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The DRYTEX® Production Process
DRYTEX® Production Graphic
Tow To Top Production Process
Advantages Of The Dry Spun Technology
DRYTEX® Dry Spinning Versus Wet Diagram
Our DRYTEX® Products
Uses of the DRYTEX® ACRYLIC FIBER
Properties of the DRYTEX® ACRYLIC FIBER

 
   
TOW TO TOP PRODUCTION PROCESS  

Recommendations for the DRYTEX® Tow Breakage Return >>

4.1 Feeding to the breaker

The feeding must be made by choosing the numbered bales in a random way and not in correlative form, in a way that enters fiber of fardos at the beginning, at the middle and at the end of the lot to cause a good homogenization of the package. In case of using 2 tows for the feeding is important that they work in form of a sandwich (one above the other one). The machines of last generation can work with more than 2 TOWS "side to side".

4.2 Parts or zones of work of a BREAKER or CRAQUER (Transformations that experiences the fiber in each one of them).

 

4.2.1 Sleeky Zone the entrance of cables does not have to offer an excessive resistance to the entrance of the first cylinder of the breaker or Craquer machine, with the object of clearing the curling conferred to the TOW. The devices to center and widen must guide the cables, distributing uniformly to the set of filaments to all the wide of the tape, applying a smooth longitudinal uniform tension.

4.2.2 Heating Zone ,is composed by por heating plates , that go placed one above the other. Between both sets an opening of 1 mm generally stays, through where the material passes.

The calibration of heating plates must be made necessarily in such a way that they slightly iron the material so that there is a good and uniform heat transference to the cable. The temperature of plates, the alignment and distance among them, influence in the fiber conferring it the metastable state, (latent or potential shrinking). To greater temperature, greater shrinking.

Normally temperatures between 130 and 1500 Cs are used depending of the machine type because the caloric power, environment, effectiveness of the cooling band of the exit wick, speed of the machine influences in it. Therefore an exact temperature cannot be recommended to obtain a same value of shrinking between 2 machines, even if they are of the same model.

The temperature over 165° C derives a badly operation of the machine. Also, the dirtiness of the plates with the TOW antistatic, will have to be cleaned periodically, otherwise it will influence in such operation ( see cleaning paragraph)

4.2.2.1 Calibration of plates for suitable heat transference, TOW must be always in contact with the heating plates. For this aim it is necessary that the superior and inferior plates must be level out with the transport rollers.

we give like an example, the calibration (leveling) of plates of a Breaker Seydel 870 procedure and is applicable to the other models of this mark. The procedure is the following one:

1. To turn on the switch to close plates (electrical board).
2. To relax chain of superior plate movement (it misadjusts of 2 to per to us of subjection).
3. To turn on the switch to open plates.
4. The superior plate group must be aligned with the ceramic rollers of mall pillows 2 and 3.

In order to verify and to regulate this one alignment, wires of tempered steel of 1 mm of diameter are placed to the ceramic rollers as shown in the drawing (they must have counterbalances in the ends to maintain them tense).

5. The superior plate's bolts became loose and the regulators are adjusted so that the plates are aligned with the wires. The bolts are adjusted.
6. Turn on the switch to close the plates and the superior plate's movement chain has to be set.
7. To verify the correct plate damping, if it's defective change the springs that are necessary.
8. Level inferior plates with the selected gauge (generally 1 mm).

With certain regularity the correct alignment of plates must be checked with a gauge.

4.2.2.2 Enlargements Calibration It is not possible to give an exact calibration of the enlargements for the Rompedoras or Craquers machines by traction due to the variations in the engine power, distances between cylinders, quality of the ceramicados inferior cylinders, covering of the superior cylinders of polyurethane and its pressure. Normally it is used approximately from 17% to 20% between plates to obtain from 18 to 22% of shrinking of a spinning HB. It is not advisable to stretch more than 24% between plates.

