improving process performance across multiple sites with a
TRANSCRIPT
How to Use This Presentation Template© Copyr i gh t 2014 O SIs o f
t , LLC .
Presented by
Improving Process
Performance Across
Peter Lundqvist, Mathias Holmgård
© Copyr i gh t 2014 O SIs o f t , LLC .
Peter Lundqvist
© Copyr i gh t 2014 O SIs o f t , LLC .
Mathias Holmgård
© Copyr i gh t 2014 O SIs o f t , LLC .
Contents of todays talk
server concept.
sites can now be made in minutes instead of
days.
4
© Copyr i gh t 2014 O SIs o f t , LLC .
Global Science Company with a Broad Portfolio
5
© Copyr i gh t 2014 O SIs o f t , LLC . 6
© Copyr i gh t 2014 O SIs o f t , LLC .
Manufacturing set-up
- Different colors illustrates different platforms (approximated)
- Number of dots illustrates on a relative basis number of runs (not based on
actuals)
Plant E Plant F Plant G Pilot scale
= engineers
© Copyr i gh t 2014 O SIs o f t , LLC .
Reasons for a central PI Server
• WAN traffic site-to-site slow
– Unrealistic to pull the data from each sites PI Server
– PI Batch performance an issue
• Easiest way to fix was installing a Central PI Server
pulling the needed data from the sites
8
© Copyr i gh t 2014 O SIs o f t , LLC .
Architecture of the Central PI Server solution
– One PI to PI Interface on the Central PI Server
• One instance per Production Site pulling data
• Data is converted to SI units on the local PI Server before
transfer
• PI Asset Framework (PI AF) for configuration
• PI Batch for batches
9
© Copyr i gh t 2014 O SIs o f t , LLC .
Structure of Excel tool
End Time
Excel Trends
Measurements Aliases
© Copyr i gh t 2014 O SIs o f t , LLC . 11
Time *-350d * Time incr. 00:06:00 360,00 360s File version : 2014_02_26, PLu
Unit *MF* 2 PI server gcorpp01 BAC
Phase to plot Fermentation 2 Process Fermentation
Batch Batch id Product Unit Product Color Transp. Line weight Trend Alias Unit Y-min Y-max
Batch 1 - * 0 2 Trend 1 OTR mmol/kg/h 112 0 400 2402 SU
Batch 2 - * 0 2 Trend 2 CTR mmol/kg/h 65 0 400 17598 SU
Batch 3 - * 0 2 Trend 3 Carbon-source 1 Feed Mass Flow (as is) kg/h 52 0 auto 2450 SU
Batch 4 - * 0 2 Trend 4 DO2-2 (%) % 71 0 auto 2534 SU
Batch 5 - * 0 2 Trend 5 Active pH pH 2 6,7 7,8 713 SU
Batch 6 - * 0 2 Trend 6 pH-1 pH 120 6,7 7,8 2402 SU
Batch 7 - * 0 2 Trend 7 Ammonia Feed Mass Flow (as is) kg/h 23 0 auto 636 SU
Batch 8 - * 0 2 Trend 8 Ammonia Feed Totalizer (as is) kg 26 0 auto 1238 SU
Batch 9 - * 0 2 Trend 9 Mixing Electrical Energy / Broth Mass kW/kg 107 0 auto 669 SU
Batch 10 - * 0 2 Trend 10 Airflow (Nm3/h) Nm3/h 18 0 12000 2427 SU
Batch 11 - * 0 2 Trend 11 Over Pressure bar 113 0 2,5 534 SU
Batch 12 - * 0 2 Trend 12 kLA-1 1/h 101 0 2000 9071 SU
Batch 13 - * 0 2 Trend 13 Total CTR mol/h 144 0 50000 2366 SU
Batch 14 - * 0 2 Trend 14 Total OTR mol/h 146 0 auto 727 SU
Batch 15 - * 0 2 Trend 15 VVM 1/min 149 0 auto 534 SU
Batch 16 - * 0 2 Trend 16 Offgas %CO2 % 108 0 auto 668 SU
Batch 17 - * 0 2 Trend 17 Offgas %O2 % 110 10 auto 2570 SU
Batch 18 - * 0 2 Trend 18 Temperature Fermentation C 141 0 auto 660 SU
Batch 19 - * 0 2 Trend 19 Broth Mass kg 40 0 auto 2427 SU
Batch 20 - * 0 2 Trend 20 DCO2-1 - at probe level (mmol/kg) mmol/kg 66 0 auto 534 SU
Trend 21 Test 1 Unit 1 0 auto
0 = filled Trend 22 Test 2 Unit 2 0 auto
0,5 = semi-transparent Trend 23 Test 3 Unit 3 0 auto
1 = transparent Trend 24 Test 4 Unit 4 0 auto
