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WELCOME

PROJECT AT SINTEX

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Page 1: PROJECT AT SINTEX

WELCOME

Page 2: PROJECT AT SINTEX

INTRODUCTION TO MACHINE AND PROCESS OF PROCESSING, FINISHING, YARN DYEING, LAB-DIP DEVELOPMENT DEPARMENTS

UNDER THE GUDLINE and co-operation OF :-Mr. Prasant Maharana

:- Mr. Nilesh sir

:- Mr. Nishith oza

:- Mr. Subhash patel

SUBMITTED BY :- Mr. pradipta Baliarsingh

-college of engineering and technology, Bbsr, Odisha

- [email protected]

Page 3: PROJECT AT SINTEX

CONTENTS:-

SINGEING AND DESIZING MACHINE

BLEACHING MACHINE AND TIPS FOR INSPECTION

MERCERISER MACHINE

DYEING MACHINE AND TIPS FOR INSPECTION

WASHING MACHINE

STENTER

CALENDARING MACHINE

RAISE MACHINE

SHRINKAGE MACHINE

MY SUGGESTION FOR LUBRICATION CARE

YARN DYEING

INTRODUCTION TO LAB DIP-DEVELOPMENT AND MACHINARY

CPB-PROCESS

INTRODUCTION TO REACTIVE DYES

SAMPLE DYED BY DIFFERENT DYES

CONCLUSION

Page 4: PROJECT AT SINTEX

Singeing and Desizing :-

Singeing :- This is a process carried out for the purpose of removing the loose hairy fibrescalled “FUZZ” protruding from the surface of cloth(grey fabric)

Merits:- *smoothness

*even look

*increase lusture

*smoothness

Page 5: PROJECT AT SINTEX

GOLLER SINGEING AND DESIZING M/C:-

Specification :- Singeing burner pressure :- 12mbar

temperature impregnated :- 800c

squeezer pressure :- 3bar

compensator pressure :- 2bar

production speed :- 80m/min

Page 6: PROJECT AT SINTEX

GOLLER CONTINOUS BLEACHING AND SCOURING RANGE:-

Page 7: PROJECT AT SINTEX

GOLLER CONTINOUS BLEACHING AND SCOURING RANGE FLOW PATH:-

Effect

washing

compartment

Thermpalte

heating

VACU-

SET

VACU-

SET

DIP-SAT

PLUS

DIP-SAT

PLIUS

DOSING

SYSTEM

ROLLER

BED

VERTICAL

STEAMER

PASSAGE TO

WASHIG

RANGE

NEUTRALISA

TION

Page 8: PROJECT AT SINTEX

GOLOR CONTINOUS BLEACHING AND SCOURING RANGE SETTINGS:-

SPECIFICATION AND SETTINGS:- production speed :- 50m/min

compensator j box pressure- 1.8 bar

compensator pressure :- 3.8 bar

squeezer jbox:- 2.8 bar

squeezer fx :- 4.8 bar

squeezer :- 2.8 bar

temperature :- 73.40c

Page 9: PROJECT AT SINTEX

CHEMICALS USED IN CBR PROCESS:-

CHEMICALS:- KOH

:-SEQUESTERING AGENT (ELIMINATES HARDNESS OF H2O)

:-INORGANIC POLYPHOSPHATES

:-AMINOCARBOXYLIC ACID

:-ORGANOPHOSPHONIC ACID

:-HYDROCARBOXYLIC ACID

:- BLEACHING AGENT ( NASCENT OXYGEN DECOMPOSES THE COLOURING MATTER INTO SMALLER COMPOUNDS)

:-OXIDISING BLEACHING AGENT ( H2O2)

Page 10: PROJECT AT SINTEX

TIPS for GOLLER CBR MACHINE:-

Continuous visual inspection

for rollers, loose component, gear boxes, motors, pneumatic cylinders, cloth guiders, squeeze covering, greasing at FEED AND DELIVERY PART.

