Tuesday, May 11, 2021

Blow room lecture # 4, Blow Room Machine , unifloc A-11, unifloc B-11,

 Blow Room Machine

    UNIFLOC A 11

    Overview of proceeding process

  • The control of the bale laydown directly affects the performance of the UNIfloc. The number of assortments determines the maximum production rate.


  •  The positioning of bales should be performed to obtain consistent mixing and, ultimately, blending of the fibers
  •  The waste bales and bales of unusual color should be carefully located so as to avoid an undue influence on the consistency of the blend.
  • Wherever possible mix the bale location in the laydown:
  •  Regions of origin should not be separated.
  • Fiber properties should be averaged in mini-blends.
  •  Fiber appearance can indicate troublesome cotton.
  •  The presence of sticky cotton quickly contaminates the equipment. Care should be taken to control the number of sticky bales in the laydown

    Principal features

 The UNIfloc is a unique machine designed to remove small tufts of fiber from the top of bales in preparation for optimal cleaning, mixing and blending. The principal features are:

  •   Production up to 1400 kg/hr with the 2300 mm wide frame feeding from a single laydown.
  • Production up to 950 kg/hr with the 1700 mm wide frame.
  •  Laydown length up to 50 m.
  •  Up to 130-bales/ laydown on each side
  •  A laydown “run-in run-out” program to automatically compensate for variations in bale density from top to bottom by adjusting “take off step depth” to maintain a constant production rate.
  •  A laydown transition program automatically swivels the tower to remove fibers from the new bales during the run-out phase of the old bales (bottom 50 cm).
  • i.e. several cycles of - 8 passes on the old bales and 2 passes from the new laydown
  • Minimum of 18 bales when feeding cotton or 12 bales of man made fibers are required for satisfactory mixing.


    Air requirements

  •   Transport air from the UNIfloc: 0.85 1.20 m3/sec
  •  Suction in the pipe:   400 Pa (300 mm water)

    Undesirable practices:

  •   Go/stop ratio - Too low. - Production rate and fiber quality affected
  •  Laying bale parts on top of the new laydown. - Creates chokes and loss of blend control.
  •  Incorrect location of waste bales. Waste bales should not be concentrated in one area or located at the end of the laydown.
  •  Inadequate bale blooming time and the variation in blooming time between bales.
  • Warning: Spiral pipes should not be used for fiber transportation because of excessive swirling and fiber entanglement.
  •  Where fiber passes through a fan, be sure that a “material-handling fan” is used.

Where fiber is transported from one building to another it is necessary to insulate the pipes in cold climates, to prevent condensation in the pipes, which causes fiber chokes.

 

   Start up suggestions

 The production rate of the UNIfloc should meet the needs of the blowroom. It is very important to balance the delivery rate with the needs of the rest of the line. The effective running time or GO / STOP ratio should be 85% to 90%.

 A starting guideline is to use the basic default values and then adjust the settings to optimize the degree of fiber opening and the production rate.

 There are four settings that can be adjusted:

    Take Off Roll penetration Controls tuft size.

 For cotton bales normal settings are:

  •  2 mm for low production rates with soft bales,
  •  3 mm for low production rates with hard bales,
  •  3 mm for high production rates with soft bales, and
  •  4 mm for high production rates with hard bales.

 For bales of man made fibers normal settings are 0 to 2 mm.

   Arm lowering steps

                   Illustration of Roll Penetration



Controls the production rate and is automatically varied during the run-in / run-out program which has to programmed depending upon the variation of bale density. 

 

A guide line of step depths / production rates for the middle portion of cotton bales is:

 

 1 mm for 200 to 350 Kg/hr

 2 mm for 350 to 600 Kg/hr

 3 mm for 600 to 900 Kg/hr

 4 mm for 800 to 1200 Kg/hr

 5 mm for 1000 to 1500 Kg/hr

    Arm traverse speed

Illustration of the variation in step depth during the run-in / run-out program

 

The traveling speed of the arm affects the production speed. Care has to be taken to avoid overloading the opening rollers, which can cause unopened fiber to be fed resulting in chokes in the transportation system.

Normal traverse speeds are between 9.5 and 10 m/min.

 

 

   Take off roller speed

 

The take off roller speed can be adjusted to feed smaller tufts, but care has to be taken to ensure that neps are not created or the tufts are not too small. When the tufts are too small the material is too bulky and is difficult to transport without choking in the pipes.

 

1500 rpm is normal for cotton

1300 rpm is normal for man-made fibers

 

Suggested set up steps to increase the production rate for cotton.


 

Progressive production increase

Traverse speed

9.5 m/min

9.5 m/min

10.5 m/min

10.5 m/min

11 m/min

11 m/min

Roller speed

1600

1600

1600

1600

1600

1600

Roller penetration

3 mm

3 mm

3 mm

3 mm

3 mm

4 mm

Arm step depth

3 mm

4 mm

4 mm

5 mm

5 mm

5 mm

  

Trouble shooting 

   Production rate too low: 


Check and adjust if necessary.