Trend 25 Test 5 Unit 5 0 auto
1 = thin
Recalc Calculations
RecalcFind Batches
© Copyr i gh t 2014 O SIs o f t , LLC . 12
Time *-350d * Time incr. 00:06:00 360,00 360s File version : 2014_02_26, PLu
Unit *MF* 2 PI server gcorpp01 BAC
Phase to plot Fermentation 2 Process Fermentation
Batch Batch id Product Unit Product Color Transp. Line weight Trend Alias Unit Y-min Y-max
Batch 1 - * 0 2 Trend 1 OTR mmol/kg/h 112 0 400 2402 SU
Batch 2 - * 0 2 Trend 2 CTR mmol/kg/h 65 0 400 17598 SU
Batch 3 - * 0 2 Trend 3 Carbon-source 1 Feed Mass Flow (as is) kg/h 52 0 auto 2450 SU
Batch 4 - * 0 2 Trend 4 DO2-2 (%) % 71 0 auto 2534 SU
Batch 5 - * 0 2 Trend 5 Active pH pH 2 6,7 7,8 713 SU
Batch 6 - * 0 2 Trend 6 pH-1 pH 120 6,7 7,8 2402 SU
Batch 7 - * 0 2 Trend 7 Ammonia Feed Mass Flow (as is) kg/h 23 0 auto 636 SU
Batch 8 - * 0 2 Trend 8 Ammonia Feed Totalizer (as is) kg 26 0 auto 1238 SU
Batch 9 - * 0 2 Trend 9 Mixing Electrical Energy / Broth Mass kW/kg 107 0 auto 669 SU
Batch 10 - * 0 2 Trend 10 Airflow (Nm3/h) Nm3/h 18 0 12000 2427 SU
Batch 11 - * 0 2 Trend 11 Over Pressure bar 113 0 2,5 534 SU
Batch 12 - * 0 2 Trend 12 kLA-1 1/h 101 0 2000 9071 SU
Batch 13 - * 0 2 Trend 13 Total CTR mol/h 144 0 50000 2366 SU
Batch 14 - * 0 2 Trend 14 Total OTR mol/h 146 0 auto 727 SU
Batch 15 - * 0 2 Trend 15 VVM 1/min 149 0 auto 534 SU
Batch 16 - * 0 2 Trend 16 Offgas %CO2 % 108 0 auto 668 SU
Batch 17 - * 0 2 Trend 17 Offgas %O2 % 110 10 auto 2570 SU
Batch 18 - * 0 2 Trend 18 Temperature Fermentation C 141 0 auto 660 SU
Batch 19 - * 0 2 Trend 19 Broth Mass kg 40 0 auto 2427 SU
Batch 20 - * 0 2 Trend 20 DCO2-1 - at probe level (mmol/kg) mmol/kg 66 0 auto 534 SU
Trend 21 Test 1 Unit 1 0 auto
0 = filled Trend 22 Test 2 Unit 2 0 auto
0,5 = semi-transparent Trend 23 Test 3 Unit 3 0 auto
1 = transparent Trend 24 Test 4 Unit 4 0 auto
Trend 25 Test 5 Unit 5 0 auto
1 = thin
areas
© Copyr i gh t 2014 O SIs o f t , LLC . 13
Time *-350d * Time incr. 00:06:00 360,00 360s File version : 2014_02_26, PLu
Unit *MF* 2 PI server gcorpp01 BAC
Phase to plot Fermentation 2 Process Fermentation
Batch Batch id Product Unit Product Color Transp. Line weight Trend Alias Unit Y-min Y-max
Batch 1 6690337 * 0 2 Trend 1 OTR mmol/kg/h 112 0 400 2402 SU
Batch 2 6690342 * 0 2 Trend 2 CTR mmol/kg/h 65 0 400 17598 SU
Batch 3 6690345 * 0 2 Trend 3 Carbon-source 1 Feed Mass Flow (as is) kg/h 52 0 auto 2450 SU
Batch 4 6690346 * 0 2 Trend 4 DO2-2 (%) % 71 0 auto 2534 SU
Batch 5 6713835 * 0 2 Trend 5 Active pH pH 2 6,7 7,8 713 SU
Batch 6 6713845 * 0 2 Trend 6 pH-1 pH 120 6,7 7,8 2402 SU
Batch 7 6714717 * 0 2 Trend 7 Ammonia Feed Mass Flow (as is) kg/h 23 0 auto 636 SU
Batch 8 6735521 * 0 2 Trend 8 Ammonia Feed Totalizer (as is) kg 26 0 auto 1238 SU
Batch 9 6735527 * 0 2 Trend 9 Mixing Electrical Energy / Broth Mass kW/kg 107 0 auto 669 SU
Batch 10 6735528 * 0 2 Trend 10 Airflow (Nm3/h) Nm3/h 18 0 12000 2427 SU
Batch 11 6754076 * 0 2 Trend 11 Over Pressure bar 113 0 2,5 534 SU
Batch 12 6754078 * 0 2 Trend 12 kLA-1 1/h 101 0 2000 9071 SU
Batch 13 6754079 * 0 2 Trend 13 Total CTR mol/h 144 0 50000 2366 SU
Batch 14 6754080 * 0 2 Trend 14 Total OTR mol/h 146 0 auto 727 SU
Batch 15 6754081 * 0 2 Trend 15 VVM 1/min 149 0 auto 534 SU
Batch 16 6754082 * 0 2 Trend 16 Offgas %CO2 % 108 0 auto 668 SU
