Classifications

• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
  • D01F2/00—Monocomponent artificial filaments or the like of cellulose or cellulose derivatives; Manufacture thereof
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
  • B29C48/05—Filamentary, e.g. strands
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
  • B29C48/07—Flat, e.g. panels
  • B29C48/08—Flat, e.g. panels flexible, e.g. films
• • D—TEXTILES; PAPER
  • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
  • D01D—MECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
  • D01D5/00—Formation of filaments, threads, or the like
  • D01D5/06—Wet spinning methods
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
  • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
  • B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
  • B29C48/25—Component parts, details or accessories; Auxiliary operations
  • B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
  • B29C48/919—Thermal treatment of the stream of extruded material, e.g. cooling using a bath, e.g. extruding into an open bath to coagulate or cool the material

Definitions

• This invention relates to methods of manufacturing cellulose articles in which a solution of cellulose in a tertiary a ine N-oxide is extruded by way of a die into a coagulating bath.
• cellulose can be dissolved in certain tertiary amine N-oxides (which may for convenience also be called amine oxides) to form a solution or dope which can be extruded by way of a die into a coagulating bath to form shaped articles such as fibres and films.
• the dope generally contains a small proportion of water, ar.d the coagulating bath is usually an aqueous bath.
• the coaculated article is then washed to remove residual amine oxide therefrom.
• This process is an example of a solvent-spinning process, and fibre so produced may be called solvent-spun cellulose fibre or lyocell fibre.
• An example of a suitable amine oxide solvent is N-methylmorpholine N-oxide (NMMO) .
• WO-A-93/19230 describes a solvent-spinning process wherein the filaments in the air-gap are cooled before introduction into the coagulating bath, for example by subjecting them to a current of cold air.
• the temperature of the dope may be 90 to 110°C, the temperature of the cooling air -5 to -*-5°c, and the length of the air-gap 60 to 145 mm.
• theie is provided a method of manufacturing extruded articles of lyocell wherein a solution of cellulose in a tertiary a_..ine N-oxide is extruded by way cf a die through an air-gap into a coagulating bath, air being supplied to anc discharged from the air-gap, characterised in that the air-gap comprises a first region adjacent the face of the c;e and a second region more remote from the face of the cie, the moisture content of the air supplied to the first region being maintained at a lower value than the moisture content of the air supplied to the second region.
• the extruded lyocell articles may take the form of films or, preferably, filaments (including not only tows of filaments which may subsequently be cut to form staple fibre but also continuous filament yarns).
• the die is commonly called a spinnerette, and the process of extrusion is commonly called spinning.
• the length of the air-gap between the die and the coagulating bath is preferably in the range 10 to 160 mm, more preferably 15 to 100 mm or 20 to 60 mm. It will be understood that, although the gas in the air-gap is preferably air, other inert gases or gas mixtures, for example nitrogen, may be used.
• the two regions of the air-gap may be of the same or different lengths.
• the length of the first region is less than the length of the second region.
• the first region is preferably 3 to 10 mm in length so that the second region occupies the remaining longer portion of the air-gap.
• the cellulose solution (which may also be called a dope) is conventionally extruded downwardly through the air-gap.
• Air is preferably supplied to and extracted from the air-gap in a direction substantially transverse to the direction of travel of the dope extrudate through the air-gap, that is to say horizontally when using such conventional extrusion techniques.
• the current of air flowing across the air-gap may conveniently be referred to as a cross-draft.
• the velocity of the air supplied to the air-gap in both regions is preferably in the range 1 to 20 m/sec, more preferably 2 to 10 m/sec.
• the velocity of the air should be high enough to maintain different atmospheric conditions around the dope extrudate within the two different regions of the air-gap, but not so high as to disrupt the orderly passage of the dope extrudate therethrough. In general, higher velocities may cause such disruption in longer air-gaps.
• the velocity of the air in the first and second regions of the air-gap may be the same or different. Suitable air velocities can be determined in any particular case by simple trial.
• Air can conveniently be supplied to and extracted from the air-gap by suitably designed blowing and suction nozzles. It will be understood that separate blowing nozzles are required for each of the first and second regions. There may be one or more suction nozzles. In a preferred embodiment, each blowing nozzle faces towards a suction nozzle of similar dimensions thereto. This has the advantage that it permits closer control of the atmospheric conditions around the dope extrudate across each region of the air-gap; particularly in the first region if, as may be preferred, the length of the first region is less than the length of the second region.
• the temperature of the air supplied to the air-gap is generally around ambient temperature, for example in the range 0 to 40°C, often 20 to 30°C.
• the temperature of the dope supplied to the die is commonly in the range of about 80-125°C, and the air flow accordingly serves to cool the extrudate in the air gap.
• the take-up velocity of the extruded article from the coagulation bath is higher than the extrusion velocity of the dope through the die, often by about a factor in the range 2.5 to 25, so as to stretch the extrudate with the purpose of improving its mechanical properties. It is thought that such stretching occurs almost entirely within the air-gap.
• Cooling the extrudate in the air-gap often restricts the zone in which stretching occurs to the portion of the air-gap closest to the face of the die. In the method of the invention, it may be preferred that substantially all the stretching occurs within the first region of the air-gap.
• the take-up velocity of the extruded article is preferably in the range 5 to 100 m/min.
• the moisture content of the air supplied to the second region of the air-gap is preferably in the range of about 1 to 30 g, more preferably 10 to 20 g, water per kg air greater than the moisture content of the air supplied to the first region.
• the moisture content of the air supplied to the first region is preferably in the range 0 to 20, more preferably 0 to 10, g water per kg air, and the moisture content of the air supplied to the second region is preferably in the range 5 to 30 g water per kg air.
• Lyocell fibres commonly exhibit a tendency to fibrillate, particularly when subjected to mechanical stress during hot wet processing treatments such as those commonly encountered during fabric manufacture, for example scouring, bleaching and dyeing. On fibrillation, long fibrils become partially detached from the surface of the fibre, giving the individual fibres (as well as yarns and fabrics containing them) a hairy appearance which may be aesthetically unpleasing. It has surprisingly been found that fibre produced by the method of the invention may exhibit a lower tendency towards fibrillation than fibre produced by conventional fibre spinning techniques. - D -
• the average degree of polymerisation (D.P.) of the cellulose in the dope may generally be in the range 250 to
• cellulose D.P. is in the range 750 to 1000.
