SlideShare a Scribd company logo
1 of 24
PRESENTED BY: 
SUBHASISH DAS 
Management Trainee 
Fisher College Of Business ( Indian Programme)
OBJECTIVE 
PROCESS OPTIMIZATION OF CED 
PASTE SECTION
PHASE 1 
EVALUATE PRESENT PRODUCTION CAPACITY 
 PRODUCT MIX: 
 (ACP 675-60%,ACP 610 BLACK-20%,ACP 611 GREY- 
20%) 
 NO. OF WORKING DAYS: 
25 
 NO. OF SHIFTS AVAILABLE EACH MONTH 
75 
 OPERATION TIME PER SHIFT 
370 MINS
PROCESS FLOW CHART 
CHARGING 
HSD 
DISPERSING 
GRINDING ( 
HSD-PM-HSD) 
DISCHARGI 
NG 
SAMPLING 
/ADJUSTM 
ENT/QA 
FILTERATION PACKING
CHARGING 
 CARRIED OUT AT HSD LEVEL(1ST FLOOR) 
LIQUID CHARGING: (90-150 MINS) 
 REQUIRES ADDITIONAL MAN POWER 
 THE HSD HOOD IS RAISED TO POUR THE RAW 
MATERIAL DIRECTLY BUT WITH FREQUENT WEIGHT 
MEASURE MENT 
POWDER CHARGING: (45-90 MINS) 
 IT IS CARRIED OUT THROUGH THE 
CHARGING/INSPECTION PORT 
 IT IS DONE SLOWLY TO ALLOW THE POWDER TO MIX
DISPERSING 
 CARRIED OUT AT HSD LEVEL (1ST FLOOR) 
 DISPENSING CAN LAST FROM 60-180 MINS 
 RESULTS IN PARTIAL GRINDING 
 MAIN OBJECTIVE IS TO ACHIEVE HOMOGENEOUS 
MIXTURE.
MILLING 
 OPERATOR ENGAGEMENT AT GROUND FLOOR 
 OPERATION TIME VARY BETWEEN 180-240 MINS 
 PREMIER MILL WITH ZERKONIA BEADS IS USED 
5LT/MIN 
HSD PM 
 FINAL FINISH IS ACHIEVED DURING MILLING 
OPERATION
DISCHARGING AND FILTERATION 
 OPERATOR ENGAGEMENT AT GROUND FLOOR 
 OPERATION TIME IS BETWEEN 240-300 MINS 
DISCHARGING 
HSD PM 
10μ 25μ 
FILTERATION 
MIXER/ 
1KL 
MIXER 
2KL 
MIXER/1K 
L
PACKING 
 OPERATOR ENGAGEMENT AT GROUND 
FLOOR 
 TIME TAKEN IS BETWEEN 60-90 MINS 
 PACKED IN 30 LTS CANS AND 200 LT BARRELS 
 ADDITIONAL MAN REQUIRED TO TRANSFER 
THE PACKED ITEM TO BSR
AVERAGE CYCLE TIME 
 ACP 675 GREY(2.5 T) : 24 HRS 
 ACP 610 BLACK (2.5 T) : 21.5 HRS 
 ACP 611 GREY (2.5 T) : 19.25 HRS 
 CCP 675 (2.24 T) : 18 HRS 
 CCP 610/611 (2.4 T) :18.5 HRS 
 INTERMEDIATE (1 T) : 9 HRS 
Existing production capacity per month : 40 MT 
Existing man days per month : 100 
Existing Man Days per KL produced : 2.77 
CED production capacity.existing.xlsx
PHASE 2 
OBSERVATIONS 
& 
RECOMENDATIONS
MONTH PLANNING 
 Following to be taken into consideration when planning 
• Change over 
NON CLEANING SEQUENCE 
CLEANING REQUIRED 
WHITE 
(CCP) 
• Priority for each month 
• CCP storage capacity 
• Raw material availability 
BLACK 
(ACP 610) 
GREY 
( 675/611) 
BLACK 
(ACP 6100 
GREY 
(ACP 
675/611) 
WHITE 
(CCP)
OBSERVATION 
 Cleaning involves significant amount of time, hence 
month plan should be designed such a way that non 
cleaning sequence can be executed in consideration with 
the priority 
 Presently average no. of cleaning per month is 
2.83,which can be reduced to 2 by increasing the CCP 
storage capacity by installing additional plastic tank 
outside CED room(1st floor). 
 Currently CCP is stored in barrels, a 1or2 ton tank would 
consume the same amount of space of 4 barrels(800 
lts),so three tanks can be installed to replace 12 barrels 
which would increase the storage capacity with no 
additional space required
CYCLE TIME 
OBSERVATION: 
 Irregular sequence, there is no consistency and certain 
activities are performed at different points 
 man power deployment keeps varying 
 Sometimes N.P.W is carried out in sequence with 
productive activity that results in varied cycle time 
 The above makes it difficult to monitor and control the 
process and also in finding bottle necks 
 Some activities like liquid charging involves too much 
time than it actually should, as it involves preparation. 
 Premier Mill can at one time process only 1 batch and 
hence sometimes the process time takes to much time 
during change over.
RECOMMENDATIONS: 
 Standard sequence be designed where in the N.P.W is well 
placed simultaneously with critical activities, floor wise. 
 Operators & officers should be trained to execute the 
planned sequence. 
recommended sequence.xlsx 
 Preparation for certain activities can be carried out 
simultaneously with previous activities. 
ex: 1 set of empty barrels and cans be kept ready for 
each liquid R.M.so the operator can keep measured 
quantity of liquid R.M prepared for liquid charging well in 
advance simultaneously with a previous activity. This will 
considerably reduce the time for charging. 
recommended preparation.xlsx
PROCESS 
OBSERVATION: 
 SAMPLING 
SAMPLE POINT 
MIXTURE PROCESSOR 
PRESENT SAMPLE POINT 
• Incorrect sampling point 
• Sampling is not carried out as per the time mentioned in the standard 
process 
RESULT: Sample obtained doesn't represent the actual mixture 
and hence the finish obtained is incorrect. 
- the batch fails to pass QA analysis and hence the batch has 