For chemical flow, control boxes, level sensors, pneumatic cylinders, indirect heating, perforated rolls, Acid metering, Squeezers, greasing at washing and impregnation chamber.

for rolls, gear boxes, motors, loose components, pneumatic cylinders, steam nozzle, steaming, steaming quality, roller bed, transportation rolls at reaction chamber

For steam connections, bearings, drives, guide rollers and expanders, greasing at drying range.

Page 11: PROJECT AT SINTEX

Goller merceriser:-

Page 12: PROJECT AT SINTEX

Goller merceriser:-

Mercerising:- swells of the fibre

_ increase the hygroscopic nature

_increase lusture and smoothness

settings:- speed:- 40m/min

_compensator jbox- 2.0 bar

-compensator wc-2.0 bar

-squeezer jbox-1.0 bar

-squeezer m/c-4.0 bar

-squeezer wc-2.0 bar

-reaction time-32 sec

-squeezer fx-4.0bar

Page 13: PROJECT AT SINTEX

Flow chart of merceriser :-

Fabric settled onto the

roller for mercerising

Liquor impregnation in the

penetration passage

through dipping and liquor

feeding into nip

Fabric tension control Thermpalte heating

Effect washing

compartment

Stabilizing compartment neutralisation

Fabric take up

Page 14: PROJECT AT SINTEX

MONFORTEX SHRINKING RANGE:-

Page 15: PROJECT AT SINTEX

MONFORTEX SHRINKING RANGE:-

less energy consumption during compressive shrinking

Now with larger shrink cylinder for longer shrinking paths

Further extended service life of the rubber blanket

Improvement in the residual shrinkage value by up to 4%

Up to 20% higher production speed possible

Automated operator controlled grinding of the rubber belt for greater availability of the ranger and consistently high performance. Up to 80% time saving compared with non-automated grinding

Faster rubber blanket changing with quick change facility

Significantly reduced water consumption upto 40%

Page 16: PROJECT AT SINTEX

MARIO-CROSTA PITCH MACHINE:-

Page 17: PROJECT AT SINTEX

GOLLER PAD STEAM DYEING RANGE:-

Page 18: PROJECT AT SINTEX

GOLLER PAD STREAM MACHINE:-

Dyeing steamer:- ideal steam consumption by proven, maintenance-free and temperature regulated sump heating

Water seal:- even cooling water distribution over the full fabric width

-constant temperature via pc-controlled regulation

Thermoflush:- increase of washing capacity

-Quick energy transfer

-Dissolving of surface impurities

-Core diffusion

effcta washing components :- optimized liquor level and nip washing

-tensionless and crease free fabric transport and tight strand passage

--minimized use of operation agents and reproducibility of finishing results

Page 19: PROJECT AT SINTEX

TIPS FOR GOLLER PAD STEAM DYEING RANGE:-

Regular visual inspection:-

At Roller and cloth guiders(pneumatic pressure should be constant) at fabric feed and delivery part

At color feeding pipe, trough rollers ends shaft with brush bearing, swimming rollers, roller pick up, drive motor greasing, gear box oil level, water line pressure( change hyd. Oil every 6k working hrs), color tank, dosing pump at dye padder.

At vacuum pump water feeding pressure, rubber roller, guider roller bearings at washing component with vacuum system.

At nip roller bearings, greasing, pneumatic cylinder, nip roller pick up, gear box oil level at intermediate squeezer.

at steam pressure, guide roller bearings, temperature indicator, pneumatic cylinders, gear boxes at washing compartment with squeezer.

At drying cylinders, gear boxes and motors, greasing at drying range.

Page 20: PROJECT AT SINTEX

KUSTER CALICO WASHING RANGE:-

Page 21: PROJECT AT SINTEX

KUSTER CALICO WASHING RANGE:-

Product Information :

Under liquor roller vat

Washer

Washer with accumulated fabric

High efficiency squeezer consisting of one S-Roll

Accumulator type washer

Salient Features :

Fully flooded washing machine with suction slot for removal of mechanically attached dirt.

Up and down washers with top squeezing rolls for improved efficiency.

Close rolls for liquid penetration and avoiding creases.

Accumulator type washer for giving time.

Page 22: PROJECT AT SINTEX

KUSTER CALICO WASHING RANGE:-

Merits :

Removal of all soluble deposits from the surface of the fabric.