• the degree of polymerisation (D.P.) of cellulose is conveniently 0 assessed by viscosimetry of a dilute solution of cellulose in an aqueous metal/amine complex solvent, for example cuprammonium hydroxide solution. A suitable method, based on TAPPI Standard T206, is described hereinafter as Test Method 3.
• Cellulose D.P. is a measure of the number of 5 anhydroglucose units per molecule. It will be understood that D.P. measured in this manner is a viscosity average D.P.
• a solution of cellulose in aqueous amine oxide is fed by way of a gear pump 1 to a spinnerette 2.
• the dope may for example contain 5 to 25% by weight cellulose, 70 to 85% by weight NMMO and 5 to 15% by weight water, and the temperature of the dope may be in the range 80 to 125°C.
• the dope is extruded downwardly through the holes in the s innerette 2 into an air gap 3 maintained at a temperature below that of the dope, where it solidifies to form a bundle of filaments 4.
• the filaments 4 then pass into an aqueous coagulating bath 5, pass partly around a roller 6 and are withdrawn for washing, drying and other conventional processing operations.
• the surface speed of the roller 6 is higher than the velocity of the dope issuing through the holes of the spinnerette 2 so as to stretch the filaments 4. Stretching of the filaments occurs largely within the air gap 3.
• a first supply of air is blown into the air-gap 3 in a first region 9 adjacent the spinnerette 2 from a blowing nozzle 7 and extracted from the air-gap 3 by a suction nozzle 8, so that it passes through the air-gap 3 transversely to the direction of travel of the filaments 4.
• the nozzles 7, 8 are so arranged that this procedure serves to maintain the temperature and humidity of the atmosphere in the first region 9, which lies adjacent the face 2a of the spinnerette 2, at desired values.
• a second supply of air is similarly blown into the air-gap 3 in a second region 12 remoter from the spinnerette 2 from a blowing nozzle 10 to a suction nozzle 11.
• the nozzles 10, 11 are so arranged that this procedure serves to maintain the temperature and humidity of the second region 12, situate between the first region 9 and the coagulating bath 5, at desired values.
• the nozzles 7 and 10 extend to supply air across the entire bundle 4 of filaments.
• the moisture content of the air supplied to blowing nozzle 7 is lower than that supplied to blowing nozzle 10.
• the temperatures of the two supplies of air may be the same or different.
• the fibrillation tendency of lyocell fibre may be assessed by the following Test Methods:
• a small tuft cf fibre containing 100 to 200 filaments is cut to 5 mm lengths. These short fibres are placed in a 20 ml phial containing 4 g of glass micro-beads, and 8 ml water is added. The phial is securely stoppered and shaken on a
• the fibrillation index (C t ) is calculated from optical micrographs of the fibrillated fibres.
• the total lengths of the fibrils, f, attached to a length of fibre, L, are measured.
• the fibrillation index is given by the equation:
• This operation can be carried out manually or by image analysis. Alternatively, a set of standard micrographs can be set up for comparison. Trained fibre technologists have been found to be consistent in their assessment with this method. In practice, it is impossible to measure a fibrillation index above about 30, owing to the difficulty in seeing the large number of fibrils. Data are measured on the middle of the 5 mm length of fibre and on the end. Experience shows that the result for the fibre end correlates best to fabric performance, and only this is the figure quoted herein as C f (TM1). -8- Test Method 2 (Scour-dye.
• Fibrillation Index F.I.
• Samples of fibre were arranged into a series showing increasing degrees of fibrillation.
• a standard length of fibre from each sample was then measured and the number of fibrils (fine hairy spurs extending from the main body of the fibre) along the standard length was counted.
• the length of each fibril was measured, and an arbitrary number, being the product of the number of fibrils multiplied by the average length of each fibril, was determined for each fibre.
• the fibre e.xhibiting the highest value of that arbitrary number was identified as being the most fibrillated fibre and was assigned an arbitrary Fibrillation Index of 10.
• a wholly unfibrillated fibre was assigned a Fibrillation Index of zero, and the remaining fibres were ranged from 0 to 10 based on the microscopically measured arbitrary numbers.
• the measured fibres were then used to form a standard graded scale.
• To determine the Fibrillation Index for any other sample of fibre five or ten fibres were visually compared under the microscope with the standard graded fibres. The visually determined numbers for each fibre were then averaged to give a Fibrillation Index for the sample under test. It will be appreciated that visual determination and averaging is many times quicker than measurement, and it has been found that skilled fibre technologists are consistent in their rating of fibres.
• the Fibrillation Index of fabrics can be assessed on fibres drawn from the surface of the fabric. Woven and knitted fabrics having an F.I. of more than about 2.0 to 2.5 exhibit an unsightly appearance.
• a tow of 1.7 dtex lyocell fibres was crimped and cut to form 30 mm staple fibre, which was spun into 20 tex yarn.
• the yarn was knitted into an 80 mm wide stockinette, which was scoured and eyed to a navy blue shade.
• the knitted fabric was washed at 40°C in a domestic washing machine and dried in a domestic tumble dryer.
• the Fibrillation Index (F.I.) was measured on fibres drawn from the surface of the dry fabric either after scouring and dyeing or after one or more wash/tumble (W/T) cycles.
• a spinning dope was prepared containing woodpulp cellulose (various proportions; various degrees of polymerisation (D.P.)) specified below, 74-80% NMMO and 7.5- 12.6% water. This was extruded by way of a spinnerette (head temperature 115°C) containing 95 holes each 80 micron in diameter through an air-gap of length specified below into - 10 - temperature 115°C) containing 95 holes each 80 micron in diameter through an air-gap of length specified below into a coagulating bath comprising 25% NMMO and 75% water 25°C to form lyocell fibre. Air was blown transversely across the 5 extruded filaments from upper and lower supplies . The depth of the first, upper region of these cross-drafts was approximately 4 mm. The second, lower cross-draft was produced by directing an air flow from a hand-held electric blower through a shaped funnel. The moisture content of the
• Spinning speed 30 m/min; air-gap 150 mm; upper air-supply 0 (first region) 20°C/40% R.H. ; lower air-supply (second region) 30°C/60% R.H.
• first region 20°C/40% R.H.
• second region 30°C/60% R.H.
• Example 1 was repeated, except that the dope contained 15.2% woodpulp cellulose (D.P. 600), 75% NMMO and 9.8% water.
• the fibre so produced was assessed for fibrillation 5 tendency using Test Methods 1 and 2.
• Experimental details and results are presented in Table 2:
• Example 1 was repeated, except that the temperatures and relative humidities of the upper air supply were 20°C and 40% and of the lower air supply were 30°C and 60%. Other experimental details and results are presented in Table 3:
• Tow tension is an arbitrary number, higher values indicating higher tensions. Some stuck filaments were observed on occasion with the longer air-gaps, particularly at the higher air velocity.
• a spinning dope was prepared containing 13% cellulose (average D.P. 800), 75% NMMO and 12% water. It was extruded downwardly through a spinnerette,having 18,400 holes each 70 micron in diameter clustered in three parallel rows each about 1 m long (dope temperature 83°C) , through a 30 mm air-gap into a coagulating bath containing 25% NMMO and 75% water to form a tow of lyocell filaments.