to be reversed which results in longer cycle time.
RECOMMENDATION: 
 Samples to be taken from correct sampling point 
 Samples should be taken at the interval mentioned 
in the W.O slip and be logged correctly to monitor 
the process. 
 Officers and operators be explained about the 
significance of sampling time and point. 
 Samples be sent well in advance to QA department 
,considering the lead time of 4 hrs, to maintain the 
sequence.
 FLOW RATE 
• The flow rate of all the variants during milling is 5-5.2 lts/min 
i.e. it should take around 12 sec to fill up 1 lt can. 
• The tolerance is only 200 ml and hence it is very important to 
maintain the flow rate within the range to achieve the desired 
finish in time. 
• Presently it takes 7-8 sec to fill up 1lt can i.e. 7.5 lts/min 
which is quite high than the standard flow rate. 
Results: 
• It takes longer time to achieve the Finnish. 
• Even after the finish is obtained the discharging is done 
through Premier mill to make sure the finish is as desired, 
which is not a standardize procedure and add to the cycle 
time.
RECOMMENDATION: 
 Officers and operators be explained about the 
significance of flow rate during milling operations 
 The flow rate be checked frequently during operations as 
there is no flow meter available and should be logged 
correctly. 
 If the flow rate is maintained and the samples taken 
from the correct point and time as per standardized 
procedure, desired finish can be achieved in time and 
discharging to the mixers can be done without PM 
,which would considerably reduce the cycle time. 
recommended.process.xlsx
OPERATORS ENGAGEMENT TIME 
 Presently the operator engagement is 370 mins per shift, 
which is 88 % of the standard time of 420 mins. 
 Operation is stopped for 
• 45-50mins during shift change 
• 45-50 mins during lunch/dinner break 
• 15-20 mins during tea breaks 
 Workers engagement and operation is not monitored by 
officers 
 CED operators have to wait for instructions during 
takeover of shift as the officer is engaged in instructing the 
other operators or making shift reports
RECOMMENDATIONS 
 Operations and workers engagement time be logged by the 
officer 
 Operator should log time during breaks along with operations 
carried out 
 Officer should make instruction slip for the relieving operator 
when the handing over operator reports at the end of the shift, 
so that time is saved when the next operator comes on shift. 
 Performance bonus apart from CED allowance be offered 
during projected target achieving months to motivate the 
operators 
 Young operators be trained and put in regular shift so as to 
implement new norms effectively and efficiently 
 The shift change time of operators and workers be staggered 
so that the operation is not effected during shift change 
process. 
recommended.operation time.xlsx
IMPACT 
 CYCLE TIME 
 Standard sequence of activity will reduce the MD per ton by 14 
%,and will help in monitoring and identifying bottle necks. 
 Preparing for activities in advance will reduce MD per ton by 10 % 
,and time involved in activities like liquid charging will reduce 
significantly. 
 PROCESS 
 If the standardized procedure is followed religiously then 
discharging can be done without Premier Mill with the desired 
finish and will reduce the MD per ton by 8-10% 
 OPERATION TIME 
 If the operation and operator engagement time is monitored with 
95% of standard operation time would further reduce MD per ton 
The above recommendation will effectively reduce MD per KL but 
also the monthly production can be increased by 15-20%
TOTAL PRODUCTIVE MAINTENANCE 
• PED/operators & officers are to be involved in keeping the 
equipment in good working order to minimize production losses 
from equipment repairs, assists, set-ups, and the like. 
• Preventive maintenance system be designed so as to reduce the 
downtime especially for the Premier Mill . 
(weekly checks like leakages, lubrication, connections, glands 
,vibration and electrical etc and monthly checks like motor 
insulation etc, and maintenance intervals be reduced by 25%) 
• Miscellaneous equipments like flow meters should be checked, as 
every time operators have to otherwise measure and add water 
which takes time. 
• Ex: flow meter(1st floor) on DM water line is not visible and hence 
operators have to manually measure and add water which consumes 
time 
• Portable high pressure water jet machines(40-60 kgf) can be used 
for cleaning of HSD & MIXERS which can reduce the time by 
more than 50% and also water usage can be reduced by 50%.
THANK YOU

