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OJT AT SURYA NEPAL 
Bikram Dahal 
Thapathali Campus 
PMD 
Supervisor 
Ayush Raj Aryal 
I/C PMD
Projects 
Objective 
Increase productivity, quality and profitability through keen data analysis and process 
design; significantly improve operations and provide efficient resolution of process issues. 
• Admoist protocol 
• Increase filling value of Surya 
Main 
projects 
• Spillage reduction in CTS bin 
• GFP feed maintenance at CRS Cutter 
• Cp & Cpk of CRS Dryer 
• Optimization of blend change time (CRS line) 
Side Project 
Design • Design of pan for Sampling at HT and stand for Serrico Trap 
OJT at Surya Nepal
Methodology 
1 
2 
Asking question (understanding problem) 
Labeling patterns in data 
Modeling conceptually 
Decomposing 
Experimenting 
implementation 
3 
4 
5 
6 
7 
Continual monitoring and communicating 
OJT at Surya Nepal
Moisture Content 
variation in cutter above 
0.5 
Admoist protocol and Data Analysis 
Method Mother Nature Raw material 
Moisture Content 
Intrinsic Property 
Size distribution 
Bulking time 
Type 
(cold or Hot) 
Humidity 
Temperature 
Power failure 
Hand feel 
Moisture 
Uniformity of water, raw material 
and steam flow 
Measuring Instrument Least count 
Setting of machine 
Uniformity of filling 
Machine 
Man 
Finding 
Fig 1: Fish bone Diagram of causes for moisture variation
Result and Discussion 
40.00 
39.50 
39.00 
38.50 
38.00 
37.50 
37.00 
36.50 
36.00 
35.50 
Moisture Mean Ex-cutter 
0 5 10 15 20 25 30 35 
0.60 
0.50 
0.40 
0.30 
0.20 
0.10 
0.00 
S.D Chart 
0 5 10 15 20 25 30 35 
Admoist protocol and Data Analysis
Result and Discussion 
• Weight deviation 
for HVM/VSN5 
stem is high 
because stem of 
this Grade are 
longer and have 
non-uniform 
thickness 
Admoist protocol and Data Analysis 
6.00% 
5.00% 
4.00% 
3.00% 
2.00% 
1.00% 
0.00% 
Coefficient of Variation of weight 
0 5 10 15 20 25 30
Due to low filling value of CRS from regular interval in QUAS daily report after 17 aswin. 
Temperature of product at 1 meter distance from outlet of admoist was checked. It was 
found that temperature was above SOP i.e. 76. 
Cause Solution Result 
• Failure of PRV to 
maintain set pressure of 
0.3-0.4 bar. Line 
pressure was changing 
as per main pressure 
variation. 
• Main line pressure was 
decrease to 5bar from 
maximum pressure of 
boiler i.e. 7- 8 bar. 