Traverse and counter current flow of liquid.

Combination of surface and penetration washing of heavy to delicate fabric without creases.

Diffusion of hydrolised colours for complete washing.

Even and maximum squeezing for better efficiency.

Uniform results.

Increase in production.

Large savings in terms of chemicals, energy, water and time.

Less polluting and eco-friendly.

Page 23: PROJECT AT SINTEX

KUSTER WASHING RANGE:-

Settings:- machine speed :- 50 m/min

chemical used :- KOH

Page 24: PROJECT AT SINTEX

BRUECKNER STENTER:-

Page 25: PROJECT AT SINTEX

BRUECKNER STENTER:-

The benefits of the new POWER-FRAME ECO generation

minimum energy consumption due to central heating system with integrated hot gas ducts

possibility of half-zone temperature control, this allows an absolute accuracy in the temperature circuit

clearly increased productivity

fabric transport with extremely low tension

shortest possible fabric paths in the entry area of the line

integrated exhaust air tubing

easily maintainable, integrated heat recovery system on operator level

Page 26: PROJECT AT SINTEX

DHALL SHRINKING RANGE:-

Page 27: PROJECT AT SINTEX

DHALL SHRINKING RANGE:-

Machine speed Up to 100mtr / min. Higher on request

Working width of fabric

600 to 3200mm

Heating media Steam

Steam Consumption 350kgs/hr. for fabric width - 1800mm

Water consumption 250kg/hr for fabric width - 1800mm

Electrical connected load

36 H.P for fabric width 1800mm

Width of machine 4660 mm for fabric width - 1800mm

Height of machine 3580mm

Length of machine 10615mm

Felt calender cylinder 2500mm. 2000mm. 1500mm. 800mm

Page 28: PROJECT AT SINTEX

DHALL SHRINKING RANGE:-

Features :

Feeding of fabric is from trolley.

Steaming cylinder are positively driven with auto on/off valve.

Rubber cylinder is of stainless steel of 610 mm diameter.

Rubber tension & pressure rolls can be motorised on request.

Felt calender main cylinder is jacket of 2000 mm dia with felt drying drum of 1000 mm diameter respectively.

Platter assembly is driven separately by gear motor on two wooden winches provided to draw fabric

Rotor damping system supplied on request.

AC inverter multi motor drive system provided.

Complete Grinding roll assembly provided.

Page 29: PROJECT AT SINTEX

GUOGUANG GROUP CALENDARING MACHINE:-

Page 30: PROJECT AT SINTEX

LUBRICATION TIPS FOR INDUSTRY:-

LUBRICATION HELPS TO OPTIMISE MACHINE UPTIME:- Friction arises during the moving, sliding and rotating parts consume a lot of power. Moreover if friction reaches a critical level the heat generated may fuse the part and causes ultimate damage. It has many purpose of lubrication.

Reduction of friction and water

Extension of fatigue life

Dissipation of frictional heat and cooling

Prevents from corrosion and rusting

TOP LUBRICANTS:-

1- Dupont krytox GPL 227 and Dupont Hitemp T8-27

2- Chemlube 801 & IT-7487

3- Dupont Vydox-6420 R

Page 31: PROJECT AT SINTEX

Yarn dyeing section

MOSTLY YARN USED IN YARN DYEING

Page 32: PROJECT AT SINTEX

Machines used in yarn dyeing section:-

Dying m/cs

Total machine no.- 38 (gofronts,frongs)

Ex:- f127(2),f146(6),f160(3),f1110(3),f1109(4),g1200(1),g1300(1),f1850(1),g1400(2),g1600(2),labwin(8)

Drying m/cs

Hydro extractor (2), RF dryer(2), pressure dryer(1)

Page 33: PROJECT AT SINTEX

Chemical used in yarn dyeing section:-

Amazen dye fix:- dye fixing agent

COntavon gal:- stabilizer( organic chelate from based on hyfroxycarboxylicacid and stabilize to alkali for H2O2 )

H2O2 – Bleaching agent (whitening the yarn)

Heptol KEB:- softening the water

Falosan APF SP2- smoothening the yarn

Barcu soap:- softener

CH3COOH- Ph maintain

Decol:- soaping

Page 34: PROJECT AT SINTEX

YARN DYEING:-

Yarn dyeing is a special type of dyeing process. This dyeing process is slightly difference from woven or knit dyeing. Dyed yarns are used for making stripe knit or woven fabrics or solid dyed yarn fabric or in sweater manufacturing.

