EP2119816A1 - Spinneret comprising bilobal spinning orifices - Google Patents
Spinneret comprising bilobal spinning orifices Download PDFInfo
- Publication number
- EP2119816A1 EP2119816A1 EP08008901A EP08008901A EP2119816A1 EP 2119816 A1 EP2119816 A1 EP 2119816A1 EP 08008901 A EP08008901 A EP 08008901A EP 08008901 A EP08008901 A EP 08008901A EP 2119816 A1 EP2119816 A1 EP 2119816A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- spinneret
- bilobal
- spinning
- filaments
- orifices
- 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.)
- Granted
Links
- 238000009987 spinning Methods 0.000 title claims abstract description 41
- 238000001816 cooling Methods 0.000 claims abstract description 8
- 238000007664 blowing Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 13
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 229920000642 polymer Polymers 0.000 description 13
- 238000010791 quenching Methods 0.000 description 7
- 239000000155 melt Substances 0.000 description 6
- 230000000171 quenching effect Effects 0.000 description 6
- 238000001125 extrusion Methods 0.000 description 3
- 230000002238 attenuated effect Effects 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229920001169 thermoplastic Polymers 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 239000004750 melt-blown nonwoven Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 235000001954 papillon Nutrition 0.000 description 1
- 244000229285 papillon Species 0.000 description 1
Images
Classifications
-
- 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
- D01D5/253—Formation of filaments, threads, or the like with a non-circular cross section; Spinnerette packs therefor
-
- 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
- D01D4/00—Spinnerette packs; Cleaning thereof
- D01D4/02—Spinnerettes
- D01D4/025—Melt-blowing or solution-blowing dies
-
- 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
- D01D5/08—Melt spinning methods
- D01D5/088—Cooling filaments, threads or the like, leaving the spinnerettes
-
- 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
- D01D5/08—Melt spinning methods
- D01D5/098—Melt spinning methods with simultaneous stretching
- D01D5/0985—Melt spinning methods with simultaneous stretching by means of a flowing gas (e.g. melt-blowing)
Definitions
- the present invention relates to the field of spunbond technology or meltblown technology.
- the invention relates to an improved spinneret for manufacturing spunbonded or meltblown nonwovens, said spinneret comprising bilobal spinning orifices.
- Spunbonded nonwoven webs are produced by depositing extruded spun filaments onto a collecting moving belt, preferably a foraminous belt, in a random manner, and by bonding the filaments.
- an extrusion die comprising a plate perforated with a lot of small orifices, and usually referred as spinneret plate, is used.
- a spinneret plate comprises more than one hundred spinning orifices per meter.
- the continuous spun filaments are formed by forcing one or several molten thermoplastic polymers to pass through said small orifices of the spinneret plate.
- only one spinneret plate can be used or several spinneret plates that are placed side by side can be used.
- each filament is given by the geometry of the spinning orifice of the spinneret plate through which the filament is being formed.
- Different shapes of filaments can be produced to date, like for example round filaments, bilobal filaments, trilobal filaments. More particularly, for producing a bilobal filament, also commonly referred as "papillon" filament, a bilobal orifice consisting essentially of two circular apertures connected with one another by a connecting aperture is used. All the spinning orifices of a spinneret plate can have the same geometry, or a spinneret plate can have spinning orifices of different shapes, like for example round orifices combined with bilobal orifices.
- the spun filaments are rapidly cooled by cold air streams that are blown below the spinneret plate (quenching step), and the filaments are then stretched and attenuated by additional blown air streams in order to orient the molecular chains and increase the filament strength.
- the melt blown process is somewhat similar to the spunbond process from an equipment and operator's point of view.
- the two main differences between a melt blown process and a spunbond process that use air attenuation are: (i) the temperature and volume of air used to attenuate the filaments and (ii) the location where the filament draw or attenuation force is applied.
- a meltblown process a high volume air flow at a temperature which is typically equal or slightly greater than the melt temperature of the polymer, is used to attenuate the filaments.
- the spunbond process generally uses a smaller volume of cold air close to ambient temperature to first quench and solidify the filaments and then to attenuate said filaments.
- the draw or attenuation force is applied at the exit of the extrusion die (spinneret) while the polymer is still in the molten state, whereas in the spunbond process, this force is applied at some distance from the spinneret plate, after the polymer has been cooled and solidified (quenching step).
