
  • the pipe 1 has a shunt or by-p'ass 3 through which part of .the spinning solution flows.
  • pumps 4 and S which are interconnected in series by a tube including the cross conduit ofa T-connection '6.
  • a filter 9 is located in the pipe 7 and, associated with the filter, are valves and 11.
  • the pipe 7 is in open connection with the reservoir 8 for the low viscosity additive.
  • the shunt or by-pass pipe 3 and the main viscose pipeline 1 discharge In this shunt there are located two gear into the mixer 12, and, from any suitable mixer may be used.
  • Pump 4 is operatedto deliver less than pump- 5; therefore. dyestufi solutions or pigment suspension flows, from pipe 7 through the con :1 nection 6 into the spinning solution, the. total of. the 'two' solutions meeting the pumping demand; of pump 5.
  • a nozzle which carries the dyestufli into the center of the stream in conduit 13.
  • This nozzle bearsreference numeral 21. substantially uniform cross-section throughout its length but the conduit area within the nozzle 21 is less than the conduit area within the tube 1.
  • Nozzle 21 is curved so that its mouth faces pump 5.
  • the entire T-connection is made of glass.
  • Glass is a suitable material because it is resistant to the chemi- ;;solution is brought about.
  • the improved results obtained with the present invention are believed to be due to the fact that under the conditionsof viscous flow existing in the pipe 3 the dye dispersion does not intimately mix with the viscose solution until introduced into mixer 12. This arrangement prevents stratification of the dye dispersion in pipe 3 and also facilitates the pumping of the mixture through pump 5. While in the illustrated embodiment the pumps 4 and 5 in the additive line are applied to a by-pass in the main system, the actual proportioning of flow between the lines 1 and 3 may vary considerably even to the point where the line 3 carries more than half of the total spinning solution.
  • a supply conduit for supplying viscose spinning solution to said blending apparatus, a aelivery conduit for delivering said viscose spinning solution to a spinning machine, a pair of connecting conduits extending from said supply conduit to said delivery con:
  • one of said connecting conduits supplying viscose spinning solution from said supply conduit directly to said delivery conduit, a gear pump of low capacity and a gear pump of high capacity in the other of said connecting conduits, the gear pump of high capacity being nearer said delivery conduit, and means providing a supply 2,934,448. g at nted Apr; 2 6,

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • Textile Engineering (AREA)
  • Coloring (AREA)
  • Artificial Filaments (AREA)
  • Treatment Of Fiber Materials (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Description