Landscapes

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

Applications Claiming Priority (3)

Publications (1)

Family

ID=10767787

Family Applications (1)

Country Status (13)

Families Citing this family (27)

Family Cites Families (4)

• 1995
  • 1995-01-10 GB GBGB9500387.7A patent/GB9500387D0/en active Pending
• 1996
  • 1996-01-09 SK SK841-97A patent/SK84197A3/sk unknown
  • 1996-01-09 WO PCT/GB1996/000030 patent/WO1996021758A1/en not_active Application Discontinuation
  • 1996-01-09 TR TR97/00597T patent/TR199700597T1/xx unknown
  • 1996-01-09 KR KR1019970704662A patent/KR19980701273A/ko not_active Application Discontinuation
  • 1996-01-09 CN CN96191362A patent/CN1168159A/zh active Pending
  • 1996-01-09 CZ CZ972066A patent/CZ206697A3/cs unknown
  • 1996-01-09 AU AU43514/96A patent/AU4351496A/en not_active Abandoned
  • 1996-01-09 EP EP96900125A patent/EP0802992A1/de not_active Ceased
  • 1996-01-09 JP JP8521509A patent/JPH10505886A/ja active Pending
  • 1996-01-09 BR BR9606733A patent/BR9606733A/pt not_active Application Discontinuation
  • 1996-01-11 TW TW085100387A patent/TW303395B/zh active
• 1997
  • 1997-06-10 FI FI972465A patent/FI972465A/fi unknown

Non-Patent Citations (1)

Also Published As

Similar Documents

Legal Events