- the spinneret of a spunbonded unit comprises an apertured spinneret plate through which the molten polymer is extruded
- the spinneret generally comprises a so-called die nosepiece with spinning orifices.
- die nosepiece There are typically two types of die nosepiece.
- One type is the capillary type wherein slots are milled into a flat surface and then matched with identical slots milled into a mating surface. The two halves are then matched and carefully aligned to form a row of spinning orifices.
- the second type is the drilled-hole type wherein spinning orifices are drilled in a single block of metal.
- One main objective of the invention is to improve the spinning of bilobal filaments in a spunbond process or in a meltblown process.
- the particular orientation of the bilobal spinning orifices as defined in claim 1 improves the circulation of the air around the filaments, and thus improves the cooling and attenuation of the filaments.
- FIG. 1 shows a spunbonding unit 1 comprising:
- thermoplastic polymer In operation, a thermoplastic polymer, optionally blended with additives, is processed in the extruder 10 in order to obtain a molten polymer. Said molten polymer is pumped by the spinning pump 11 within the duct 12 and through the filter 13, and is fed by the spinning pump 11 to the spinning pack 140 (extrusion die).
- the spinning pack 140 comprises a spinneret plate 140a of longitudinal axis X and having a lot of bilobal spinning orifices 141.
- the spinneret plate 140a comprise for example between 2000 orifices per meter (in the direction of longitudinal axis X), and 6000 orifices per meter. This plate 140 is orientated in such a way that the longitudinal axis X of the plate is perpendicular to the plan of figure 1 .
- the spinneret plate 140a comprises a top surface 140b and a bottom surface 140c.
- a first cavity 141 a For each bilobal spinning orifice 141, a first cavity 141 a, a second cavity 141 c of smaller dimension in cross section, and a transition cavity 141 b connecting the first 141 a and second cavity 141c are drilled in the plate 140a.
- the first cavity 141a has a cylindrical cross section and has a polymer inlet 141d in the top surface 140b of the spinneret plate 140a.
- the second cavity 141c has a bilobal cross section and a polymer outlet 141 (bilobal orifice) in the bottom surface 140c of the spinneret plate 140a.
- the polymer flow is symbolized by arrow P.
- the filtered molten polymer is pushed and forced by the spinning pump 11 through the cylindrical cavity 141a, through the transition portion 141 b and through the second bilobal cavity 141 c of each spinning orifice 141 and forms continuous spun filaments F at the outlet of the spinneret plate 140a.
- the spun continuous filaments F have a bilobal shape corresponding to the shape of the bilobal spinning orifices 141.
- air suction means 15 comprising two suction boxes are provided for sucking the monomers and oligomers (by products) from the spinning pack.
- air quenching means 16 comprising air cooling boxes 16a, 16b, are provided for blowing cold air streams F 1 , F 2 on both sides of the curtain of filaments F.
- Said cold air streams F 1, F 2 are directed towards the curtain of filaments F in a transversal direction ( figure 1 - arrow T) that is substantially parallel to the spinneret plate 140a and perpendicular to the longitudinal axis X of the spinneret plate 140a.
- the filaments F are rapidly cooled by said cold air streams F 1 . F 2 .
- This cooling step is more commonly referred as quenching step.
- the air drawing unit 17 is positioned below the air quenching means 16, and is knowingly used for stretching and attenuating the filaments F trough an attenuating slot 17a, by means of compressed air streams F3 blown towards the filaments F. This attenuation step increases the orientation of the polymer chains and is performed in order to obtain filaments having notably the required strength and count.
- the attenuated filaments F are deposited in a random manner onto the moving belt 18 in order to form a spunbonded web.
- the width of this spunbonded web corresponds to the longitudinal axis (X) of the spinneret plate 140a.
- each bilobal orifice 141 is constituted by two round apertures 141a, 141b that are connected to each other by a straight junction aperture 141c as shown in figure 4 .
- Each bilobal orifice 141 is characterized by a longitudinal central axis A passing through the centre O a , O b of the two aforesaid round portions 141 a, 141 b.
- each bilobal orifice 141 is titled in relation to the transversal direction T (main direction of the air streams F1, F2).