Un ted S es ,Patent'O ice SPUN DYED YARN j Theodore E. Patton, Erika, N.C., assignor to American 21m Corporation, Enka, N.C., a corporation of Delare Q, I Application May 19, 1954, Serial No. 430,813.
g 2 Claims. (Cl. 106'165) I Thisinvention relates to a method for adding an adustable amount of a liquid to a viscous spinning solution and is an improvement in the invention described in Serial Number 417,196, filed March 18, 1954, now abancloned in favor of continuation application Serial No. 655,004, filed August 25, 1957.
In said application Serial No. 655,004 there is described a system for adding materials such as dyestuli to a spinning solution. According to that application, the spinning solution being delivered to the spinnerets is divided into two streams and, in one of the streams, a suction zone is created by arranging two pumps in tandem, the second drawing more than the first delivers. The desired additive is introduced into this suction zone through an ordinary T-connection.
While the above arrangement is entirely satisfactory for some additives and for some spinning solutions, it has been found that the homogeneity of dye distribution in viscose is not reliably maintained.
It is therefore an object of the present invention to overcome this difiiculty and to provide for an improved admixture of an additive with a spinning solution.
Other objects and advantages of this invention will be apparent upon consideration of the following detailed description of a preferred embodiment thereof in conjunction with the annexed drawings, wherein:
Figure 1 is a schematic layout of an'additive supply system in which the present invention is incorporated; and
Figure 2 is a side view to an enlarged scale partly in section showing an additive introduction arrangement according to the present invention.
In accordance with the present invention, the aboveidentified system of providing a shunt stream of viscose and introducing a predetermined quantity of additive thereto prior to combining with a main stream is improved upon by installing at the point of additive introduction a special T-connection having a noule which insures that all of said dispersion is introduced coaxially or centrally of the shunt stream in a direction toward the high capacity pump. This improved system has been found to result in much more homogeneous mixing without the necessity of additional elaborate equipment.
Referring to the drawing in greater detail, a viscous spinning solution is supplied through a pipeline 1 to a spinning machine 2 through a mixer 12. The pipe 1 has a shunt or by-p'ass 3 through which part of .the spinning solution flows. pumps 4 and S which are interconnected in series by a tube including the cross conduit ofa T-connection '6. A supply pipe 7, serving to supply a dyestuif solution or a pigment suspensionfrom a reservoir 8, discharges into the intersecting conduit of the T-connection 6. A filter 9 is located in the pipe 7 and, associated with the filter, are valves and 11.
During use the pipe 7 is in open connection with the reservoir 8 for the low viscosity additive. The shunt or by-pass pipe 3 and the main viscose pipeline 1 discharge In this shunt there are located two gear into the mixer 12, and, from any suitable mixer may be used. Pump 4 is operatedto deliver less than pump- 5; therefore. dyestufi solutions or pigment suspension flows, from pipe 7 through the con :1 nection 6 into the spinning solution, the. total of. the 'two' solutions meeting the pumping demand; of pump 5.
nated by numeral 18 and it is provided with a collar 19 and sealing gaskets working with an end flange 20.
At the point where the conduit 18 discharges into the conduit 13 a nozzle is formed which carries the dyestufli into the center of the stream in conduit 13. This nozzle bearsreference numeral 21. substantially uniform cross-section throughout its length but the conduit area within the nozzle 21 is less than the conduit area within the tube 1. Nozzle 21 is curved so that its mouth faces pump 5.
As shown in Figure 2, the entire T-connection, except for the collars 14, 15 and 19, is made of glass. Glass is a suitable material because it is resistant to the chemi- ;;solution is brought about.
dispersion to viscose solution the improved results obtained with the present invention are believed to be due to the fact that under the conditionsof viscous flow existing in the pipe 3 the dye dispersion does not intimately mix with the viscose solution until introduced into mixer 12. This arrangement prevents stratification of the dye dispersion in pipe 3 and also facilitates the pumping of the mixture through pump 5. While in the illustrated embodiment the pumps 4 and 5 in the additive line are applied to a by-pass in the main system, the actual proportioning of flow between the lines 1 and 3 may vary considerably even to the point where the line 3 carries more than half of the total spinning solution.
Inasmuch as other alternatives and modifications will become apparent to those skilled in this art, it is intended that the present invention be limited only to the,
:extent set forth in the following claims.
What is claimed is:
1. In an, apparatus for blending a dyevdispersion a viscose spinning solution having higher viscosity than said dispersion including a supply conduit for supplying viscose spinning solution to said blending apparatus, a aelivery conduit for delivering said viscose spinning solution to a spinning machine, a pair of connecting conduits extending from said supply conduit to said delivery con:
duit, one of said connecting conduits supplying viscose spinning solution from said supply conduit directly to said delivery conduit, a gear pump of low capacity and a gear pump of high capacity in the other of said connecting conduits, the gear pump of high capacity being nearer said delivery conduit, and means providing a supply 2,934,448. g at nted Apr; 2 6,
the mixer lithe goes tothe spinning machine 2. The particular mixen; used at 12 forms no part of the present inventionand This conduit is held Ihe nozzle is of v with Q i i be iiIdisbei ioi1g the iinpro 1 nec tion havinga', crossconduitconneting said pumps in nlentecomprising 2 1- T-conspinning meeh ine, the hifionensent eomp fisi ng int focfie ing' all of said dye dispersion from the supply tl nerefor' series within said other connecting conduit and an interfleeting eonduitg said intersectin'g pond-nit terminating in coaxially into the'center of said second stream; whereby homogeneous blending of the dye within the viscose solue nozileglisposed'cefiti'al ly and- Coaidally of me crass? tion will occur.
visose spinning solation having higher viscosity'lh'an' 7 said dispersion includingjthestepsofmaintaining a; supply of: viscose spinning 'solution',-'dividing sajgl supply =into -=99 d" ;?n ohnecting'said intersecting 'conginit to V j u yfi dy persion, '7 i V Y In memod'ror; blen' djng a dye-odis a ,-r,lfi rst nd second str eamsj,' "djrecting'viscoseQspinn ng solu- V etionfrom said first streamftoward aspinning machine,
feeding viscose spinn ing' s olutioniinto said'seoond stream" 1 atla' -first rate and wi thdrawing said solution from: this stieam a t a second, higher, fate, supplying adye dispersion to 'sai d-second stream at'a'pointprior to withdrawalof said second stream-at said higher rate; and combining said I and seqondstreams before int roduetionto said References Cited the file of this patent j '1 NIT STA'ITES PATENTS"