• Temperature of 3 samples 
of 3 operation was tracked 
average value was found 
71 C 
Further Step 
Admoist protocol and Data Analysis
Finding (Research) 
Increasing filling Value of Surya 
• Virginia Tobacco have less filling Value due to high sugar Content 
• Lamina Cutter is optimum at 32CPI other argue its best at 25 CPI 
• F.V varies among different part of same leaf, between different year crops 
• FV is very sensitive to moisture 
• Main control able factor effecting filling value 
• HT steam pressure 
• CPI of cutter 
• Storage time and temperature 
• Cheese pressure of cutter 
• Type of dryer
Finding(Data analysis) 
Increasing filling Value of Surya 
• F.V after Ex-cutter was below average 
• Expansion from cutter to H.T of both 
lamina and CRS was with in speciation limit 
• CPI of Cutter was below average and 
not uniform 
• Steam pressure of CRS H.T could be increase 
• Order of operation had no effect on 
filling value 
• Filling value jump from ex-cutter 
and ex-dryer 
13.62 
8.11 
16% 
14% 
12% 
10% 
8% 
6% 
4% 
2% 
0% 
Ex-cutter to Ex-bin Ex-cutter to Ex-Dryer 
CRS Lamina
Step taken to improve F.V 
Increasing filling Value of Surya 
• Maintenance and Calibration of Cutter was carried out 
• Steam pressure of CRS H.T was increased from 4bar to 5bar 
• Cheese pressure of lamina cutter was reduce for NG to 15KN 
• Temperature of lamina dryer was reduced from 66 C to 62 C
Increasing filling Value of Surya 
CPI of Cutter Result 
139 
166 
180 
160 
140 
120 
100 
80 
60 
40 
20 
0 
Before After 
CPI 
0.35 
0.30 
0.25 
0.20 
0.15 
0.10 
0.05 
0.00 
Wax Thickness (before) 
0 10 20 30 40 50 
0.25 
0.2 
0.15 
0.1 
0.05 
0 
Wax Thickness (after) 
0 10 20 30 40 50
Result 
Increasing filling Value of Surya 
Filling Value Cut Tobacco 
47.78 
49.15 
49.50 
49.00 
48.50 
48.00 
47.50 
47.00 
Before After 
After Before 
Mean 49.16 47.78 
Observa 
tions 32 36 
p-value 2.91E-06 
• Continuous 
monitoring was 
carried till end of 
project 
* FV value for before batch (NG1-42) and after (NG-43-78) was taken form QUAS daily report
Scope of Further Improvement 
Increasing filling Value of Surya 
• Increase tobacco and steam ratio to find optimum ratio in H.T 
• Changing rate and temperature of airflow in dryer 
• Experimenting with CPI of both cutter under control environment
Result 
3.5 
3 
2.5 
2 
1.5 
1 
0.5 
0 
Cp and Cpk of CRS dryer 
1 2 3 4 5 6 7 8 9 10 
Old Boiler | | New boiler 
Cpk 
Cp 
0.7 
0.6 
0.5 
0.4 
0.3 
0.2 
0.1 
0 
SD chart of Steam pressure at HT 
0 1 2 3 4 5 6 7 8 9 10 
Old Boiler | | New Boiler 
Cp and Cpk of CRS Dryer
In order to maintain uniform flow of product at CRS cutter, product level at GFP should always 
be visible. But some of the time, product at GFP of CRS cutter is empty. 
Cause Solution Result 
• Large tart time 
difference between 
VOV(2) and bin belt 
conveyer(1) i.e. 5 sec 
• High speed of Belt 
conveyer(6) 
• Start time difference 
between 2 and 1 was 
reduce to 1 sec 
• Speed of 6 was reduce to 
12+0.5 all other blend 
except VSY from which it 
was reduce to 15+ 0.5 
• No single gap between 
stem in conveyer from bin 
to cutter 
• Product at GFP was visible 
most of the time 
Introduction 
Feed maintenance at CRS cutter GFP
Feed maintenance at CRS cutter GFP
Spillage reduction CTS Area
• Inter-operational 
time 8 minutes 
• 90sec gap 
• 390sec time 
difference 
between start 
and finish 
Stem Conditioning 
WEIGHCON 
Optimization of Blend Change Time 
SC 
ADMOIST 
AIR LIFT 
40 sec 65 sec 165sec 
45 sec 510 sec 
60 sec 
Inter-operational time 
sec 
30 sec 
35 sec 
OP 1 390 sec 90 Sec OP 2 
Start: 
Finish: 
Diff. start to finish Gap
HT 
• Speed cylinder 
rpm at tail out 
was increase 
from 16 to 18 
• Decrease In 1 
minutes tail 
out time 
• Inter-operation 
time is 360sec 
after sensor in 
GFP Detects no 
Tobacco 
CRS Dryer 
VC 
WEYCON 
KLS 
Optimization of Blend Change Time 
55 sec 70 sec 390 sec 45 sec 
Variable 40 -240 sec 90 sec 705 sec 50 sec 
Start: 
Finish: 
Inter-operational time 
Diff. start to finish Gap 
sec 
OP 1 280 sec 80 Sec OP 2
Design 
Design of Pan for Sampling at HT
Summary 
OJT at Surya Nepal 
• Admoist protocol was passed 
• Filling value of NG was increased by 3% on average 
• Cp and Cpk of CRS dryer were calculated 
• Spillage of CTS was reduce by 5-8 kg/day 
• Uniform feed at CRS cutter was maintained 
• Pan and stand were designed 
• Standard blend change time was established for CRS conditioning and CRS 
Dryer line. Along with decrease in tail out time of CRS dryer.