- the angle between direction T and the longitudinal axis A of a bilobal orifice 141 is referred ⁇ .
- the angle between the longitudinal axis X of the spinneret plate 140a and the longitudinal axis A of a bilobal orifice 141 is referred ⁇ .
- ⁇ 90°- ⁇
- angle ⁇ is between 3° and 15°, and preferably between 5° and 10°, which correspond to an angle ⁇ between 87° and 75°, and preferably between 85° and 80°.
- ⁇ is generally equal to 3° and preferably at least equal to 5°
- a better circulation of the air flows between the filaments F is achieved and the cooling of the bilobal filaments is more efficient and more uniform on the whole surface of the filament.
- the attenuation of the filaments F is also improved.
- angle ⁇ is preferably not more than 15°, and even more preferably not more than10°, because for higher values, the surfaces of the bilobal filament in front of the air stream F1 or F2 is in that case too large, and the curtain formed by the filaments F tends to be detrimentally deformed by the air streams (F1, F2).
- angle ⁇ is 7.5°, i.e. angle ⁇ is preferably equal to 82.5°.
- all the bilobal orifices 141 have the same orientation (i.e. angle ⁇ is the same for all the bilobal orifices 141 or otherwise stated the central longitudinal axis A of the bilobal orifices 141 are parallel).
- the values of the angle ⁇ (or ⁇ ) of the bilobal orifices 141 can be different ; preferably, but not necessarily, all angles ⁇ ( or ⁇ ) are however within the range of the invention.
- spinneret plate 140a all the orifices of the spinneret plate 140a are not necessary bilobal, but in another variant the spinneret plate 140a can have bilobal orifices combined with non bilobal orifices (e.g. round orifices, trilobal orifices).
- the bilobal orifices 141 of the spinneret plate 140a are aligned in order to form a plurality of row R i that are substantially parallel to the longitudinal axis X of the spinneret plate 140a.
- the bilobal orifices 141 of two adjacent rows R i of orifices 141 are longitudinally offset to achieve a better circulation of air between the rows R i and thus a better cooling and attenuation of the filaments F.
- the invention is not limited to a spinneret plate 140a for a spunbonding unit, but in reference to figures 6 to 8 the invention can also be used for making a spinneret of a meltblown unit.
- a spinneret for a meltblown unit comprises a die nosepiece 140'a wherein spinning bilobal orifices 141 are drilled.
- the melt blown unit further comprises at least one extruder, a spinning pump, and air blowing means for attenuating the filaments that are extruded from the spinneret ;
- All the bilobal orifices 141 are aligned along axis X of the die nosepiece 140'a ( figure 8 ) and are fed with the polymer through an internal distribution cavity 140'b having a polymer inlet 140'c ( figure 7 ).
- This die nosepiece 140'a is assembled with a block 140'd for forming two lateral air channels 140'e.
- the high velocity and hot air for the attenuation of the filaments is blown in a known way inside these air channels 140'e ( figure 7 / arrow F4).
- each bilobal spinning orifice 141 is tilted in relation to the longitudinal axis X of the spinneret (angle ⁇ ).
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Textile Engineering (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Nonwoven Fabrics (AREA)
Abstract
Description
- The present invention relates to the field of spunbond technology or meltblown technology. In this field, the invention relates to an improved spinneret for manufacturing spunbonded or meltblown nonwovens, said spinneret comprising bilobal spinning orifices.
- Spunbonded nonwoven webs are produced by depositing extruded spun filaments onto a collecting moving belt, preferably a foraminous belt, in a random manner, and by bonding the filaments.
- For spinning the filaments, an extrusion die comprising a plate perforated with a lot of small orifices, and usually referred as spinneret plate, is used. Generally, a spinneret plate comprises more than one hundred spinning orifices per meter. The continuous spun filaments are formed by forcing one or several molten thermoplastic polymers to pass through said small orifices of the spinneret plate. For producing spunbonded nonwoven webs having a large width, only one spinneret plate can be used or several spinneret plates that are placed side by side can be used.