Claims (1)

  1. 2. IN A METHOD FOR BLENDING A DYE DISPERSION WITH A VISCOSE SPINNING SOLUTION HAVING HIGHER VISCOSITY THAN SAID DISPERSION INCLUDING THE STEPS OF MAINTAINING A SUPPLY OF VISCOSE SPINNING SOLUTION, DIVIDING SAID SUPPLY INTO FIRST AND SECOND STREAMS, DIRECTING VISCOSE SPINNING SOLUTION FROM SAID FIRST STREAM TOWARD A SPINNING MACHINE, FEEDING VISCOSE SPINNING SOLUTION INTO SAID SECOND STREAM AT A FIRST RATE AND WITHDRAWING SAID SOLUTION FROM THIS STREAM AT A SECOND, HIGHER, RATE, SUPPLYING A DYE DISPERSION TO SAID SECOND STREAM AT A POINT PRIOR TO WITHDRAWAL OF SAID SECOND STREAM AT SAID HIGHER RATE, AND COMBINING SAID FIRST AND SECOND STREAMS BEFORE INTRODUCTION TO SAID SPINNING MACHINE, THE IMPROVEMENT COMPRISING INTRODUCING ALL OF SAID DYE DISPERSION FROM THE SUPPLY THEREFOR COAXIALLY INTO THE CENTER OF SAID SECOND STREAM, WHEREBY HOMOGENEOUS BLENDING OF THE DYE WITHIN THTE VISCOSE SOLUTION WILL OCCUR.
US430813A 1953-04-17 1954-05-19 Spun dyed yarn Expired - Lifetime US2934448A (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
BE526558D BE526558A (en) 1953-04-17
BE535477D BE535477A (en) 1953-04-17
NL78571D NL78571C (en) 1953-04-17
NLAANVRAGE7907437,A NL177639B (en) 1953-04-17 HIGH PRESSURE SODIUM VAPOR DISCHARGE LAMP.
DEA19722A DE1086851B (en) 1953-04-17 1954-02-18 Device for incorporating adjustable amounts of liquid into a viscous spinning solution
GB532954A GB756590A (en) 1953-04-17 1954-02-23 Improved method of adding a liquid to a viscous spinning solution
US430813A US2934448A (en) 1954-05-19 1954-05-19 Spun dyed yarn
GB455555A GB777990A (en) 1953-04-17 1955-02-15 Improved method for adding a liquid to a viscous spinning solution
ES0220793A ES220793A2 (en) 1954-05-19 1955-03-21 Spun dyed yarn
ES0220792A ES220792A1 (en) 1954-05-19 1955-03-21 Spun dyed yarn
US65500457 US2929731A (en) 1953-04-17 1957-04-25 Process for mixing coloring material with viscose