•  Arm lowering step distance – too low

•  Take-off roll protrusion - too low

•  Traverse speed - too low.

•  Run-in / run-out not optimized

•  Excessive assortments or tower swings.

•  Change of material, particularly bulky man made fibers such as acrylics.

 

   Chokes in the fiber transport line:

 

§       Remove loose fiber from the tops of the laydown and pack it between the bales.

§       Check the air speed in the different points in the line.

§       Check the condition of pipes. Seams, joints, surfaces and bends can cause fiber chokes.

§       Check the condition of the fan inside the UNIfloc. All material, including trash, pass through this fan.

§       Ensure correct fan speeds.

§       Reduce the penetration of the take-off roll.

§     If chokes occur after the fiber has passed from one building to another, check to see if condensation is occurring in the pipes between the buildings. Insulation may be necessary in cold climates.

 

   Excessive neps in the opened material:

 

§       Check the airflow from the UNIfloc. Insufficient airflow can cause an increase in the nep level.

§       Check nep levels throughout the system to determine where the change in nep level occurs.

§       Throughout the laydown and look for problematic bales,

§       Take several samples immediately after the UNIfloc,

§       Take several samples at the entry to the machine following the UNIfloc.

§     Check the condition of the teeth on the take-off roll. If damaged they should be replaced. If worn or rounded they should be replaced or sharpened if the replacement parts are not available.

§       Reduce the take-off roll speed.

 

   Trash in the opened material is too high:

 

§       Check the go/stop ratio and correct if not close to 85%.

§       Increase take-off roll speed to reduce tuft size.*

§       Reduce the penetration of the take-off roll to reduce tuft size.*

§       Reduce traverse speed.

Note: Some of the above actions may reduce the production rate. Production rate of the UNIfloc should be checked for several shifts. One check is not enough.


 ..................................................

 

   UNICLEAN B-11

     General Information

 The UNIclean is an outgrowth of Reiter’s experience in removing trash from cotton while it is airborne as the first cleaning point in the blowroom and is consistent with the cleaning philosophy:


 

  •  a minimum number of cleaning positions
  •  maximum working efficiency
  •  optimum fiber preservation
  •  high raw material yield

 

Removal of foreign matter during the first cleaning stage in the blowroom.

   UNIclean B 11

   Principal Features

  Production up to 1'200 kg/h (2'600 lbs/hr)

  • Selective trash removal
  •  High dedusting effect
  •  Gentle fiber treatment
  •  VarioSet for easy operation
  • Change waste amount in a range of 1:10

  

   Mode of operation

 In contrast to conventional pre-cleaners, i.e. single-cylinder cleaners or horizontal cleaners, material transport inside the UNIclean takes place mechanically by means of special pins, independently of the conveying air. The raw material is forced over the cleaning grid bars where trash is removed and an integrated de-dusting unit to remove fine particles.

The waste is collected inside the machine and is automatically released to the waste suction system.

Since dust and sand cause considerable problems in the spinning operations, the UNIclean has been equipped with an integrated dedusting unit. Dust, sand, some pepper trash and fiber fragments are separated from the cotton by a perforated plate and released to the filter system. Only some 0.5 cubic m/s of dust laden exhaust air has to be removed in the dedusting function.

 


To control the cleaning action of the UNIclean both the “cleaning intensity” and the “waste rate” have to be programmed into the machine. The cleaning intensity controls both the speed of the drum and a compensatory setting of the grid bars. Increasing the “cleaning intensity” increases the trash removal. The “waste rate” changes the grid angle to remove more or less material. These setting are made on the machine control panel or in the VarioSet program if it is available.

 

   Fiber transportation

 The material is blown to the UNIclean, and is circulated seven times inside the machine by the tines on the drum. The cleaned fiber is sucked from the machine by the transportation fan. Careful adjustment of the airflow is essential to the effective operation of the machine.

Part of the feed transport air is sucked through the perforated plate by the dust waste fan. Fine particles are removed and discharged to the filter system.

The quantity of air required to transport the fiber to the next machine exceeds that amount passing through the machine.

To minimize the volume of air passing through the machine, a supplementary air inlet is provided to allow extra air to be sucked into the system as needed.

 

   Cleaning process

 As the fibers enter the machine they are carried in a circular motion by the tines.

The fibers are directed by the guide plates to make seven revolutions before leaving the machine. In each revolution the fibers pass the grid bars and the perforated plate.

The “Cleaning Intensity” can be adjusted step-less, to changing the rotational speed of the drum. The adjustment can be done while the machine is running. Additionally, the angle of the grid bars is automatically changed in combination with the speed.

The “Waste rate” can be varied by changing the grid bar angle with an electrically controlled cylinder. The settings of the cleaning intensity and waste rate can be recalled and used again at a later date.