- The shape in cross section of each filament is given by the geometry of the spinning orifice of the spinneret plate through which the filament is being formed. Different shapes of filaments can be produced to date, like for example round filaments, bilobal filaments, trilobal filaments. More particularly, for producing a bilobal filament, also commonly referred as "papillon" filament, a bilobal orifice consisting essentially of two circular apertures connected with one another by a connecting aperture is used. All the spinning orifices of a spinneret plate can have the same geometry, or a spinneret plate can have spinning orifices of different shapes, like for example round orifices combined with bilobal orifices.
- In a spunbond process, before depositing the filaments onto the collecting moving belt, the spun filaments are rapidly cooled by cold air streams that are blown below the spinneret plate (quenching step), and the filaments are then stretched and attenuated by additional blown air streams in order to orient the molecular chains and increase the filament strength.
- The melt blown process is somewhat similar to the spunbond process from an equipment and operator's point of view. The two main differences between a melt blown process and a spunbond process that use air attenuation are: (i) the temperature and volume of air used to attenuate the filaments and (ii) the location where the filament draw or attenuation force is applied. More particularly, in the meltblown process, a high volume air flow at a temperature which is typically equal or slightly greater than the melt temperature of the polymer, is used to attenuate the filaments. In contrast, the spunbond process generally uses a smaller volume of cold air close to ambient temperature to first quench and solidify the filaments and then to attenuate said filaments. Thus in the meltblown process, the draw or attenuation force is applied at the exit of the extrusion die (spinneret) while the polymer is still in the molten state, whereas in the spunbond process, this force is applied at some distance from the spinneret plate, after the polymer has been cooled and solidified (quenching step).
- Another difference between a spunbonding unit and a meltblown unit consists in the structure of the spinneret. More particularly, whereas the spinneret of a spunbonded unit comprises an apertured spinneret plate through which the molten polymer is extruded, in a typical meltblown unit, the spinneret generally comprises a so-called die nosepiece with spinning orifices. There are typically two types of die nosepiece. One type is the capillary type wherein slots are milled into a flat surface and then matched with identical slots milled into a mating surface. The two halves are then matched and carefully aligned to form a row of spinning orifices. The second type is the drilled-hole type wherein spinning orifices are drilled in a single block of metal.
- One main objective of the invention is to improve the spinning of bilobal filaments in a spunbond process or in a meltblown process.
- This objective is achieved by using the spinneret of
claim 1. - According to the invention, the particular orientation of the bilobal spinning orifices as defined in
claim 1 improves the circulation of the air around the filaments, and thus improves the cooling and attenuation of the filaments. - Other characteristics and advantages of the invention will appear more clearly on reading the following description preferred embodiments of the invention, which description is given by way of non-limiting example and is made with reference to the accompanying drawings, in which:
-
Figure 1 is a schematic representation of a spunbonding unit, -
Figure 2 is a top view of a spinneret plate according to the invention, -
Figure 3 is an enlarged view of a part of the spinneret plate offigure 2 , -
Figure 4 is an enlarged view of a bilobal orifice of the spinneret plate offigure 2 or 3 , -
Figure 5 is a view in transversal cross section of the spinneret plate offigure 2 in the region of spinning orifice, -
Figure 6 is a schematic representation in perspective view of a die nosepiece of a spinneret for a melt blown unit, -
Figure 7 is a schematic view in cross section of a part of spinneret of a melt blown unit, comprising the die nosepiece offigure 6 , -
Figure 8 is a bottom view of the die nose piece offigure 7 showing the row of bilobal spinning orifices. -
Figure 1 shows aspunbonding unit 1 comprising: - an
extruder 10, - a
spinning pump 11 connected to the outlet of the extruder via aduct 12 and afilter 13, - a
spinning beam 14 comprising aspinning pack 140 connected to the outlet of thespinning pump 11 and fitted with aspinneret plate 140a, - air suction means 15,
- air quenching means 16,
- an
air drawing unit 17 - a
conveyor belt 18. - In operation, a thermoplastic polymer, optionally blended with additives, is processed in the