An OJT Report On 3 Month Internship at Surya Nepal

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An OJT Report On 3 Month Internship at Surya Nepal

  • 1. OJT AT SURYA NEPAL Bikram Dahal Thapathali Campus PMD Supervisor Ayush Raj Aryal I/C PMD
  • 2. Projects Objective Increase productivity, quality and profitability through keen data analysis and process design; significantly improve operations and provide efficient resolution of process issues. • Admoist protocol • Increase filling value of Surya Main projects • Spillage reduction in CTS bin • GFP feed maintenance at CRS Cutter • Cp & Cpk of CRS Dryer • Optimization of blend change time (CRS line) Side Project Design • Design of pan for Sampling at HT and stand for Serrico Trap OJT at Surya Nepal
  • 3. Methodology 1 2 Asking question (understanding problem) Labeling patterns in data Modeling conceptually Decomposing Experimenting implementation 3 4 5 6 7 Continual monitoring and communicating OJT at Surya Nepal
  • 4. Moisture Content variation in cutter above 0.5 Admoist protocol and Data Analysis Method Mother Nature Raw material Moisture Content Intrinsic Property Size distribution Bulking time Type (cold or Hot) Humidity Temperature Power failure Hand feel Moisture Uniformity of water, raw material and steam flow Measuring Instrument Least count Setting of machine Uniformity of filling Machine Man Finding Fig 1: Fish bone Diagram of causes for moisture variation
  • 5. Result and Discussion 40.00 39.50 39.00 38.50 38.00 37.50 37.00 36.50 36.00 35.50 Moisture Mean Ex-cutter 0 5 10 15 20 25 30 35 0.60 0.50 0.40 0.30 0.20 0.10 0.00 S.D Chart 0 5 10 15 20 25 30 35 Admoist protocol and Data Analysis
  • 6. Result and Discussion • Weight deviation for HVM/VSN5 stem is high because stem of this Grade are longer and have non-uniform thickness Admoist protocol and Data Analysis 6.00% 5.00% 4.00% 3.00% 2.00% 1.00% 0.00% Coefficient of Variation of weight 0 5 10 15 20 25 30
  • 7. Due to low filling value of CRS from regular interval in QUAS daily report after 17 aswin. Temperature of product at 1 meter distance from outlet of admoist was checked. It was found that temperature was above SOP i.e. 76. Cause Solution Result • Failure of PRV to maintain set pressure of 0.3-0.4 bar. Line pressure was changing as per main pressure variation. • Main line pressure was decrease to 5bar from maximum pressure of boiler i.e. 7- 8 bar. • Temperature of 3 samples of 3 operation was tracked average value was found 71 C Further Step Admoist protocol and Data Analysis
  • 8. Finding (Research) Increasing filling Value of Surya • Virginia Tobacco have less filling Value due to high sugar Content • Lamina Cutter is optimum at 32CPI other argue its best at 25 CPI • F.V varies among different part of same leaf, between different year crops • FV is very sensitive to moisture • Main control able factor effecting filling value • HT steam pressure • CPI of cutter • Storage time and temperature • Cheese pressure of cutter • Type of dryer
  • 9. Finding(Data analysis) Increasing filling Value of Surya • F.V after Ex-cutter was below average • Expansion from cutter to H.T of both lamina and CRS was with in speciation limit • CPI of Cutter was below average and not uniform • Steam pressure of CRS H.T could be increase • Order of operation had no effect on filling value • Filling value jump from ex-cutter and ex-dryer 13.62 8.11 16% 14% 12% 10% 8% 6% 4% 2% 0% Ex-cutter to Ex-bin Ex-cutter to Ex-Dryer CRS Lamina