Batch 17 6754143 * 0 2 Trend 17 Offgas %O2 % 110 10 auto 2570 SU
Batch 18 6754158 * 0 2 Trend 18 Temperature Fermentation C 141 0 auto 660 SU
Batch 19 6754177 * 0 2 Trend 19 Broth Mass kg 40 0 auto 2427 SU
Batch 20 6754195 * 0 2 Trend 20 DCO2-1 - at probe level (mmol/kg) mmol/kg 66 0 auto 534 SU
Trend 21 Test 1 Unit 1 0 auto
0 = filled Trend 22 Test 2 Unit 2 0 auto
0,5 = semi-transparent Trend 23 Test 3 Unit 3 0 auto
1 = transparent Trend 24 Test 4 Unit 4 0 auto
Trend 25 Test 5 Unit 5 0 auto
1 = thin
Recalc Calculations
RecalcFind Batches
© Copyr i gh t 2014 O SIs o f t , LLC . 14
Time *-350d * Time incr. 00:06:00 360,00 360s File version : 2014_02_26, PLu
Unit *MF* 2 PI server gcorpp01 BAC
Phase to plot Fermentation 2 Process Fermentation
Batch Batch id Product Unit Product Color Transp. Line weight Trend Alias Unit Y-min Y-max
Batch 1 6690337 * CEDA_MF_R261 C01227 0 2 Trend 1 OTR mmol/kg/h 112 0 400 2402 SU
Batch 2 6690342 * CEDA_MF_R262 C01227 0 2 Trend 2 CTR mmol/kg/h 65 0 400 17598 SU
Batch 3 6690345 * CEDA_MF_R263 C01227 0 2 Trend 3 Carbon-source 1 Feed Mass Flow (as is) kg/h 52 0 auto 2450 SU
Batch 4 6690346 * CEDA_MF_R264 C01227 0 2 Trend 4 DO2-2 (%) % 71 0 auto 2534 SU
Batch 5 6713835 * CEDA_MF_R261 C01227 0 2 Trend 5 Active pH pH 2 6,7 7,8 713 SU
Batch 6 6713845 * CEDA_MF_R262 C01227 0 2 Trend 6 pH-1 pH 120 6,7 7,8 2402 SU
Batch 7 6714717 * CEDA_MF_R264 C01227 0 2 Trend 7 Ammonia Feed Mass Flow (as is) kg/h 23 0 auto 636 SU
Batch 8 6735521 * CEDA_MF_R261 C01227 0 2 Trend 8 Ammonia Feed Totalizer (as is) kg 26 0 auto 1238 SU
Batch 9 6735527 * CEDA_MF_R262 C01227 0 2 Trend 9 Mixing Electrical Energy / Broth Mass kW/kg 107 0 auto 669 SU
Batch 10 6735528 * CEDA_MF_R263 C01227 0 2 Trend 10 Airflow (Nm3/h) Nm3/h 18 0 12000 2427 SU
Batch 11 6754076 * CEDA_MF_R261 C01026 0 2 Trend 11 Over Pressure bar 113 0 2,5 534 SU
Batch 12 6754078 * CEDA_MF_R262 C01026 0 2 Trend 12 kLA-1 1/h 101 0 2000 9071 SU
Batch 13 6754079 * CEDA_MF_R263 C01026 0 2 Trend 13 Total CTR mol/h 144 0 50000 2366 SU
Batch 14 6754080 * CEDA_MF_R264 C01026 0 2 Trend 14 Total OTR mol/h 146 0 auto 727 SU
Batch 15 6754081 * CEDA_MF_R261 C01026 0 2 Trend 15 VVM 1/min 149 0 auto 534 SU
Batch 16 6754082 * CEDA_MF_R262 C01026 0 2 Trend 16 Offgas %CO2 % 108 0 auto 668 SU
Batch 17 6754143 * CEDA_MF_R263 C01026 0 2 Trend 17 Offgas %O2 % 110 10 auto 2570 SU
Batch 18 6754158 * CEDA_MF_R264 C01026 0 2 Trend 18 Temperature Fermentation C 141 0 auto 660 SU
Batch 19 6754177 * CEDA_MF_R261 C01026 0 2 Trend 19 Broth Mass kg 40 0 auto 2427 SU
Batch 20 6754195 * CEDA_MF_R262 C01026 0 2 Trend 20 DCO2-1 - at probe level (mmol/kg) mmol/kg 66 0 auto 534 SU
Trend 21 Test 1 Unit 1 0 auto
0 = filled Trend 22 Test 2 Unit 2 0 auto
0,5 = semi-transparent Trend 23 Test 3 Unit 3 0 auto
1 = transparent Trend 24 Test 4 Unit 4 0 auto
Trend 25 Test 5 Unit 5 0 auto
1 = thin
Recalc Calculations
RecalcFind Batches
© Copyr i gh t 2014 O SIs o f t , LLC . 15
Time *-350d * Time incr. 00:06:00 360,00 360s File version : 2014_02_26, PLu
Unit *MF* 2 PI server gcorpp01 BAC
Phase to plot Fermentation 2 Process Fermentation
Batch Batch id Product Unit Product Color Transp. Line weight Trend Alias Unit Y-min Y-max
Batch 1 6690337 * CEDA_MF_R261 C01227 0 2 Trend 1 OTR mmol/kg/h 112 0 400 2402 SU
Batch 2 6690342 * CEDA_MF_R262 C01227 0 2 Trend 2 CTR mmol/kg/h 65 0 400 17598 SU