extruder 10 in order to obtain a molten polymer. Said molten polymer is pumped by thespinning pump 11 within theduct 12 and through thefilter 13, and is fed by thespinning pump 11 to the spinning pack 140 (extrusion die). - Referring to
figure 2 , thespinning pack 140 comprises aspinneret plate 140a of longitudinal axis X and having a lot ofbilobal spinning orifices 141. Typically, thespinneret plate 140a comprise for example between 2000 orifices per meter (in the direction of longitudinal axis X), and 6000 orifices per meter. Thisplate 140 is orientated in such a way that the longitudinal axis X of the plate is perpendicular to the plan offigure 1 . - Referring to
figure 5 , thespinneret plate 140a comprises atop surface 140b and abottom surface 140c. For eachbilobal spinning orifice 141, afirst cavity 141 a, asecond cavity 141 c of smaller dimension in cross section, and atransition cavity 141 b connecting the first 141 a andsecond cavity 141c are drilled in theplate 140a. Thefirst cavity 141a has a cylindrical cross section and has apolymer inlet 141d in thetop surface 140b of thespinneret plate 140a. Thesecond cavity 141c has a bilobal cross section and a polymer outlet 141 (bilobal orifice) in thebottom surface 140c of thespinneret plate 140a. - In
figure 5 , the polymer flow is symbolized by arrow P. In operation of thespinneret plate 140a, the filtered molten polymer is pushed and forced by thespinning pump 11 through thecylindrical cavity 141a, through thetransition portion 141 b and through the secondbilobal cavity 141 c of eachspinning orifice 141 and forms continuous spun filaments F at the outlet of thespinneret plate 140a. The spun continuous filaments F have a bilobal shape corresponding to the shape of thebilobal spinning orifices 141. - Below the
spinneret plate 140a, air suction means 15 comprising two suction boxes are provided for sucking the monomers and oligomers (by products) from the spinning pack. - Below the suction means 15, air quenching means 16 comprising
air cooling boxes figure 1 - arrow T) that is substantially parallel to thespinneret plate 140a and perpendicular to the longitudinal axis X of thespinneret plate 140a. In operation, the filaments F are rapidly cooled by said cold air streams F1. F2. This cooling step is more commonly referred as quenching step. - The
air drawing unit 17 is positioned below the air quenching means 16, and is knowingly used for stretching and attenuating the filaments F trough anattenuating slot 17a, by means of compressed air streams F3 blown towards the filaments F. This attenuation step increases the orientation of the polymer chains and is performed in order to obtain filaments having notably the required strength and count. - Finally, at the outlet of the
air drawing unit 17, the attenuated filaments F are deposited in a random manner onto the movingbelt 18 in order to form a spunbonded web. The width of this spunbonded web corresponds to the longitudinal axis (X) of thespinneret plate 140a. - Referring to
figures 2 to 4 , eachbilobal orifice 141 is constituted by tworound apertures straight junction aperture 141c as shown infigure 4 . Eachbilobal orifice 141 is characterized by a longitudinal central axis A passing through the centre Oa, Ob of the twoaforesaid round portions - According to the invention, the longitudinal central axis A of each
bilobal orifice 141 is titled in relation to the transversal direction T (main direction of the air streams F1, F2). The angle between direction T and the longitudinal axis A of abilobal orifice 141 is referred β. The angle between the longitudinal axis X of thespinneret plate 140a and the longitudinal axis A of abilobal orifice 141 is referred α. For eachbilobal orifice 141, the relationship between α and β is defined by the following equation: β = 90°- α - According to the invention, for each
bilobal orifice 141, angle β is between 3° and 15°, and preferably between 5° and 10°, which correspond to an angle α between 87° and 75°, and preferably between 85° and 80°. - In the prior art, β is generally equal to zero (i.e. α=90°), which in turn leads to a non uniform cooling of the bilobal filament. By increasing the value of angle β to a value that is at least equal to 3° and preferably at least equal to 5°, a better circulation of the air flows between the filaments F is achieved and the cooling of the bilobal filaments is more efficient and more uniform on the whole surface of the filament. As a result, the attenuation of the filaments F is also improved.
- In return, angle β is preferably not more than 15°, and even more preferably not more than10°, because for higher values, the surfaces of the bilobal filament in front of the air stream F1 or F2 is in that case too large, and the curtain formed by the filaments F tends to be detrimentally deformed by the air streams (F1, F2).
- More particularly, it has been tested that an optimum value for angle β is 7.5°, i.e. angle α is preferably equal to 82.5°.