  • 10. Step taken to improve F.V Increasing filling Value of Surya • Maintenance and Calibration of Cutter was carried out • Steam pressure of CRS H.T was increased from 4bar to 5bar • Cheese pressure of lamina cutter was reduce for NG to 15KN • Temperature of lamina dryer was reduced from 66 C to 62 C
  • 11. Increasing filling Value of Surya CPI of Cutter Result 139 166 180 160 140 120 100 80 60 40 20 0 Before After CPI 0.35 0.30 0.25 0.20 0.15 0.10 0.05 0.00 Wax Thickness (before) 0 10 20 30 40 50 0.25 0.2 0.15 0.1 0.05 0 Wax Thickness (after) 0 10 20 30 40 50
  • 12. Result Increasing filling Value of Surya Filling Value Cut Tobacco 47.78 49.15 49.50 49.00 48.50 48.00 47.50 47.00 Before After After Before Mean 49.16 47.78 Observa tions 32 36 p-value 2.91E-06 • Continuous monitoring was carried till end of project * FV value for before batch (NG1-42) and after (NG-43-78) was taken form QUAS daily report
  • 13. Scope of Further Improvement Increasing filling Value of Surya • Increase tobacco and steam ratio to find optimum ratio in H.T • Changing rate and temperature of airflow in dryer • Experimenting with CPI of both cutter under control environment
  • 14. Result 3.5 3 2.5 2 1.5 1 0.5 0 Cp and Cpk of CRS dryer 1 2 3 4 5 6 7 8 9 10 Old Boiler | | New boiler Cpk Cp 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0 SD chart of Steam pressure at HT 0 1 2 3 4 5 6 7 8 9 10 Old Boiler | | New Boiler Cp and Cpk of CRS Dryer
  • 15. In order to maintain uniform flow of product at CRS cutter, product level at GFP should always be visible. But some of the time, product at GFP of CRS cutter is empty. Cause Solution Result • Large tart time difference between VOV(2) and bin belt conveyer(1) i.e. 5 sec • High speed of Belt conveyer(6) • Start time difference between 2 and 1 was reduce to 1 sec • Speed of 6 was reduce to 12+0.5 all other blend except VSY from which it was reduce to 15+ 0.5 • No single gap between stem in conveyer from bin to cutter • Product at GFP was visible most of the time Introduction Feed maintenance at CRS cutter GFP
  • 16. Feed maintenance at CRS cutter GFP
  • 18. • Inter-operational time 8 minutes • 90sec gap • 390sec time difference between start and finish Stem Conditioning WEIGHCON Optimization of Blend Change Time SC ADMOIST AIR LIFT 40 sec 65 sec 165sec 45 sec 510 sec 60 sec Inter-operational time sec 30 sec 35 sec OP 1 390 sec 90 Sec OP 2 Start: Finish: Diff. start to finish Gap
  • 19. HT • Speed cylinder rpm at tail out was increase from 16 to 18 • Decrease In 1 minutes tail out time • Inter-operation time is 360sec after sensor in GFP Detects no Tobacco CRS Dryer VC WEYCON KLS Optimization of Blend Change Time 55 sec 70 sec 390 sec 45 sec Variable 40 -240 sec 90 sec 705 sec 50 sec Start: Finish: Inter-operational time Diff. start to finish Gap sec OP 1 280 sec 80 Sec OP 2
  • 20. Design Design of Pan for Sampling at HT
  • 21. Summary OJT at Surya Nepal • Admoist protocol was passed • Filling value of NG was increased by 3% on average • Cp and Cpk of CRS dryer were calculated • Spillage of CTS was reduce by 5-8 kg/day • Uniform feed at CRS cutter was maintained • Pan and stand were designed • Standard blend change time was established for CRS conditioning and CRS Dryer line. Along with decrease in tail out time of CRS dryer.