More Related Content

What's hot

General HydropowerPresentation
General HydropowerPresentationGeneral HydropowerPresentation
General HydropowerPresentationTongai Mundiya
 
Case study electronics industry
Case study   electronics industryCase study   electronics industry
Case study electronics industryGanesh TN
 
Chirag darji resume for production operator (oil & gas)
Chirag darji resume for production operator (oil & gas)Chirag darji resume for production operator (oil & gas)
Chirag darji resume for production operator (oil & gas)CHIRAG DARJI
 
Glen &dimplex Process improvements
Glen &dimplex Process improvementsGlen &dimplex Process improvements
Glen &dimplex Process improvementsNigel Charles
 
Senior Water Treatment Plant Operator
Senior Water Treatment Plant Operator Senior Water Treatment Plant Operator
Senior Water Treatment Plant Operator YPIC
 
Marketing Presentation - June 2016
Marketing Presentation - June 2016 Marketing Presentation - June 2016
Marketing Presentation - June 2016 Mark Knippa
 
LEAN SMED TRAINING FOR SUPERVISORS AND OPERATORS
LEAN SMED TRAINING FOR SUPERVISORS AND OPERATORSLEAN SMED TRAINING FOR SUPERVISORS AND OPERATORS
LEAN SMED TRAINING FOR SUPERVISORS AND OPERATORSJulian Kalac P.Eng
 
How to implement Single minute exchange of die
How to implement Single minute exchange of die How to implement Single minute exchange of die
How to implement Single minute exchange of die Nikunj Rana
 
Retrocommissioning Works
Retrocommissioning WorksRetrocommissioning Works
Retrocommissioning WorksCx Associates
 
FDF Energy Services
FDF Energy Services FDF Energy Services
FDF Energy Services Kurt Daigle
 
CV Oil and Gas Field Operator Nishanth P Joy
CV Oil and Gas Field Operator Nishanth P JoyCV Oil and Gas Field Operator Nishanth P Joy
CV Oil and Gas Field Operator Nishanth P JoyNISHANTH JOY
 

What's hot (19)

chinna terminal operator.
chinna terminal operator.chinna terminal operator.
chinna terminal operator.
 