Yarn can dye in two form, package or hank form. Flowchart of yarn dyeing can be divided into three stages. Preparatory process, Dyeing and After-treatment process.

Page 35: PROJECT AT SINTEX

YARN DYEING MACHINE:-

Page 36: PROJECT AT SINTEX

YARN DYEING FLOW CHART:-(Preparatory process )

Soft

winding

Batchin

g

Batch

loaded

Demineraliz

ation (50˚C,

20 min;

PH=4.5)

Scouring &

bleaching

(100˚C×40

min.)

Drain

rinse drain

Neutralization

with acid (50°C

×20 min)

Hot Wash

with

peroxide

killer

(60˚C,20

min.)

drain

Page 37: PROJECT AT SINTEX

YARN DYEING FLOW CHART:- (Dyeing)

Leveling agent

& Salt (60° × 20

min; PH=6)

Color

dosing

(60°C×20

min.)

Run

time =

10 min.

(60°C)

Color

migration

(80°C × 20

min.)

Cooling

(60°C)

Level

Check

Soda

dosing

(60°C×30

min.)

Dyeing run

(Dark-60°C×60

min;Medium-

60°C×40

min;Light-

60°C×

30 min)

Dyeing

sample

check

(If Ok)

Drain

Page 38: PROJECT AT SINTEX

YARN DYEING FLOW CHART:- (After-treatment)

Rinse (with

cold Water)

Neutralization

after dyeing

(50°C×20 min.)Drain

Soaping

(Hot

wash)

Drain

Rinse

Add

finishing

chemical(60

°C×20 min)

DrainUnload

Page 39: PROJECT AT SINTEX

LAB-DIP DEVELOPMENT

THIS IS THE DEPARTMENT WHERE THE DESIRED SAMPLE’S(PARTY SAMPLE) SHADE IS MATCHED WITH SOME SAMPLE MADE BY DIFFERENT SHADE TO MATCH THE COLOR WHICH IS TO BE PRODUCED IN MASS.

HERE SAMPLE IS DYED IN DIFFERENT

PROCESS LIKE CPB, PDCPB, REACTIVE PDPS, VAT PDPS ETC.

Page 40: PROJECT AT SINTEX

LAB-DIP DEVELOPMENT MACHINERY:-

Pad stream range model ps-js(rapid) (1)

Rapid horizontal padding mangle (2)

Rapid Padding mangle horizontal P-Ao (1)

Rapid mini dryer (1)

Jeams heal rotary iron (1)

Page 41: PROJECT AT SINTEX

CPB(COLD PAD BATCH) FLOWCHART:-

MAKE 450 ml BY

DISSOLVING DYE IN WATER

50 ml KOH+ silicate

Pad through padding

mangle Batch for 16 hrs

washing

soaping

Neutralization and dry

Page 42: PROJECT AT SINTEX

INTRODUCTION TO REACTIVE DYES:-

REACTIVE DYE:-

As the name implies, these dyes react with cellulose to establish covalent bond, are water soluble.

Dichlorotriazinyl reactive dyes are highly reactive, suitable for exhaust method; cellulose dyed with these will have poor wash fastness because of partial hydrolysis. While monochlorotriazinyl and vinyl sulphone are less reactive, suitable for application of padding and posses good wash fastness(no partial hydrolysis).

Dyes are eco-friendly; full hue as well as shade range exist.

Due to strong fiber-dye interaction, fastness properties are remarkably good except wash fastness.

Reactive dyes have very good light fastness of rating 6.

Reactive dyes have good wash fastness of rating 4-5

Page 43: PROJECT AT SINTEX

GENERALIZATION OF REACTIVE DYES:-

Introduction:-

The general formula of reactive dye can be written as following D-X-Y Here,

D= reactive site

X= Bridge between and reactive site and chromophore

Y= chromogen with water solubilizing group

D-X-Y+ Fiber = Fiber covalent bond.