- Preferably, but not necessarily, as shown on the example of
figure 3 , all thebilobal orifices 141 have the same orientation (i.e. angle α is the same for all thebilobal orifices 141 or otherwise stated the central longitudinal axis A of thebilobal orifices 141 are parallel). In another variant however, the values of the angle α (or β) of thebilobal orifices 141 can be different ; preferably, but not necessarily, all angles α ( or β) are however within the range of the invention. Within the scope of the invention, all the orifices of thespinneret plate 140a are not necessary bilobal, but in another variant thespinneret plate 140a can have bilobal orifices combined with non bilobal orifices (e.g. round orifices, trilobal orifices). - Referring to the particular example of
figure 3 , thebilobal orifices 141 of thespinneret plate 140a are aligned in order to form a plurality of row Ri that are substantially parallel to the longitudinal axis X of thespinneret plate 140a. Preferably, but not necessarily, thebilobal orifices 141 of two adjacent rows Ri oforifices 141 are longitudinally offset to achieve a better circulation of air between the rows Ri and thus a better cooling and attenuation of the filaments F. - The invention is not limited to a
spinneret plate 140a for a spunbonding unit, but in reference tofigures 6 to 8 the invention can also be used for making a spinneret of a meltblown unit. - Referring to
figure 6 and7 , a spinneret for a meltblown unit comprises a die nosepiece 140'a wherein spinningbilobal orifices 141 are drilled. Like the previously described spunbonding unit, the melt blown unit further comprises at least one extruder, a spinning pump, and air blowing means for attenuating the filaments that are extruded from the spinneret ; These technical means are well known in the art and are thus not further described, nor shown on the appended figures. - All the
bilobal orifices 141 are aligned along axis X of the die nosepiece 140'a (figure 8 ) and are fed with the polymer through an internal distribution cavity 140'b having a polymer inlet 140'c (figure 7 ). This die nosepiece 140'a is assembled with ablock 140'd for forming two lateral air channels 140'e. The high velocity and hot air for the attenuation of the filaments is blown in a known way inside these air channels 140'e (figure 7 / arrow F4). - Referring to
figure 8 , and according to the invention, the longitudinal central axis A of eachbilobal spinning orifice 141 is tilted in relation to the longitudinal axis X of the spinneret (angle α).
Claims (8)
- A spinneret (140a; 140'a) for producing a spunbonded or meltblown web, said spinneret having a longitudinal axis (X) that corresponds to the width of the web, and said spinneret comprising bilobal spinning orifices (141) each having a longitudinal central axis (A), characterised in that the angle (α) between the longitudinal axis (X) of the spinneret and the longitudinal central axis (A) of one bilobal spinning orifice (141) is between 75° and 87°.
- The spinneret of claim 1 wherein the angle (α) between the longitudinal axis (X) and the longitudinal central axis (A) of one bilobal spinning orifice (141) is between 80° and 85°.
- The spinneret of claim 2, wherein the said angle (α) is about 82.5°.
- The spinneret of any one of claims 1 to 3, wherein the longitudinal central axes (A) of all the bilobal spinning orifices (141) are parallel.
- The spinneret of any one of claims 1 to 4, wherein the bilobal spinning orifices (141) are arranged in rows (Ri) that are parallel to the longitudinal axis (X) of the spinneret, and the bilobal spinning orifices (141) of two adjacent rows (Ri) are longitudinally offset.
- The spinneret of any one of claims 1 to 5 being an apertured spinneret plate (140a).
- A spunbonding unit comprising at least one extruder (10), a spinning pump (11), a spinneret (140a) and air blowing means (16, 17) for cooling and attenuating the filaments that are extruded from the spinneret, wherein the spinneret (140a) is the one defined in any one of claims 1 to 6.
