28 Apr 2013

PROCESS PARAMETERS IN BLOW ROOM


PROCESS PARAMETERS IN BLOW ROOM
BASIC FUNCTIONS OF BLOW ROOM
1.Opening & Cleaning
2.Mixing or Bleanding
3.Micro dust removal
4.Uniform feed to the Carding
5.Recycling of waste
The larger the dirt particle , the better they can be removed

Since almost every blowroom machine can shatter particles, as far as possible a lot of impurities should be eliminated at the start of the process.Opening should be followed immediately by cleaning, if possible in the same machine.
The higher the degree of opening, the higher the degree of cleaning. A very high cleaning effect is

almost always purchased at the cost of a high fibre loss. Higher roller speeds give a better cleaning effect but also more stress on the fibre.
Cleaning is made more difficult if the impurities of dirty cotton are distributed through a larger quantity of material by mxing with clean cotton.

The cleaning efficiency is strongly dependent on the TRASH %. It is also affected by the size of the particle and stickyness of cotton. Therefore cleaning efficiency can be different for different cottons with the same trash %. There is a new concept called CLEANING RESISTANCE. Different cottons have different cleaning resistance.

If cotton is opened well in the opening process, cleaning becomes easier because opened cotton has more surface area, therefore cleaning is more efficient

If automatic bale opener is used, the tuft size should be as small as possible and the machine stop time should be reduced to the minimum level possible
If Manual Bale openers are used, the tuft size fed to the feed lattice should be as small as possible

Due to machine harvesting , cotton contains more and more impurities, which furthermore are shattered by hard ginning. Therefore cleaning is always an important basic operation.

In cleaning, it is necessary to release the adhesion of the impurities to the fibres and to give hte particles an opportunity to separate from the stock. The former is achieved mostly by picking of flocks, the latter is achieved by leading the flocks over a grid.
Using Inclined spiked lattice for opening cotton in the intial stages is always a better way of

opening the cotton with minimum damages. Ofcourse the production is less with such type of machines
But one should bear in mind that if material is recyled more in the lattice, neps may increase. Traditional methods use more number of machines to open and clean natural fibres.

Mechanical action on fibres causes some deterioration on yarn quality, particularly in terms of neps . Moreover it is true that the staple length of cotton can be significantly shortened .

Intensive opening in the initial machines like Bale breaker and blending machines means that shorter overall cleaning lines are adequate.
In a beating operation, the flocks are subjected to a sudden strong blow. The inertia of the impurities

accelerated to a high speed, is substantially greater than that of the opened flocks due to the low air resistance of the impurities. The latter are hurled against the grid and because of their small size, pass between the grid bars into the waste box, while the flocks continue around the periphery of the rotating beater.

By using a much shorter machine sequence, fibres with better elastic properties and improved spinnability can be produced.
Air streams are often used in the latest machine sequence, to separate fibres from trash particles by buoyancy differences rather than beating the material against a series of grid bars.
There are three types of feeding apparatus in the blowroom opening machines two feed rollers( clamped)

 
Two feed roller arrangements gives the best forwarding motion, but unfortunately results in greatest

clamping distance between the cylinders and the beating element feed roller and pedal arrangement gives secure clamping throughout the width and a small clamping distance, which is very critical for an opening machine In a feed roller and table arrangement, the clamping distance can be made very small. This gives intensive opening, but clamping over the whole width is poor, because the roller presses only on the highest points of the web.
Thin places in the web can be dragged out of hte web as a clump by the beaters

Honeydew(sugar) or stickiness in cotton affect the process very badly. Beacause of that production and quality is affected. Particles stick to metal surfaces, and it gets aggreavated with heat and pressure
These deposits change the surface characteristics which directly affects the quality and running behavior.
There are chemicals which can be sprayed to split up the sugar drops to achieve better distribution. But this system should use water solutions which is not recommended due to various reasons.

It is better to control the climate inside the department when sticky cotton is used. Low temperature

( around 22 degree Celsius) and low humidity (45% RH). This requires an expensive air conditioning set up.
easiest way to process sticky cotton is to mix with good cotton and to process through two blending machines with 6 and 8 doublings and to install machines which will seggregate a heavier particles by buoyancy differences.