Reactive basically belong to two classes via 1)substitutive

2)additive

substitutive dyes include mono and dichlorotriazines

additive type include mainly vinyl sulphone dyes(ramazol dyes)

Page 44: PROJECT AT SINTEX

TYPES OF REACTIVE DYES:-

Dichlorotriazine- Two chlorine; so highly reactive

- Nucleophilic substitution mechanism

- Alkali needed to stabilize the phis Na2CO3.

- Temperature required is 400

monochlorotriazine- One chlorine; so less reactive

- Nucleophilic substitution mechanism

- Alkali needed is NaOH.

- Temperature needed is 700 .

vinyl sulphone-Nucleophilic addition mechanism

-

Page 45: PROJECT AT SINTEX

REACTIVE DYES USED AT BVM:-

1:- REACTOBOND GO YELLOW RNL 2:- REACTOBOND YELLOW 4GL

3:- REACTOBOND YELLOW FG 4:- REACTOBOND ORANGE 3R

5:- REACTOBOND T-BLUE G H/C 6:- REACTOBOND T-BLUE G

7:- REACTOBOND VIOLET 5R H/C 8:- REACTOBOND RED RB

9:- REACTOBOND RED 5B 10:- REACTOBOND GO YELLOW RGB

11:- REACTOBOND RED RGB 12:- REACTOBOND NAVY RGB

13:- REACTOBOND GREY RGB 14:- REACTOBOND BLACK RL

15:- REACTOBOND NAVY GG 16:- REACTOBOND YELLOW 3RX

17:- REACTOBOND RED 2GX 18:- REACTOBOND RED TS-3R

19:- REACTOBOND BLUE XL 20:- REACTOBOND OCEAN BR

Page 46: PROJECT AT SINTEX

Trade name Manufacturer CountryRemazol Hoechst GermanyLevafix Bayer GermanyReactone Geigy Switzerland

21:- JAKAZOL VIOLET 5R 22: JAKAZOL BLACK B

23:- JAKAZOL YELLOW HLF 24:- LEVAFIX AMBER CA N

25:- LEVAFIX FAST RED CA 26:- LEVAFIX RED CA N

27:- LEVAFIX BLUE CA 28:- LEVAFIX ORANGE CA

29:- LEVAFIX BR-YELLOW CA 30:- LEVAFIX YELLOW CA

31;- REMAZOL BR.BLUE R 31:- REMAZOL YELLOW RGBN

32:- COROFIX BLACK GDNN

Page 47: PROJECT AT SINTEX

CPB PROCESS:-cpb(cold pad batch ) is of two types.1:- M.O2:- batch

Page 48: PROJECT AT SINTEX

CPB PROCESS SPECIFIACTION:-

SETTINGS OF PADDING MANGLE WHILE PADDING:-

Pressure – 2.4Kg/Cm2

RPM of roller-8.5

QUALITY OF FABRIC TAKEN:- 130*12

For dye fixation – KOH and SILICATE solution

Page 49: PROJECT AT SINTEX

MACHINERY SPECIFIACTION AVAILABLE AT LAB-DIP DEVELOPMENT:-

PAD STEAM RANGE PS-JS:-

roller width-300 mm

diameter- 125mm

dwell time-20-120 sec

temperature- 98-104j

PADDING MANGLE VERTICAL P-Ao:-

roller width-450 mm

diameter- 125mm

pressure load-max 5 kg/cm2

Fixed rpm- 10

MINI DRYER:-

SMAPLE SIZE MAX- 36*42cm

Dwell time 10sec-6min

Electric heating 6kw

Temp-20-2500c with circulating fan

Page 50: PROJECT AT SINTEX

COLD PAD BATCH PROCESS:-

Cold pad batch dyeing method gives you the required fastness standards with ease and minimum costs, and less energy; however dyers have been reluctant to use this method in general because of following reasons given by them:

1- Difficulty of lab. To bulk reproduction.

2- Large space required for batching.

3- Control of temperature during fixation phase.