- A meltblown unit comprising at least one extruder, a spinning pump, a spinneret (140'a), and air blowing means for attenuating the filaments that are extruded from the spinneret, wherein the spinneret (140'a) is the one defined in any one of claims 1 to 6.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE602008004316T DE602008004316D1 (en) | 2008-05-14 | 2008-05-14 | Spinneret with double-lobed spinning openings |
PL08008901T PL2119816T3 (en) | 2008-05-14 | 2008-05-14 | Spinneret comprising bilobal spinning orifices |
AT08008901T ATE494405T1 (en) | 2008-05-14 | 2008-05-14 | SPINNING NOZZLE WITH TWO-LABEL SPINNING OPENINGS |
EP08008901A EP2119816B1 (en) | 2008-05-14 | 2008-05-14 | Spinneret comprising bilobal spinning orifices |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08008901A EP2119816B1 (en) | 2008-05-14 | 2008-05-14 | Spinneret comprising bilobal spinning orifices |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2119816A1 true EP2119816A1 (en) | 2009-11-18 |
EP2119816B1 EP2119816B1 (en) | 2011-01-05 |
Family
ID=39967410
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08008901A Active EP2119816B1 (en) | 2008-05-14 | 2008-05-14 | Spinneret comprising bilobal spinning orifices |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP2119816B1 (en) |
AT (1) | ATE494405T1 (en) |
DE (1) | DE602008004316D1 (en) |
PL (1) | PL2119816T3 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012020053A1 (en) * | 2010-08-12 | 2012-02-16 | Galliano Boscolo | Process and apparatus for spinning fibres and in particular for producing a fibrous-containing nonwoven |
CN103981582A (en) * | 2014-06-04 | 2014-08-13 | 徐伯琴 | T-shaped polyester fiber spinneret plate |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3554854A (en) * | 1962-02-03 | 1971-01-12 | Freudenberg Carl Kg | Non-woven fabric |
US4753834A (en) * | 1985-10-07 | 1988-06-28 | Kimberly-Clark Corporation | Nonwoven web with improved softness |
WO2003014429A1 (en) * | 2001-08-11 | 2003-02-20 | Tencel Limited | Spinneret |
WO2008000354A1 (en) * | 2006-06-29 | 2008-01-03 | Irema-Filter Gmbh | Apparatus for producing a nonwoven fabric using a melt-blowing method |
CN201053042Y (en) * | 2007-06-12 | 2008-04-30 | 上海德福伦化纤有限公司 | Thread spraying plate with cross thread hole |
-
2008
- 2008-05-14 AT AT08008901T patent/ATE494405T1/en not_active IP Right Cessation
- 2008-05-14 DE DE602008004316T patent/DE602008004316D1/en active Active
- 2008-05-14 PL PL08008901T patent/PL2119816T3/en unknown
- 2008-05-14 EP EP08008901A patent/EP2119816B1/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3554854A (en) * | 1962-02-03 | 1971-01-12 | Freudenberg Carl Kg | Non-woven fabric |
US4753834A (en) * | 1985-10-07 | 1988-06-28 | Kimberly-Clark Corporation | Nonwoven web with improved softness |
WO2003014429A1 (en) * | 2001-08-11 | 2003-02-20 | Tencel Limited | Spinneret |
WO2008000354A1 (en) * | 2006-06-29 | 2008-01-03 | Irema-Filter Gmbh | Apparatus for producing a nonwoven fabric using a melt-blowing method |
CN201053042Y (en) * | 2007-06-12 | 2008-04-30 | 上海德福伦化纤有限公司 | Thread spraying plate with cross thread hole |
Non-Patent Citations (1)
Title |
---|
DATABASE WPI Week 200849, Derwent World Patents Index; AN 2008-H60239, XP002504596 * |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012020053A1 (en) * | 2010-08-12 | 2012-02-16 | Galliano Boscolo | Process and apparatus for spinning fibres and in particular for producing a fibrous-containing nonwoven |
CN103210133A (en) * | 2010-08-12 | 2013-07-17 | 波玛工程有限公司 | Process and apparatus for spinning fibres and in particular for producing a fibrous-containing nonwoven |
JP2013536328A (en) * | 2010-08-12 | 2013-09-19 | ボマ エンジニアリング エスアールエル | Method and apparatus for producing fibers, in particular for producing fiber-containing nonwovens |
EP2845936A1 (en) * | 2010-08-12 | 2015-03-11 | Boma Engineering Srl | Process and apparatus for spinning fibres |
RU2602481C2 (en) * | 2010-08-12 | 2016-11-20 | Бома Инжиниринг Срл | Method and device for moulding fibres, in particular, for making fiber-containing non-woven material |
US9617658B2 (en) | 2010-08-12 | 2017-04-11 | Boma Engineering Srl | Apparatus for spinning fibres and producing a fibrous-containing nonwoven |
CN103981582A (en) * | 2014-06-04 | 2014-08-13 | 徐伯琴 | T-shaped polyester fiber spinneret plate |
Also Published As
Publication number | Publication date |
---|---|
PL2119816T3 (en) | 2011-06-30 |
DE602008004316D1 (en) | 2011-02-17 |
EP2119816B1 (en) | 2011-01-05 |
ATE494405T1 (en) | 2011-01-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6800226B1 (en) | Method and device for the production of an essentially continous fine thread | |
DE112005003176B4 (en) | Apparatus for forming meltblown material | |
JP3892057B2 (en) | High speed spinning method and apparatus for composite fibers using high hole surface density spinneret and high speed quenching | |
JPH07102408A (en) | Melt-blow spinneret | |
EP1710329B1 (en) | Process and apparatus for meltspinning and cooling filaments | |