4.2.3 Curling Zone: Denominated zone of work curled camera where to the broken cable is curl.

Considering that the curled camera overheats after 15 minutes of operation approximately, it is necessary a visual control, becasuse that it is reason of loss in the intensity of the curling. This disadvantage must be remedied by readjusting the pressure of the curling tongue-piece, watching that the excessive pressure originates defects in the fiber.

Normally the Breakers, at sea level, have a continuous built-in vaporized camera when coming out of zone of curly or crimpado . About that and other forms of vaporization we will deal in point 4.2.

4.2.4 Tape cooling Zone the tape has a relatively high temperature (approx 70° C) after the curling and breakage processes, having therefore to be cooled, without that fact an uncontrolled preshrinking (loss by shrinking) can be originated. This cooling takes place on a perforated conveyor belt through which the air passes. Few curly produces a tape with little cohesion. Lot of Curled "acartona" the fiber doing it's opening more difficult in the following passages

An additional cool tape device of this type can be obtained for all the breaker machines. As an additional precaution measurement we recommended to deposit tapes preferably in perforated aluminum containers. These are better conductors of the residual heat to the surface, diminishing the shrinking potential. The tapes temperature within the containers would not have to exceed 60°C. At the present time perforated teflón boats are also used, which are light and easy to arm.

4.3 The vaporized of the tape at the exit of the Rompedora or Craqueadora

Concluded the passage by the Breaker or Craquer, all the fiber is in a shrinkable state. For the elaboration of the spinnings N type the material must shrink by vaporized.

 

4.3.1 Continuous Vaporized the vaporized at sea level, takes place feeding saturated steam in a temperature of 110°C. It is important that the temperature within the vaporized camera, reaches 101 to 103 °C. The respective control is recommended with a thermometer.

4.3.2 Vaporized in autoclave (OBEM - WELKER) When vaporizing in autoclave it is important to reach constant 110° Cs in each cycle. an example can be the following one:

5 minutes to the emptiness 0,7 - 0,8 Bar
10 minutes of steam 110° C
5 minutes to the emptiness 0,7 - 0,8 Bar
10 minutes of steam 110° C
7 minutes to the emptiness 0,7 - 0,8 Bar Elimination of emptiness and opening of the machine

NOTE. - The tins or boats vaporized must be retired immediately of the camera to avoid the yellowness of the fiber by the temperature that still maintains .

When several boats are vaporized simultaneously, it is important that several loads of the different vaporized ones to diminish any defect between load and load, because they produce different tonalities . It is necessary to control every day the sterilizer with maxima thermometer.

4.3.3 Bell vaporized(LAGARDE - OBEM) after reaching the final emptiness, five steam blows generally occur, leaving the steam off after each operation. The final emptiness gives the necessary dryness to the material. For this procedure a vaporized temperature of 110°C is recommended. Aside from the control of the temperature attention to the quality of the steam will have to be put, also to the vaporized total time (the excess can increase the coloration making the fiber yellow ). Both must be constant, from load to load, to guarantee a uniform coloration of the package.

4.4 General considerations for all the machines:

The curled intensity must be readjusted once the curling machine is hot since variations of curly exist when unevenness of temperature in the curling camera takes place. The amount of curl to apply is made visually and through tests when DRYTEX® Acrylic Fiber works for the first time. The operator must count, in front of his machine, with a tape model with the suitable curl.

The following list will have to be considered:

  • It is important that the fiber at the entrance of the boat or tin and at the exit of the machine does not have more than 60° C because it can cause a reduction in the fiber S (without vaporizing).
  • The continous vaporized must have a pressure of 6 bar approx and then be reduced between 1,4 and 1,8 bar at the entrance of the vaporizer.
  • It is important that the material does not comes humid because in the following process it can cause tangles.
  • It is important to control the good operation of the steam traps.
  • In ANNEXED N° 1 and 2 we indicated some initial regulation calibrations, commonly used according to the machine's mark and model .

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