General HydropowerPresentation
General HydropowerPresentationGeneral HydropowerPresentation
General HydropowerPresentation
 
Case study electronics industry
Case study   electronics industryCase study   electronics industry
Case study electronics industry
 
kashif( 23-2-15)
kashif( 23-2-15)kashif( 23-2-15)
kashif( 23-2-15)
 
Chirag darji resume for production operator (oil & gas)
Chirag darji resume for production operator (oil & gas)Chirag darji resume for production operator (oil & gas)
Chirag darji resume for production operator (oil & gas)
 
Omar's CV
Omar's CVOmar's CV
Omar's CV
 
Glen &dimplex Process improvements
Glen &dimplex Process improvementsGlen &dimplex Process improvements
Glen &dimplex Process improvements
 
jan eve resume final
jan eve resume finaljan eve resume final
jan eve resume final
 
Dinesh Chauhan
Dinesh ChauhanDinesh Chauhan
Dinesh Chauhan
 
Senior Water Treatment Plant Operator
Senior Water Treatment Plant Operator Senior Water Treatment Plant Operator
Senior Water Treatment Plant Operator
 
resume (2)
resume (2)resume (2)
resume (2)
 
Marketing Presentation - June 2016
Marketing Presentation - June 2016 Marketing Presentation - June 2016
Marketing Presentation - June 2016
 
Antro
AntroAntro
Antro
 
LEAN SMED TRAINING FOR SUPERVISORS AND OPERATORS
LEAN SMED TRAINING FOR SUPERVISORS AND OPERATORSLEAN SMED TRAINING FOR SUPERVISORS AND OPERATORS
LEAN SMED TRAINING FOR SUPERVISORS AND OPERATORS
 
How to implement Single minute exchange of die
How to implement Single minute exchange of die How to implement Single minute exchange of die
How to implement Single minute exchange of die
 
Retrocommissioning Works
Retrocommissioning WorksRetrocommissioning Works
Retrocommissioning Works
 
FDF Energy Services
FDF Energy Services FDF Energy Services
FDF Energy Services
 
CV Oil and Gas Field Operator Nishanth P Joy
CV Oil and Gas Field Operator Nishanth P JoyCV Oil and Gas Field Operator Nishanth P Joy
CV Oil and Gas Field Operator Nishanth P Joy
 
SMED-Observation Training
SMED-Observation TrainingSMED-Observation Training
SMED-Observation Training
 

Similar to Asian Paints

Process Selection and Facility layout.ppt
Process Selection and Facility layout.pptProcess Selection and Facility layout.ppt
Process Selection and Facility layout.pptSandipanMaji3
 
Schneider Case Study Challenge
Schneider Case Study ChallengeSchneider Case Study Challenge
Schneider Case Study ChallengeNikhil Kejriwal
 
Lean Supply Chain Management--by JULIAN KALAC
Lean Supply Chain Management--by JULIAN KALACLean Supply Chain Management--by JULIAN KALAC
Lean Supply Chain Management--by JULIAN KALACJulian Kalac P.Eng
 
Implémentation Méthode Single Minute Exchange of Dies(SMED)
Implémentation Méthode Single Minute Exchange of Dies(SMED)Implémentation Méthode Single Minute Exchange of Dies(SMED)
Implémentation Méthode Single Minute Exchange of Dies(SMED)MohammedLahssaini1
 
Production planning
Production planningProduction planning
Production planningDavid Jaison
 
Nokia manaus090828 final_presentation_vsa_v4
Nokia manaus090828 final_presentation_vsa_v4Nokia manaus090828 final_presentation_vsa_v4
Nokia manaus090828 final_presentation_vsa_v4CarlosMoura111
 
Batch & Queue vs Lean Continuous Flow
Batch & Queue vs Lean Continuous FlowBatch & Queue vs Lean Continuous Flow
Batch & Queue vs Lean Continuous FlowJulian Kalac P.Eng
 
Production planning and control 2019
Production planning and control 2019Production planning and control 2019
Production planning and control 2019sserwaniko
 
Aggregate planning and mps om
Aggregate planning and mps omAggregate planning and mps om
Aggregate planning and mps omfatuma ahmed
 
Standardised work for garment industry- Prakhar Jain
Standardised work for garment industry- Prakhar JainStandardised work for garment industry- Prakhar Jain
Standardised work for garment industry- Prakhar JainPrakhar Jain
 
chinedu's CV - maintenance - BOP engr
chinedu's CV - maintenance -  BOP engrchinedu's CV - maintenance -  BOP engr
chinedu's CV - maintenance - BOP engrChinedu Emeanuwa
 