Batch 3 6690345 * CEDA_MF_R263 C01227 0 2 Trend 3 Carbon-source 1 Feed Mass Flow (as is) kg/h 52 0 auto 2450 SU
Batch 4 6690346 * CEDA_MF_R264 C01227 0 2 Trend 4 DO2-2 (%) % 71 0 auto 2534 SU
Batch 5 6713835 * CEDA_MF_R261 C01227 0 2 Trend 5 Active pH pH 2 6,7 7,8 713 SU
Batch 6 6713845 * CEDA_MF_R262 C01227 0 2 Trend 6 pH-1 pH 120 6,7 7,8 2402 SU
Batch 7 6714717 * CEDA_MF_R264 C01227 0 2 Trend 7 Ammonia Feed Mass Flow (as is) kg/h 23 0 auto 636 SU
Batch 8 6735521 * CEDA_MF_R261 C01227 0 2 Trend 8 Ammonia Feed Totalizer (as is) kg 26 0 auto 1238 SU
Batch 9 6735527 * CEDA_MF_R262 C01227 0 2 Trend 9 Mixing Electrical Energy / Broth Mass kW/kg 107 0 auto 669 SU
Batch 10 6735528 * CEDA_MF_R263 C01227 0 2 Trend 10 Airflow (Nm3/h) Nm3/h 18 0 12000 2427 SU
Batch 11 6754076 * CEDA_MF_R261 C01026 0 2 Trend 11 Over Pressure bar 113 0 2,5 534 SU
Batch 12 6754078 * CEDA_MF_R262 C01026 0 2 Trend 12 kLA-1 1/h 101 0 2000 9071 SU
Batch 13 6754079 * CEDA_MF_R263 C01026 0 2 Trend 13 Total CTR mol/h 144 0 50000 2366 SU
Batch 14 6754080 * CEDA_MF_R264 C01026 0 2 Trend 14 Total OTR mol/h 146 0 auto 727 SU
Batch 15 6754081 * CEDA_MF_R261 C01026 0 2 Trend 15 VVM 1/min 149 0 auto 534 SU
Batch 16 6754082 * CEDA_MF_R262 C01026 0 2 Trend 16 Offgas %CO2 % 108 0 auto 668 SU
Batch 17 6754143 * CEDA_MF_R263 C01026 0 2 Trend 17 Offgas %O2 % 110 10 auto 2570 SU
Batch 18 6754158 * CEDA_MF_R264 C01026 0 2 Trend 18 Temperature Fermentation C 141 0 auto 660 SU
Batch 19 6754177 * CEDA_MF_R261 C01026 0 2 Trend 19 Broth Mass kg 40 0 auto 2427 SU
Batch 20 6754195 * CEDA_MF_R262 C01026 0 2 Trend 20 DCO2-1 - at probe level (mmol/kg) mmol/kg 66 0 auto 534 SU
Trend 21 Test 1 Unit 1 0 auto
0 = filled Trend 22 Test 2 Unit 2 0 auto
0,5 = semi-transparent Trend 23 Test 3 Unit 3 0 auto
1 = transparent Trend 24 Test 4 Unit 4 0 auto
Trend 25 Test 5 Unit 5 0 auto
1 = thin
Recalc Calculations
RecalcFind Batches
© Copyr i gh t 2014 O SIs o f t , LLC . 16
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50
100
150
200
250
300
350
400
m m
o l/
kg /h
p H
kg
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© Copyr i gh t 2014 O SIs o f t , LLC . 17
Batch Batch id Product Unit Product Color Transp. Line weight
Batch 1 6690337 * CEDA_MF_R261 C01227 0 1
Batch 2 6690342 * CEDA_MF_R262 C01227 0 1
Batch 3 6690345 * CEDA_MF_R263 C01227 0 1
Batch 4 6690346 * CEDA_MF_R264 C01227 0 1
Batch 5 6713835 * CEDA_MF_R261 C01227 0 1
Batch 6 6713845 * CEDA_MF_R262 C01227 0 1
Batch 7 6714717 * CEDA_MF_R264 C01227 0 5
Batch 8 6735521 * CEDA_MF_R261 C01227 0 1
Batch 9 6735527 * CEDA_MF_R262 C01227 0 1
Batch 10 6735528 * CEDA_MF_R263 C01227 0 1
Batch 11 6754076 * CEDA_MF_R261 C01026 0 1
Batch 12 6754078 * CEDA_MF_R262 C01026 0 1
Batch 13 6754079 * CEDA_MF_R263 C01026 0 1
Batch 14 6754080 * CEDA_MF_R264 C01026 0 1
Batch 15 6754081 * CEDA_MF_R261 C01026 0 1
Batch 16 6754082 * CEDA_MF_R262 C01026 0 1
Batch 17 6754143 * CEDA_MF_R263 C01026 0 1
Batch 18 6754158 * CEDA_MF_R264 C01026 0 1
Batch 19 6754177 * CEDA_MF_R261 C01026 0 1
Batch 20 6754195 * CEDA_MF_R262 C01026 0 1
© Copyr i gh t 2014 O SIs o f t , LLC . 18
0
50
100
150
200
250
300
350
400
m m
o l/
kg /h
p H
kg
<No Results Found>
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Elapsed Time (h)
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© Copyr i gh t 2014 O SIs o f t , LLC .