4- Longer batching time.

5- Long time required to asses correct shade.

Page 51: PROJECT AT SINTEX

SALIENT FEATURES:-

salient features of this method:

Significant cost saving and waste reduction, . as compared to other dyeing methods.

Total elimination of the salt and other specialty chemicals such as anti migrant, leveling agents and fixing agents.

Optimum utilization of dyes which reduces the chemical cost and waste load of effluent.

Excellent wet fastness properties.

This process works at low temperature and low liquor ratio, thus saving energy and water considerably.

A uniform dye quality with even color absorbency and color fastness.

Ease of running small batches.

A high reliability and reproducibility as compared to other continuous methods.

It improves the fabric quality.

It shows added luster, brighter shade.

A soft hand feel and far better penetration of dyes.

Page 52: PROJECT AT SINTEX

SELECTION OF DYES:-- Dye chemistry

Substantively

Reactivity

Diffusion coefficient

Solubility

DYE CHEMISTRY:-

In dye chemistry there are two main factors which govern the dye chemistry of reactive dyes chromospheres and reactivity.

The chromospheres are responsible for the color gamut, light fastness, bleach fastness, solubility, affinity and coefficient of diffusion.

The reactivity is responsible for the application properties such as dye fiber bond stability, efficiency of the reaction with the fiber, affinity and alkali requirements of dyeing

SUBSTANITIVITY:-

Mainly dependent on the nature of chromospheres. A higher substantivity will have low solubility of dyes, high fixation rate, and lower diffusion of coefficient, less sensitive towards temperature, pH and dyeing conditions, high risk of unleveled dyeing. Difficult to remove unfixed dye.

REACTIVITY:-

The reactivity of the dye can be responsible for low and high dyeing time, temperature and pH alteration can modify the reactivity and two dyes of different reactivity can be dyed at the same conditions by adjusting pH and temperature.

DIFFUSION CO-EFFICIENT:-

High diffusion coefficient dyes has better levelling and less dyeing time.

SOLUBILITY:-

Dyes of better solubility can penetrate quickly in the fiber and gives better fixation and leveling, the dye solubility can be increased by increasing temperature, adding urea and reducing electrolytes.

Page 53: PROJECT AT SINTEX

Parameters:-

For cold pad batch dyeing method the foremost thing is the preparation of the fabric which should have following parameters:

• Complete removal of size

• Good singeing

• Very good absorbency through out width and length

• Uniform whiteness

• Crease free

• Relaxed fabric

Page 54: PROJECT AT SINTEX

TYPES OF PRESSURE PADDERS:-

1-Pressure padders:- 2-Finishing padders 3-dyeing padders:-

Page 55: PROJECT AT SINTEX

Points to be taken care:-

The Most Important Factors Of Cold Pad Batch Dyeing

Suitable Fabric Humidity

The Temperature Of Fabric Before Cooling Padders

The Temperature Of Fabric Before Trough Entrance

The Temperature Of Fabric At The End Of Trough After Dyeing

The Temperature Of Fabric At The Entrance Of Washing After Waiting (Rotation)

Page 56: PROJECT AT SINTEX

Settings:-

Dye Bath Temperature :-

The temperature of the dye bath to be dyed and the temperature of trough must be supplied to be equal (20-25 ºC desired)

Pick-Up :-

The rate of pick up in sample of padder and the rate of pick up while manufacturing in bulk must be equal (The ideal pick-up is 50-60 %)

The Time Of Diving :-

The time of fabric diving into dyeing trough and dyeing diving in manufacture must be same. (2-4 seconds is desired in the time of diving)

The Time Of Waiting :-

The time of waiting of dyed fabric must be 16 hrs. but it is not always same. It mainly depends on dye used.

The Temperature Of Waiting :-

The waiting temperature of sample dye must be equal with the dyed fabric in manufacture. The sample to be waited has been cared to be winded with plastics.

(Desired waiting temperature is 20- 25 °C)

The batch should rotate not more than 40 rpm.