General factors which affect the degree of opening , cleaning and fibre loss are
1.Thickness of feed web
2.Densitiy of the feed web
3.Fibre coherence
4.Fibre allignment
5.Speed of openers
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17 Apr 2013

SIMPLE WAYS TO IMPROVE CSP IN YARN



                       IMPROVEMENT OF YARN CSP
               MILL AUTHORITIES WILLING TO IMPROVE AROUND 2300CSP

                               BEFORE
                           AFTER
          COUNT
       STRENGTH
        COUNT
      SRRENGTH
           39.1
          1582
39.4
           2234
                                  
                                       INPUT MATERIAL;28.90MM
M/C
MBO
STEP
MONO
SCUTCHER
TOTAL
Len
%
Len
%
Len
%
Len
%
         %
BEFOR
28.13
2.66
27.20
3.3
26.67
1.88
26.50
0.71
           8.30
AFTER
28.81
0.31
28.64
0.59
28.58
0.21
28.38
0.71
          1.80
IMP %
          88.35
       82.12
         88.83
       -nil-
          86.33
                         

               SPEEDS CHANGES TO REDUCE FIBRE RUPTURE
SNo
   MBO
  STEP
   MONO
                 SCUTCHER
SPD   (Rpm)
SPD   (Rpm)
SPD    (Rpm)
B.SPD(Rpm)
F.SPD(Rpm)

RATIO
Before
750
700
900
600
1500
2.5
After
400
450
500
800
1200
1.5

In MBO below this 400Rpm there is no reduction in fibre rupture but opening of the material getting poor.
v In step cleaner speed reduction as well as Buffalow plate setting reduced from 10MM to 5MM. Because fibre tranport from one to other beater poor.
v In Scutcher, speed of beater increased to reduce waste, because insufficient opening leads to more lint loss
v Beater to fan speed ratio found too high,so it was reduced 2.50 to 1.50
          
        
     FIBRE RUPTURE CONTROL DETAILS IN CARDING

                       FIBRE RUPTURE IN CARDING (BEFORE)

                        SPEEDS
    LENGTH
Mc
Cly Spd
Lic Spd
Ratio
Doff Spd
Ratio
Input
Output
Rupture%
M/C 1
340
1100
1.6
30
21.4
28.38
27.3
3.8
M/C 2
340
1100
1.6
27
23.8
28.38
27.52
3.03
                    
                     FIBRE RUPTURE IN CARDING  (AFTER)

                        SPEEDS
    LENGTH
Mc
Cly Spd
Lic Spd
Ratio
Doff Spd
Ratio
Input
Output
Rupture%
M/C 1
340
800
2.12
30
21.4
28.38
27.87
1.52
M/C 2
340
800
2.12
30
21.4
28.38
27.85
1.59
  FIBRE RUPTURE IN CARDING  (BEFORE AND AFTER FEEDPLATE STG)
MC
                  BEFORE
            AFTER
STG
INPUT
OUTPUT
RUPTURE%
STG
INPUT
OUTPUT
RUPT%
1
0.50
28.38
27.87
1.52
0.80
28.38
28.10
0.71
2
0.50
27.85
27.85
1.59
0.80
28.38
28.12
0.64


                                       Count,strength% CSP details
SNO
           BEFORE
         AFTER
1.   
41.3
38.7
1598
40.7
50.8
2067
2.   
42.7
40.2
1716
39.8
60.3
2400
3.   
36.4
34.3
1248
37.8
62.5
2362
4.   
36.4
39.8
1448
36.8
57.5
2116
5.   
36.8
43.5
1600
36.8
49.8
1833
6.   
36.8
40.3
1483
38.6
66.3
2559
7.   
38.3
41.7
1597
41.4
55.7
2306
8.   
40.3
29.5
1189
40.8
51.8
2113
9.   
41.4
37.4
1548
35.7
63.6
2271
10.            
42.3
39.3
1662
39.2
57.3
2246
11.            
37.5
50.1
1878
37.8
65.7
2483
12.            
39.7
44.1
1751
43.2
39.7
1750
13.            
41.0
33.5
1373
36.9
70.2
2590
14.            
38.2
46.7
1784
38.3
59.7
2287
15.            
40.3
43.7
1761
39.5
61.8
2441
16.            
39.5
43.5
1718
41.3
53.8
2238
17.            
40.2
30.8
1238
40.7
50.3
2047
18.            
44.3
37.9
1679
39.3
60.2
2366
19.            
35.8
65.3
2338
42.1
57.3
2412
20.            
37.3
40.8
1522
37.3
58.5
2182
21.            
36.5
43.7
1595
41.5
53.7
2229
22.            
39.3
39.8
1564
39.8
55.8
2280
23.            
37.3
37.9
1413
43.0
63.1
2713
24.            
40.3
39.6
1595
36.8
57.6
2120
25.            
43.2
35.9
1550
37.9
50.2
1903
26.            
40.1
33.2
1331
40.1
55.7
2234
27.            
39.2
39.8
1560
39.8
57.3
2281
28.            
36.6
40.3
1475
37.6
60.8
2286
29.            
35.7
37.8
1349
40.3
50.3
2027
30.            
38.3
49.6
1900
41.2
49.2
2027
A.Ct
                    39.10
                         39.41
A.Stn






A.CSP
                     1582
                          2234

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