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US430813A US2934448A (en) 1954-05-19 1954-05-19 Spun dyed yarn

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US2934448A true US2934448A (en) 1960-04-26

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US430813A Expired - Lifetime US2934448A (en) 1953-04-17 1954-05-19 Spun dyed yarn

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ES (2) ES220792A1 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3348685A (en) * 1964-09-02 1967-10-24 Phillips Petroleum Co Filter apparatus and filter aid feeding and controlling system
US3417779A (en) * 1967-01-09 1968-12-24 Perkin Elmer Corp Selectable concentration gas mixing apparatus
US3999572A (en) * 1975-03-24 1976-12-28 The Garrett Corporation Fluid flow instrumentality
WO1992007120A1 (en) * 1990-10-15 1992-04-30 E.I. Du Pont De Nemours And Company Method of mixing additive solutions into para-aramid dope streams
US6405759B1 (en) * 1997-08-05 2002-06-18 Owens Corning Composites Sprl Apparatus for the continuous preparation of glass fiber sizing compositions
DE10022889B4 (en) * 2000-05-25 2007-12-20 Lurgi Zimmer Gmbh Process for producing synthetic threads from a polyester-based polymer blend

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1007788A (en) * 1910-09-26 1911-11-07 Charles E Hailstone Means for transporting oil.
US1907486A (en) * 1931-08-13 1933-05-09 Cherry Burrell Corp Aerating means for freezers and the like
US2541799A (en) * 1947-05-22 1951-02-13 Eugene B White Method of feeding chemicals
US2565374A (en) * 1949-11-30 1951-08-21 Standard Oil Dev Co Compounding of reciprocating pumps
US2650168A (en) * 1948-10-18 1953-08-25 American Enka Corp Method for dispersing an immiscible pigment in viscose solution
US2656648A (en) * 1942-01-28 1953-10-27 Friedmann Giovanni Means for transporting and distributing fertilizers on fields
US2768135A (en) * 1953-08-04 1956-10-23 Infilco Inc Electrolytic cell

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1007788A (en) * 1910-09-26 1911-11-07 Charles E Hailstone Means for transporting oil.
US1907486A (en) * 1931-08-13 1933-05-09 Cherry Burrell Corp Aerating means for freezers and the like
US2656648A (en) * 1942-01-28 1953-10-27 Friedmann Giovanni Means for transporting and distributing fertilizers on fields
US2541799A (en) * 1947-05-22 1951-02-13 Eugene B White Method of feeding chemicals
US2650168A (en) * 1948-10-18 1953-08-25 American Enka Corp Method for dispersing an immiscible pigment in viscose solution
US2565374A (en) * 1949-11-30 1951-08-21 Standard Oil Dev Co Compounding of reciprocating pumps
US2768135A (en) * 1953-08-04 1956-10-23 Infilco Inc Electrolytic cell

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3348685A (en) * 1964-09-02 1967-10-24 Phillips Petroleum Co Filter apparatus and filter aid feeding and controlling system
US3417779A (en) * 1967-01-09 1968-12-24 Perkin Elmer Corp Selectable concentration gas mixing apparatus
US3999572A (en) * 1975-03-24 1976-12-28 The Garrett Corporation Fluid flow instrumentality
WO1992007120A1 (en) * 1990-10-15 1992-04-30 E.I. Du Pont De Nemours And Company Method of mixing additive solutions into para-aramid dope streams
US6405759B1 (en) * 1997-08-05 2002-06-18 Owens Corning Composites Sprl Apparatus for the continuous preparation of glass fiber sizing compositions
DE10022889B4 (en) * 2000-05-25 2007-12-20 Lurgi Zimmer Gmbh Process for producing synthetic threads from a polyester-based polymer blend

Also Published As

Publication number Publication date
ES220793A2 (en) 1956-01-01
ES220792A1 (en) 1956-01-01

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