Future plans
19
© Copyr i gh t 2014 O SIs o f t , LLC . 20
Questions
name &
company
© Copyr i gh t 2014 O SIs o f t , LLC .
Brought to you by
© Copyr i gh t 2014 O SIs o f t , LLC .
Please don’t forget to… Complete the online survey for
this session
Presented by
Improving Process
Performance Across
Peter Lundqvist, Mathias Holmgård
© Copyr i gh t 2014 O SIs o f t , LLC .
Peter Lundqvist
© Copyr i gh t 2014 O SIs o f t , LLC .
Mathias Holmgård
© Copyr i gh t 2014 O SIs o f t , LLC .
Contents of todays talk
server concept.
sites can now be made in minutes instead of
days.
4
© Copyr i gh t 2014 O SIs o f t , LLC .
Global Science Company with a Broad Portfolio
5
© Copyr i gh t 2014 O SIs o f t , LLC . 6
© Copyr i gh t 2014 O SIs o f t , LLC .
Manufacturing set-up
- Different colors illustrates different platforms (approximated)
- Number of dots illustrates on a relative basis number of runs (not based on
actuals)
Plant E Plant F Plant G Pilot scale
= engineers
© Copyr i gh t 2014 O SIs o f t , LLC .
Reasons for a central PI Server
• WAN traffic site-to-site slow
– Unrealistic to pull the data from each sites PI Server
– PI Batch performance an issue
• Easiest way to fix was installing a Central PI Server
pulling the needed data from the sites
8
© Copyr i gh t 2014 O SIs o f t , LLC .
Architecture of the Central PI Server solution
– One PI to PI Interface on the Central PI Server
• One instance per Production Site pulling data
• Data is converted to SI units on the local PI Server before
transfer
• PI Asset Framework (PI AF) for configuration
• PI Batch for batches
9
© Copyr i gh t 2014 O SIs o f t , LLC .
Structure of Excel tool
End Time
Excel Trends
Measurements Aliases
© Copyr i gh t 2014 O SIs o f t , LLC . 11
Time *-350d * Time incr. 00:06:00 360,00 360s File version : 2014_02_26, PLu
Unit *MF* 2 PI server gcorpp01 BAC
Phase to plot Fermentation 2 Process Fermentation
Batch Batch id Product Unit Product Color Transp. Line weight Trend Alias Unit Y-min Y-max
Batch 1 - * 0 2 Trend 1 OTR mmol/kg/h 112 0 400 2402 SU
Batch 2 - * 0 2 Trend 2 CTR mmol/kg/h 65 0 400 17598 SU
Batch 3 - * 0 2 Trend 3 Carbon-source 1 Feed Mass Flow (as is) kg/h 52 0 auto 2450 SU
Batch 4 - * 0 2 Trend 4 DO2-2 (%) % 71 0 auto 2534 SU
Batch 5 - * 0 2 Trend 5 Active pH pH 2 6,7 7,8 713 SU
Batch 6 - * 0 2 Trend 6 pH-1 pH 120 6,7 7,8 2402 SU
Batch 7 - * 0 2 Trend 7 Ammonia Feed Mass Flow (as is) kg/h 23 0 auto 636 SU
Batch 8 - * 0 2 Trend 8 Ammonia Feed Totalizer (as is) kg 26 0 auto 1238 SU
Batch 9 - * 0 2 Trend 9 Mixing Electrical Energy / Broth Mass kW/kg 107 0 auto 669 SU
Batch 10 - * 0 2 Trend 10 Airflow (Nm3/h) Nm3/h 18 0 12000 2427 SU
Batch 11 - * 0 2 Trend 11 Over Pressure bar 113 0 2,5 534 SU
Batch 12 - * 0 2 Trend 12 kLA-1 1/h 101 0 2000 9071 SU
Batch 13 - * 0 2 Trend 13 Total CTR mol/h 144 0 50000 2366 SU
Batch 14 - * 0 2 Trend 14 Total OTR mol/h 146 0 auto 727 SU
Batch 15 - * 0 2 Trend 15 VVM 1/min 149 0 auto 534 SU
Batch 16 - * 0 2 Trend 16 Offgas %CO2 % 108 0 auto 668 SU
Batch 17 - * 0 2 Trend 17 Offgas %O2 % 110 10 auto 2570 SU
Batch 18 - * 0 2 Trend 18 Temperature Fermentation C 141 0 auto 660 SU
Batch 19 - * 0 2 Trend 19 Broth Mass kg 40 0 auto 2427 SU
Batch 20 - * 0 2 Trend 20 DCO2-1 - at probe level (mmol/kg) mmol/kg 66 0 auto 534 SU
Trend 21 Test 1 Unit 1 0 auto