Temperature of the fabric , dye bath and the batching atmosphere should not be more than 35 C

Page 57: PROJECT AT SINTEX

PAD DRY RANGE CHAMBER SETTINGS:-

REACTIVE DYE:- CHAMBER 1:-

TEMPERATURE:- 400C

MEDIUM:- H20

CHAMBER 2:-

TEMPERATURE:- 600C

MEDIUM:- H202

CHAMBER 3:-

TEMPERATURE:- 450C

MEDIUM:- 2GPL DECOL

CHAMBER 4:-

MEDIUM:- 2GPL CH3COOH

WASH

VAT DYE:- CHAMBER 1:-

TEMPERATURE:- 400C

MEDIUM:- H20

CHAMBER 2:-

TEMPERATURE:- 600C

MEDIUM:- H202

CHAMBER 3:-

TEMPERATURE:- 450C

MEDIUM:- 2GPL DECOL

CHAMBER 4:-

MEDIUM:- 2GPL CH3COOH

WASH

Page 58: PROJECT AT SINTEX

SAMPLES DYED BY REACTOBOND GO YELLOW RNL :-SAMPLE NO. DYE PERCENTAGE (in gpl) DYE WEIGHT

1 0.1 0.05

2 0.5 0.25

3 1.00 0.50

4 1.50 0.75

5 2.00 1.00

6 3.00 1.50

7 5.00 2.50

8 10.00 5.00

9 20.00 10.00

10 30.00 15.00

11 40.00 20.00

12 50.00 25.00

13 60.00 30.00

14 70.00 35.00

15 80.00 40.00

Page 59: PROJECT AT SINTEX

SAMPLES DYED BY REACTOBOND VIOLET 5R H/C:-

SAMPPLE NO. DYE PERCENTAGE (in gpl) DYE WEIGHT

1 0.1 0.05

2 0.5 0.25

3 1.00 0.50

4 1.50 0.75

5 2.00 1.00

6 3.00 1.50

7 5.00 2.50

8 10.00 5.00

9 20.00 10.00

10 30.00 15.00

11 40.00 20.00

12 50.00 25.00

13 60.00 30.00

Page 60: PROJECT AT SINTEX

SAMPLES DYED LEVAFIX BLUE CA:-

SAMPPLE NO. DYE PERCENTAGE (in gpl) DYE WEIGHT

1 0.1 0.05

2 0.5 0.25

3 1.00 0.50

4 1.50 0.75

5 2.00 1.00

6 3.00 1.50

7 5.00 2.50

8 10.00 5.00

9 20.00 10.00

10 30.00 15.00

11 40.00 20.00

12 50.00 25.00

13 60.00 30.00

Page 61: PROJECT AT SINTEX

SAMPLES DYED BY REACTOBOND YELLOW 3RX AND REACTOBOND RED 2GX:-

SAMPPLE NO. DYE PERCENTAGE (in gpl)

YELLOW DYEWEIGHT(IN GM)

RED DYE WEIGHT(INGM)

1 0.1 0.022 0.28

2 0.5 0.12 0.130

3 1.00 0.24 0.261

4 1.50 0.354 0.40

5 2.00 0.55 0.45

6 3.00 0.70 0.80

7 5.00 1.38 1.1

8 10.00 2.6 2.38

9 20.00 5.05 4.95

10 30.00 7.20 7.86

11 40.00 10.5 9.5

12 50.00 12.85 12.15

13 60.00 14.98 15.02

Page 62: PROJECT AT SINTEX

CONCLUSION:-

I am very much happy by doing training program and my project work at this evolving textile division BHARAT VIJAY MILLS of SINTEX LTD. It was a real honor and advantageous period for me.

I learn so many industrial things and gain so many immortal experience which is beyond the bookish knowledge.

I like the work culture, company atmosphere, upward and downward communication in company and the support of every employee I have ever came across during training period.

I don’t know it will be helpful to this company which I suggest to look into the lubrication of processing machinery at regular interval. I know it wont increase the production rate but it will increase the machine efficiency and increase the running time of the machine which is really a cost saving thing. I wish the company will focus on this field and take necessary steps .

At last I want to Thank you all my mentors and supporting hands from SINTEX LTD. And looking forward for a positive relationship with this company in future.

Page 63: PROJECT AT SINTEX