JULIAN KALAC -EXAMPLES OF LEAN SIX SIGMA BLACK BELT PROJECTS
JULIAN KALAC -EXAMPLES OF LEAN SIX SIGMA BLACK BELT PROJECTS JULIAN KALAC -EXAMPLES OF LEAN SIX SIGMA BLACK BELT PROJECTS
JULIAN KALAC -EXAMPLES OF LEAN SIX SIGMA BLACK BELT PROJECTS Julian Kalac P.Eng
 

Similar to Asian Paints (20)

5 Steps to implementing Lean
5  Steps to implementing Lean5  Steps to implementing Lean
5 Steps to implementing Lean
 
Process Selection and Facility layout.ppt
Process Selection and Facility layout.pptProcess Selection and Facility layout.ppt
Process Selection and Facility layout.ppt
 
Schneider Case Study Challenge
Schneider Case Study ChallengeSchneider Case Study Challenge
Schneider Case Study Challenge
 
Single Minute Exchange of Dies
Single Minute Exchange of DiesSingle Minute Exchange of Dies
Single Minute Exchange of Dies
 
Lean Supply Chain Management--by JULIAN KALAC
Lean Supply Chain Management--by JULIAN KALACLean Supply Chain Management--by JULIAN KALAC
Lean Supply Chain Management--by JULIAN KALAC
 
5546
55465546
5546
 
Implémentation Méthode Single Minute Exchange of Dies(SMED)
Implémentation Méthode Single Minute Exchange of Dies(SMED)Implémentation Méthode Single Minute Exchange of Dies(SMED)
Implémentation Méthode Single Minute Exchange of Dies(SMED)
 
Tpm+basics
Tpm+basicsTpm+basics
Tpm+basics
 
Tpm+basics
Tpm+basicsTpm+basics
Tpm+basics
 
Sharath-Resume
Sharath-ResumeSharath-Resume
Sharath-Resume
 
Production planning
Production planningProduction planning
Production planning
 
Nokia manaus090828 final_presentation_vsa_v4
Nokia manaus090828 final_presentation_vsa_v4Nokia manaus090828 final_presentation_vsa_v4
Nokia manaus090828 final_presentation_vsa_v4
 
Batch & Queue vs Lean Continuous Flow
Batch & Queue vs Lean Continuous FlowBatch & Queue vs Lean Continuous Flow
Batch & Queue vs Lean Continuous Flow
 
Production planning and control 2019
Production planning and control 2019Production planning and control 2019
Production planning and control 2019
 
Aggregate planning and mps om
Aggregate planning and mps omAggregate planning and mps om
Aggregate planning and mps om
 
Standardised work for garment industry- Prakhar Jain
Standardised work for garment industry- Prakhar JainStandardised work for garment industry- Prakhar Jain
Standardised work for garment industry- Prakhar Jain
 
om
omom
om
 
chinedu's CV - maintenance - BOP engr
chinedu's CV - maintenance -  BOP engrchinedu's CV - maintenance -  BOP engr
chinedu's CV - maintenance - BOP engr
 
JULIAN KALAC -EXAMPLES OF LEAN SIX SIGMA BLACK BELT PROJECTS
JULIAN KALAC -EXAMPLES OF LEAN SIX SIGMA BLACK BELT PROJECTS JULIAN KALAC -EXAMPLES OF LEAN SIX SIGMA BLACK BELT PROJECTS
JULIAN KALAC -EXAMPLES OF LEAN SIX SIGMA BLACK BELT PROJECTS
 