0 = filled Trend 22 Test 2 Unit 2 0 auto
0,5 = semi-transparent Trend 23 Test 3 Unit 3 0 auto
1 = transparent Trend 24 Test 4 Unit 4 0 auto
Trend 25 Test 5 Unit 5 0 auto
1 = thin
Recalc Calculations
RecalcFind Batches
© Copyr i gh t 2014 O SIs o f t , LLC . 12
Time *-350d * Time incr. 00:06:00 360,00 360s File version : 2014_02_26, PLu
Unit *MF* 2 PI server gcorpp01 BAC
Phase to plot Fermentation 2 Process Fermentation
Batch Batch id Product Unit Product Color Transp. Line weight Trend Alias Unit Y-min Y-max
Batch 1 - * 0 2 Trend 1 OTR mmol/kg/h 112 0 400 2402 SU
Batch 2 - * 0 2 Trend 2 CTR mmol/kg/h 65 0 400 17598 SU
Batch 3 - * 0 2 Trend 3 Carbon-source 1 Feed Mass Flow (as is) kg/h 52 0 auto 2450 SU
Batch 4 - * 0 2 Trend 4 DO2-2 (%) % 71 0 auto 2534 SU
Batch 5 - * 0 2 Trend 5 Active pH pH 2 6,7 7,8 713 SU
Batch 6 - * 0 2 Trend 6 pH-1 pH 120 6,7 7,8 2402 SU
Batch 7 - * 0 2 Trend 7 Ammonia Feed Mass Flow (as is) kg/h 23 0 auto 636 SU
Batch 8 - * 0 2 Trend 8 Ammonia Feed Totalizer (as is) kg 26 0 auto 1238 SU
Batch 9 - * 0 2 Trend 9 Mixing Electrical Energy / Broth Mass kW/kg 107 0 auto 669 SU
Batch 10 - * 0 2 Trend 10 Airflow (Nm3/h) Nm3/h 18 0 12000 2427 SU
Batch 11 - * 0 2 Trend 11 Over Pressure bar 113 0 2,5 534 SU
Batch 12 - * 0 2 Trend 12 kLA-1 1/h 101 0 2000 9071 SU
Batch 13 - * 0 2 Trend 13 Total CTR mol/h 144 0 50000 2366 SU
Batch 14 - * 0 2 Trend 14 Total OTR mol/h 146 0 auto 727 SU
Batch 15 - * 0 2 Trend 15 VVM 1/min 149 0 auto 534 SU
Batch 16 - * 0 2 Trend 16 Offgas %CO2 % 108 0 auto 668 SU
Batch 17 - * 0 2 Trend 17 Offgas %O2 % 110 10 auto 2570 SU
Batch 18 - * 0 2 Trend 18 Temperature Fermentation C 141 0 auto 660 SU
Batch 19 - * 0 2 Trend 19 Broth Mass kg 40 0 auto 2427 SU
Batch 20 - * 0 2 Trend 20 DCO2-1 - at probe level (mmol/kg) mmol/kg 66 0 auto 534 SU
Trend 21 Test 1 Unit 1 0 auto
0 = filled Trend 22 Test 2 Unit 2 0 auto
0,5 = semi-transparent Trend 23 Test 3 Unit 3 0 auto
1 = transparent Trend 24 Test 4 Unit 4 0 auto
Trend 25 Test 5 Unit 5 0 auto
1 = thin
areas
© Copyr i gh t 2014 O SIs o f t , LLC . 13
Time *-350d * Time incr. 00:06:00 360,00 360s File version : 2014_02_26, PLu
Unit *MF* 2 PI server gcorpp01 BAC
Phase to plot Fermentation 2 Process Fermentation
Batch Batch id Product Unit Product Color Transp. Line weight Trend Alias Unit Y-min Y-max
Batch 1 6690337 * 0 2 Trend 1 OTR mmol/kg/h 112 0 400 2402 SU
Batch 2 6690342 * 0 2 Trend 2 CTR mmol/kg/h 65 0 400 17598 SU
Batch 3 6690345 * 0 2 Trend 3 Carbon-source 1 Feed Mass Flow (as is) kg/h 52 0 auto 2450 SU
Batch 4 6690346 * 0 2 Trend 4 DO2-2 (%) % 71 0 auto 2534 SU
Batch 5 6713835 * 0 2 Trend 5 Active pH pH 2 6,7 7,8 713 SU
Batch 6 6713845 * 0 2 Trend 6 pH-1 pH 120 6,7 7,8 2402 SU
Batch 7 6714717 * 0 2 Trend 7 Ammonia Feed Mass Flow (as is) kg/h 23 0 auto 636 SU
Batch 8 6735521 * 0 2 Trend 8 Ammonia Feed Totalizer (as is) kg 26 0 auto 1238 SU
Batch 9 6735527 * 0 2 Trend 9 Mixing Electrical Energy / Broth Mass kW/kg 107 0 auto 669 SU
Batch 10 6735528 * 0 2 Trend 10 Airflow (Nm3/h) Nm3/h 18 0 12000 2427 SU
Batch 11 6754076 * 0 2 Trend 11 Over Pressure bar 113 0 2,5 534 SU
Batch 12 6754078 * 0 2 Trend 12 kLA-1 1/h 101 0 2000 9071 SU
Batch 13 6754079 * 0 2 Trend 13 Total CTR mol/h 144 0 50000 2366 SU
Batch 14 6754080 * 0 2 Trend 14 Total OTR mol/h 146 0 auto 727 SU