CN1468335A (en) | Process and system for producing multicomponent spunbonded nonwoven fabrics | |
EP2899303A1 (en) | Polyphenylene sulfide composite fiber and non-woven fabric | |
US7160091B2 (en) | Device for the production of multicomponent fibers or filaments, in particular bicomponent fibers or filaments | |
CN113574216A (en) | Spinneret block with easily replaceable nozzles for producing spun fibers | |
WO2006037371A1 (en) | Meltblown method for melt spinning fine non-woven fibres and device for carrying out said method | |
EP2119816B1 (en) | Spinneret comprising bilobal spinning orifices | |
US20050048152A1 (en) | Device for spinning materials forming threads | |
CN104480557A (en) | Chinlon 6 high-strength and fine-denier full-drawn yarns with flattened circular section and preparation method thereof | |
US6660218B2 (en) | Filament draw jet apparatus and process | |
US8186986B2 (en) | Device for drawing filaments | |
US11530494B2 (en) | Spinneret and method for manufacturing fiber web | |
EP1072697A1 (en) | Drawing unit and method | |
KR102478224B1 (en) | Manufacturing method of spinning pack and fiber | |
US10947652B2 (en) | Apparatus for manufacturing non-woven fabric and method of manufacturing non-woven fabric | |
US12054865B2 (en) | Apparatus and process for producing a nonwoven fabric | |
KR20240104851A (en) | Apparatus for spunbond processing | |
JP4063086B2 (en) | Spin pack for rectangular composite spinning | |
JPH09291455A (en) | Production of long-staple web |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR |
|
AX | Request for extension of the european patent |
Extension state: AL BA MK RS |
|
17P | Request for examination filed |
Effective date: 20100112 |
|
AKX | Designation fees paid |
Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MT NL NO PL PT RO SE SI SK TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REF | Corresponds to: |
Ref document number: 602008004316 Country of ref document: DE Date of ref document: 20110217 Kind code of ref document: P |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602008004316 Country of ref document: DE Effective date: 20110217 |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: VDEP Effective date: 20110105 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 |
|
LTIE | Lt: invalidation of european patent or patent extension |
Effective date: 20110105 |
|
REG | Reference to a national code |
Ref country code: PL Ref legal event code: T3 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110406 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110416 Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110405 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110505 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110505 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110405 Ref country code: BE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 |
|
26N | No opposition filed |
Effective date: 20111006 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 Ref country code: MC Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20110531 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602008004316 Country of ref document: DE Effective date: 20111006 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: MM4A |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R081 Ref document number: 602008004316 Country of ref document: DE Owner name: ALBIS INTERNATIONAL S.R.I, IT Free format text: FORMER OWNER: ALBIS SPA, MILANO, IT Effective date: 20120216 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20110514 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20120531 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20120531 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20110514 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20110105 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: 732E Free format text: REGISTERED BETWEEN 20140508 AND 20140514 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: TP Owner name: ALBIS INTERNATIONAL S.R.L., IT Effective date: 20140624 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 9 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 10 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: PLFP Year of fee payment: 11 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20180522 Year of fee payment: 11 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20190514 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20190514 |
|
P01 | Opt-out of the competence of the unified patent court (upc) registered |
Effective date: 20230508 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20240523 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: CZ Payment date: 20240513 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20240521 Year of fee payment: 17 Ref country code: FR Payment date: 20240524 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: PL Payment date: 20240513 Year of fee payment: 17 |