zone 3 ppt.pptx
zone 3 ppt.pptxzone 3 ppt.pptx
zone 3 ppt.pptx
 

Asian Paints

  • 1. PRESENTED BY: SUBHASISH DAS Management Trainee Fisher College Of Business ( Indian Programme)
  • 2. OBJECTIVE PROCESS OPTIMIZATION OF CED PASTE SECTION
  • 3. PHASE 1 EVALUATE PRESENT PRODUCTION CAPACITY  PRODUCT MIX:  (ACP 675-60%,ACP 610 BLACK-20%,ACP 611 GREY- 20%)  NO. OF WORKING DAYS: 25  NO. OF SHIFTS AVAILABLE EACH MONTH 75  OPERATION TIME PER SHIFT 370 MINS
  • 4. PROCESS FLOW CHART CHARGING HSD DISPERSING GRINDING ( HSD-PM-HSD) DISCHARGI NG SAMPLING /ADJUSTM ENT/QA FILTERATION PACKING
  • 5. CHARGING  CARRIED OUT AT HSD LEVEL(1ST FLOOR) LIQUID CHARGING: (90-150 MINS)  REQUIRES ADDITIONAL MAN POWER  THE HSD HOOD IS RAISED TO POUR THE RAW MATERIAL DIRECTLY BUT WITH FREQUENT WEIGHT MEASURE MENT POWDER CHARGING: (45-90 MINS)  IT IS CARRIED OUT THROUGH THE CHARGING/INSPECTION PORT  IT IS DONE SLOWLY TO ALLOW THE POWDER TO MIX
  • 6. DISPERSING  CARRIED OUT AT HSD LEVEL (1ST FLOOR)  DISPENSING CAN LAST FROM 60-180 MINS  RESULTS IN PARTIAL GRINDING  MAIN OBJECTIVE IS TO ACHIEVE HOMOGENEOUS MIXTURE.
  • 7. MILLING  OPERATOR ENGAGEMENT AT GROUND FLOOR  OPERATION TIME VARY BETWEEN 180-240 MINS  PREMIER MILL WITH ZERKONIA BEADS IS USED 5LT/MIN HSD PM  FINAL FINISH IS ACHIEVED DURING MILLING OPERATION
  • 8. DISCHARGING AND FILTERATION  OPERATOR ENGAGEMENT AT GROUND FLOOR  OPERATION TIME IS BETWEEN 240-300 MINS DISCHARGING HSD PM 10μ 25μ FILTERATION MIXER/ 1KL MIXER 2KL MIXER/1K L
  • 9. PACKING  OPERATOR ENGAGEMENT AT GROUND FLOOR  TIME TAKEN IS BETWEEN 60-90 MINS  PACKED IN 30 LTS CANS AND 200 LT BARRELS  ADDITIONAL MAN REQUIRED TO TRANSFER THE PACKED ITEM TO BSR
  • 10. AVERAGE CYCLE TIME  ACP 675 GREY(2.5 T) : 24 HRS  ACP 610 BLACK (2.5 T) : 21.5 HRS  ACP 611 GREY (2.5 T) : 19.25 HRS  CCP 675 (2.24 T) : 18 HRS  CCP 610/611 (2.4 T) :18.5 HRS  INTERMEDIATE (1 T) : 9 HRS Existing production capacity per month : 40 MT Existing man days per month : 100 Existing Man Days per KL produced : 2.77 CED production capacity.existing.xlsx
  • 11. PHASE 2 OBSERVATIONS & RECOMENDATIONS
  • 12. MONTH PLANNING  Following to be taken into consideration when planning • Change over NON CLEANING SEQUENCE CLEANING REQUIRED WHITE (CCP) • Priority for each month • CCP storage capacity • Raw material availability BLACK (ACP 610) GREY ( 675/611) BLACK (ACP 6100 GREY (ACP 675/611) WHITE (CCP)
  • 13. OBSERVATION  Cleaning involves significant amount of time, hence month plan should be designed such a way that non cleaning sequence can be executed in consideration with the priority  Presently average no. of cleaning per month is 2.83,which can be reduced to 2 by increasing the CCP storage capacity by installing additional plastic tank outside CED room(1st floor).  Currently CCP is stored in barrels, a 1or2 ton tank would consume the same amount of space of 4 barrels(800 lts),so three tanks can be installed to replace 12 barrels which would increase the storage capacity with no additional space required
  • 14. CYCLE TIME OBSERVATION:  Irregular sequence, there is no consistency and certain activities are performed at different points  man power deployment keeps varying  Sometimes N.P.W is carried out in sequence with productive activity that results in varied cycle time  The above makes it difficult to monitor and control the process and also in finding bottle necks  Some activities like liquid charging involves too much time than it actually should, as it involves preparation.  Premier Mill can at one time process only 1 batch and hence sometimes the process time takes to much time during change over.
  • 15. RECOMMENDATIONS:  Standard sequence be designed where in the N.P.W is well placed simultaneously with critical activities, floor wise.  Operators & officers should be trained to execute the planned sequence. recommended sequence.xlsx  Preparation for certain activities can be carried out simultaneously with previous activities. ex: 1 set of empty barrels and cans be kept ready for each liquid R.M.so the operator can keep measured quantity of liquid R.M prepared for liquid charging well in advance simultaneously with a previous activity. This will considerably reduce the time for charging. recommended preparation.xlsx
  • 16. PROCESS OBSERVATION:  SAMPLING SAMPLE POINT MIXTURE PROCESSOR PRESENT SAMPLE POINT • Incorrect sampling point • Sampling is not carried out as per the time mentioned in the standard process RESULT: Sample obtained doesn't represent the actual mixture and hence the finish obtained is incorrect. - the batch fails to pass QA analysis and hence the batch has to be reversed which results in longer cycle time.