Batch 15 6754081 * 0 2 Trend 15 VVM 1/min 149 0 auto 534 SU
Batch 16 6754082 * 0 2 Trend 16 Offgas %CO2 % 108 0 auto 668 SU
Batch 17 6754143 * 0 2 Trend 17 Offgas %O2 % 110 10 auto 2570 SU
Batch 18 6754158 * 0 2 Trend 18 Temperature Fermentation C 141 0 auto 660 SU
Batch 19 6754177 * 0 2 Trend 19 Broth Mass kg 40 0 auto 2427 SU
Batch 20 6754195 * 0 2 Trend 20 DCO2-1 - at probe level (mmol/kg) mmol/kg 66 0 auto 534 SU
Trend 21 Test 1 Unit 1 0 auto
0 = filled Trend 22 Test 2 Unit 2 0 auto
0,5 = semi-transparent Trend 23 Test 3 Unit 3 0 auto
1 = transparent Trend 24 Test 4 Unit 4 0 auto
Trend 25 Test 5 Unit 5 0 auto
1 = thin
Recalc Calculations
RecalcFind Batches
© Copyr i gh t 2014 O SIs o f t , LLC . 14
Time *-350d * Time incr. 00:06:00 360,00 360s File version : 2014_02_26, PLu
Unit *MF* 2 PI server gcorpp01 BAC
Phase to plot Fermentation 2 Process Fermentation
Batch Batch id Product Unit Product Color Transp. Line weight Trend Alias Unit Y-min Y-max
Batch 1 6690337 * CEDA_MF_R261 C01227 0 2 Trend 1 OTR mmol/kg/h 112 0 400 2402 SU
Batch 2 6690342 * CEDA_MF_R262 C01227 0 2 Trend 2 CTR mmol/kg/h 65 0 400 17598 SU
Batch 3 6690345 * CEDA_MF_R263 C01227 0 2 Trend 3 Carbon-source 1 Feed Mass Flow (as is) kg/h 52 0 auto 2450 SU
Batch 4 6690346 * CEDA_MF_R264 C01227 0 2 Trend 4 DO2-2 (%) % 71 0 auto 2534 SU
Batch 5 6713835 * CEDA_MF_R261 C01227 0 2 Trend 5 Active pH pH 2 6,7 7,8 713 SU
Batch 6 6713845 * CEDA_MF_R262 C01227 0 2 Trend 6 pH-1 pH 120 6,7 7,8 2402 SU
Batch 7 6714717 * CEDA_MF_R264 C01227 0 2 Trend 7 Ammonia Feed Mass Flow (as is) kg/h 23 0 auto 636 SU
Batch 8 6735521 * CEDA_MF_R261 C01227 0 2 Trend 8 Ammonia Feed Totalizer (as is) kg 26 0 auto 1238 SU
Batch 9 6735527 * CEDA_MF_R262 C01227 0 2 Trend 9 Mixing Electrical Energy / Broth Mass kW/kg 107 0 auto 669 SU
Batch 10 6735528 * CEDA_MF_R263 C01227 0 2 Trend 10 Airflow (Nm3/h) Nm3/h 18 0 12000 2427 SU
Batch 11 6754076 * CEDA_MF_R261 C01026 0 2 Trend 11 Over Pressure bar 113 0 2,5 534 SU
Batch 12 6754078 * CEDA_MF_R262 C01026 0 2 Trend 12 kLA-1 1/h 101 0 2000 9071 SU
Batch 13 6754079 * CEDA_MF_R263 C01026 0 2 Trend 13 Total CTR mol/h 144 0 50000 2366 SU
Batch 14 6754080 * CEDA_MF_R264 C01026 0 2 Trend 14 Total OTR mol/h 146 0 auto 727 SU
Batch 15 6754081 * CEDA_MF_R261 C01026 0 2 Trend 15 VVM 1/min 149 0 auto 534 SU
Batch 16 6754082 * CEDA_MF_R262 C01026 0 2 Trend 16 Offgas %CO2 % 108 0 auto 668 SU
Batch 17 6754143 * CEDA_MF_R263 C01026 0 2 Trend 17 Offgas %O2 % 110 10 auto 2570 SU
Batch 18 6754158 * CEDA_MF_R264 C01026 0 2 Trend 18 Temperature Fermentation C 141 0 auto 660 SU
Batch 19 6754177 * CEDA_MF_R261 C01026 0 2 Trend 19 Broth Mass kg 40 0 auto 2427 SU
Batch 20 6754195 * CEDA_MF_R262 C01026 0 2 Trend 20 DCO2-1 - at probe level (mmol/kg) mmol/kg 66 0 auto 534 SU
Trend 21 Test 1 Unit 1 0 auto
0 = filled Trend 22 Test 2 Unit 2 0 auto
0,5 = semi-transparent Trend 23 Test 3 Unit 3 0 auto
1 = transparent Trend 24 Test 4 Unit 4 0 auto
Trend 25 Test 5 Unit 5 0 auto
1 = thin
Recalc Calculations
RecalcFind Batches
© Copyr i gh t 2014 O SIs o f t , LLC . 15
Time *-350d * Time incr. 00:06:00 360,00 360s File version : 2014_02_26, PLu
Unit *MF* 2 PI server gcorpp01 BAC
Phase to plot Fermentation 2 Process Fermentation
Batch Batch id Product Unit Product Color Transp. Line weight Trend Alias Unit Y-min Y-max