    Cleaning intensity

 

Production

Setting

Drum speed

 

Up to 1'200 kg/h

0.0 (low)

480 rpm

Step-less adjustment to

1.0 (high)

960 rpm

 

   Relative waste rate
Setting «1» (Low):                                                 Setting «10» (High):

 

Grid closed, lowest waste rate                                          Grid open, highest waste rate

dark waste composition                                                 light-colored waste composition

 

 

   Cleaning characteristic diagram

 

The typical amount of waste to be removed by varying the settings is shown in the following chart. The influence of the cleaning intensity setting increases as the waste rate is increased.


 

As a guideline, the following table gives values of the cleaning intensity and the waste rate according to the trash content of the cotton to be cleaned.

 

Trash in cotton

Applications

Cleaning intensity

Waste rate

0.5 to 2,0 %

Clean cotton fine combed yarns

0.5 to 0.9

0.5 0.8 %

1.0 to 3.5%

Ring spun carded yarns

0.6 to 0.9

0.8 1.5 %

1.5 to 4.5%

Rotor yarns

Ne 10/1 to 24/1

0.7 to 0.9

1.0 2.0 %

3.0 to 6.0% and

more

Rotor yarns

coarse counts

0.2 to 0.7

1.5 4.0 %

 

 

   Waste disposal

 

The waste is removed periodically through the airlock roller. The interval is determined by the waste transport system. The waste extraction roll incorporates an airlock, which seals the waste chamber to prevent

     Determining the amount of waste

 o determine the amount of waste extracted, the waste has to be removed by hand, weighed and compared with the production rate to calculate waste %.

 

Follow the instructions on how to isolate the trash chamber from the suction system and manually operate the air lock roller to remove the trash

Take at least three (3) tests, each of at least half an hour.

(For a provisional test, collect the waste for more than one complete cycle of the UNIfloc.) Record the running time of each test.

 

 

Calculate the production (kg) during the test time =

Carding production rate from the line kg/h x test time in min 60

Waste % = Amount of waste removed x 100 ÷ Production during test + waste

 Note:

The system should be operating with an acceptable stop/go ratio otherwise when the system is optimized the actual waste % will vary from the tested value.

Stop/go ratio =  Running time of the UNIfloc (operating hours counter)

Actual time


 

   Trouble shooting

  Neps too high in the material downstream

 Neps can be created at many points. Carefully check the nep levels throughout the system.

  • Immediately after the UNIfloc.
  •  At the entry to the UNIclean.
  •  At the exit of the UNIclean
  • At the entry to the UNImix.

 

  • Check and correct the volume and speed of the airflow in the system.
  •  Check the condition of the fans
  •  Frequently a nep increase occurs in the transportation pipes because of,
  •  Rough pipe surfaces,
  •  Tagging and roping,
  •  Rolling of stock,
  •  Bad joints

     Trash too high after the UNIclean

  •      First check the cleaning effectiveness of the UNIclean. Normal levels depend upon the type of cotton and the amount of trash in the cotton.
  •    Check and correct the stop/go ratio of the UNIfloc. If it is too low then the instantaneous fiber flow rate through the UNIclean will be too high.
  •     Adjust the cleaning settings of the UNIclean.
  •    Check to see if there is trash being pulled back from the waste chamber through the grid bars and into the cotton. If so correct, 1) the airflow through the UNIclean or, 2) the trash extraction system.
  •    Check the bale laydown to see if there is a grouping of bales with a high level of trash or waste. This produces surges of material with high trash content that can appear to be a problem with the UNIclean. Distribute the bales throughout the laydown.

 

   Blockages in the system
  •  Incorrect airflow in the system check air speed and volume.
  • A backpressure from the UNImix can occur if it is too full.
  •  Check the air pressure switch on the UNIfloc.
  •  Check the condition of the fiber transport fans, they could be loaded, damaged or not running at the correct speed.
  •  Be sure that the fan belts are in good order and tight.
  •  The air opening for the supplementary air may not be set correctly and allowing excessive false air into the pipes.

  •  The pipes may be damaged or contaminated causing the fibers to stick and choke. Long transportation distances and/or multiple pipe bends are problematic.
  •  Check the stop/go ratio of the UNIfloc. If it is too low, then the actual material flow rate can overload the system and cause chokes. It is important to maintain a ratio of 85 to 90%
  •  Check the performance and settings of the UNIfloc to be sure that it is not over feeding un-opened, large pieces, of cotton from soft bales or bale tops.

     Waste not being removed from the trash chamber

 The waste extraction roll does not turn, the drive system may be jammed,

  •  The control from the filter system may be out of order,
  • The filter may be overloaded and a back pressure built up,
  •  Waste exhaust fan may not be operating correctly.
  •  Note: If a damaged waste extraction roll has to be replaced: the plant must continue to operate without one, using continuous waste removal, it is necessary to close the grid bars to prevent excessive fiber being pulled out with the waste. This is only a temporary measure.


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