  • 17. RECOMMENDATION:  Samples to be taken from correct sampling point  Samples should be taken at the interval mentioned in the W.O slip and be logged correctly to monitor the process.  Officers and operators be explained about the significance of sampling time and point.  Samples be sent well in advance to QA department ,considering the lead time of 4 hrs, to maintain the sequence.
  • 18.  FLOW RATE • The flow rate of all the variants during milling is 5-5.2 lts/min i.e. it should take around 12 sec to fill up 1 lt can. • The tolerance is only 200 ml and hence it is very important to maintain the flow rate within the range to achieve the desired finish in time. • Presently it takes 7-8 sec to fill up 1lt can i.e. 7.5 lts/min which is quite high than the standard flow rate. Results: • It takes longer time to achieve the Finnish. • Even after the finish is obtained the discharging is done through Premier mill to make sure the finish is as desired, which is not a standardize procedure and add to the cycle time.
  • 19. RECOMMENDATION:  Officers and operators be explained about the significance of flow rate during milling operations  The flow rate be checked frequently during operations as there is no flow meter available and should be logged correctly.  If the flow rate is maintained and the samples taken from the correct point and time as per standardized procedure, desired finish can be achieved in time and discharging to the mixers can be done without PM ,which would considerably reduce the cycle time. recommended.process.xlsx
  • 20. OPERATORS ENGAGEMENT TIME  Presently the operator engagement is 370 mins per shift, which is 88 % of the standard time of 420 mins.  Operation is stopped for • 45-50mins during shift change • 45-50 mins during lunch/dinner break • 15-20 mins during tea breaks  Workers engagement and operation is not monitored by officers  CED operators have to wait for instructions during takeover of shift as the officer is engaged in instructing the other operators or making shift reports
  • 21. RECOMMENDATIONS  Operations and workers engagement time be logged by the officer  Operator should log time during breaks along with operations carried out  Officer should make instruction slip for the relieving operator when the handing over operator reports at the end of the shift, so that time is saved when the next operator comes on shift.  Performance bonus apart from CED allowance be offered during projected target achieving months to motivate the operators  Young operators be trained and put in regular shift so as to implement new norms effectively and efficiently  The shift change time of operators and workers be staggered so that the operation is not effected during shift change process. recommended.operation time.xlsx
  • 22. IMPACT  CYCLE TIME  Standard sequence of activity will reduce the MD per ton by 14 %,and will help in monitoring and identifying bottle necks.  Preparing for activities in advance will reduce MD per ton by 10 % ,and time involved in activities like liquid charging will reduce significantly.  PROCESS  If the standardized procedure is followed religiously then discharging can be done without Premier Mill with the desired finish and will reduce the MD per ton by 8-10%  OPERATION TIME  If the operation and operator engagement time is monitored with 95% of standard operation time would further reduce MD per ton The above recommendation will effectively reduce MD per KL but also the monthly production can be increased by 15-20%
  • 23. TOTAL PRODUCTIVE MAINTENANCE • PED/operators & officers are to be involved in keeping the equipment in good working order to minimize production losses from equipment repairs, assists, set-ups, and the like. • Preventive maintenance system be designed so as to reduce the downtime especially for the Premier Mill . (weekly checks like leakages, lubrication, connections, glands ,vibration and electrical etc and monthly checks like motor insulation etc, and maintenance intervals be reduced by 25%) • Miscellaneous equipments like flow meters should be checked, as every time operators have to otherwise measure and add water which takes time. • Ex: flow meter(1st floor) on DM water line is not visible and hence operators have to manually measure and add water which consumes time • Portable high pressure water jet machines(40-60 kgf) can be used for cleaning of HSD & MIXERS which can reduce the time by more than 50% and also water usage can be reduced by 50%.