Batch 1 6690337 * CEDA_MF_R261 C01227 0 2 Trend 1 OTR mmol/kg/h 112 0 400 2402 SU
Batch 2 6690342 * CEDA_MF_R262 C01227 0 2 Trend 2 CTR mmol/kg/h 65 0 400 17598 SU
Batch 3 6690345 * CEDA_MF_R263 C01227 0 2 Trend 3 Carbon-source 1 Feed Mass Flow (as is) kg/h 52 0 auto 2450 SU
Batch 4 6690346 * CEDA_MF_R264 C01227 0 2 Trend 4 DO2-2 (%) % 71 0 auto 2534 SU
Batch 5 6713835 * CEDA_MF_R261 C01227 0 2 Trend 5 Active pH pH 2 6,7 7,8 713 SU
Batch 6 6713845 * CEDA_MF_R262 C01227 0 2 Trend 6 pH-1 pH 120 6,7 7,8 2402 SU
Batch 7 6714717 * CEDA_MF_R264 C01227 0 2 Trend 7 Ammonia Feed Mass Flow (as is) kg/h 23 0 auto 636 SU
Batch 8 6735521 * CEDA_MF_R261 C01227 0 2 Trend 8 Ammonia Feed Totalizer (as is) kg 26 0 auto 1238 SU
Batch 9 6735527 * CEDA_MF_R262 C01227 0 2 Trend 9 Mixing Electrical Energy / Broth Mass kW/kg 107 0 auto 669 SU
Batch 10 6735528 * CEDA_MF_R263 C01227 0 2 Trend 10 Airflow (Nm3/h) Nm3/h 18 0 12000 2427 SU
Batch 11 6754076 * CEDA_MF_R261 C01026 0 2 Trend 11 Over Pressure bar 113 0 2,5 534 SU
Batch 12 6754078 * CEDA_MF_R262 C01026 0 2 Trend 12 kLA-1 1/h 101 0 2000 9071 SU
Batch 13 6754079 * CEDA_MF_R263 C01026 0 2 Trend 13 Total CTR mol/h 144 0 50000 2366 SU
Batch 14 6754080 * CEDA_MF_R264 C01026 0 2 Trend 14 Total OTR mol/h 146 0 auto 727 SU
Batch 15 6754081 * CEDA_MF_R261 C01026 0 2 Trend 15 VVM 1/min 149 0 auto 534 SU
Batch 16 6754082 * CEDA_MF_R262 C01026 0 2 Trend 16 Offgas %CO2 % 108 0 auto 668 SU
Batch 17 6754143 * CEDA_MF_R263 C01026 0 2 Trend 17 Offgas %O2 % 110 10 auto 2570 SU
Batch 18 6754158 * CEDA_MF_R264 C01026 0 2 Trend 18 Temperature Fermentation C 141 0 auto 660 SU
Batch 19 6754177 * CEDA_MF_R261 C01026 0 2 Trend 19 Broth Mass kg 40 0 auto 2427 SU
Batch 20 6754195 * CEDA_MF_R262 C01026 0 2 Trend 20 DCO2-1 - at probe level (mmol/kg) mmol/kg 66 0 auto 534 SU
Trend 21 Test 1 Unit 1 0 auto
0 = filled Trend 22 Test 2 Unit 2 0 auto
0,5 = semi-transparent Trend 23 Test 3 Unit 3 0 auto
1 = transparent Trend 24 Test 4 Unit 4 0 auto
Trend 25 Test 5 Unit 5 0 auto
1 = thin
Recalc Calculations
RecalcFind Batches
© Copyr i gh t 2014 O SIs o f t , LLC . 16
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© Copyr i gh t 2014 O SIs o f t , LLC . 17
Batch Batch id Product Unit Product Color Transp. Line weight
Batch 1 6690337 * CEDA_MF_R261 C01227 0 1
Batch 2 6690342 * CEDA_MF_R262 C01227 0 1
Batch 3 6690345 * CEDA_MF_R263 C01227 0 1
Batch 4 6690346 * CEDA_MF_R264 C01227 0 1
Batch 5 6713835 * CEDA_MF_R261 C01227 0 1
Batch 6 6713845 * CEDA_MF_R262 C01227 0 1
Batch 7 6714717 * CEDA_MF_R264 C01227 0 5
Batch 8 6735521 * CEDA_MF_R261 C01227 0 1
Batch 9 6735527 * CEDA_MF_R262 C01227 0 1
Batch 10 6735528 * CEDA_MF_R263 C01227 0 1
Batch 11 6754076 * CEDA_MF_R261 C01026 0 1
Batch 12 6754078 * CEDA_MF_R262 C01026 0 1
Batch 13 6754079 * CEDA_MF_R263 C01026 0 1
Batch 14 6754080 * CEDA_MF_R264 C01026 0 1
Batch 15 6754081 * CEDA_MF_R261 C01026 0 1
Batch 16 6754082 * CEDA_MF_R262 C01026 0 1
Batch 17 6754143 * CEDA_MF_R263 C01026 0 1
Batch 18 6754158 * CEDA_MF_R264 C01026 0 1
Batch 19 6754177 * CEDA_MF_R261 C01026 0 1
Batch 20 6754195 * CEDA_MF_R262 C01026 0 1
© Copyr i gh t 2014 O SIs o f t , LLC . 18
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© Copyr i gh t 2014 O SIs o f t , LLC .
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