SlideShare a Scribd company logo
1 of 30
“Say When” Sweet
Tea
Sweetness Control
Group 19:
Samantha Butler
Noah Van Ryn
Michael DePietro
Objectives
-To design and build a system that controls the sweetness,through sugar
concentration, of sweet tea
Block Diagram
Hardware
Hardware (Sensors)
-Load Cell
-Flow Meter (removed)
Hardware con’t (Actuators)
-Pump
-Stepper Motor (Auger System)
Hardware concl (Controller)
Albert II
The Pump Calibration/Step Changes
Stepper Motor Calibration/Step Test
Time Target = 0.1 to 0.03
𝝉 = 82.504s
Load Cell Calibrations/Step Tests
Simulation vs
Real Process
Who will emerge
victorious?
Process Model
-Simulation VI
Final Project VI
Model Compared to System (Gp)
Simulation Physical Change in Manipulated Variable
Simulation of Process compared to Real
System
Simulation Tuned System
Simulation of Process compared to Real
System con’t (Step Test)
Simulation
Tuned System
Tuning Strategy
Tuning our System Proportional Control First Attempt
Rise Time = 60s
Offset difference = 25 (g/L)
Control Effort saturates at at 40s
Tuning Our System Proportional Control Second
Attempt
Rise Time = 68s
Offset Differences = 11 g/L
Control Effort does not show any saturation
Tuning Our System Proportional Control Third
Attempt
Rise Time - N/A
Offset Difference - 75 g/L Control Effort immediately saturates and
the auger did not move
Tuning Our System PI Control First Attempt
Rise Time - 37s
Offset difference - 56 g/L
Control effort is stable at 0.045 until 8s and
then saturates at 13s and auger stops
working.
Tuning Our System PI Control Second Attempt
Rise time - 83s
Overshoot - 1.16
Control effort heads toward saturation at
7s but works its way back up around 80s
Tuning Our System PI Control Third Attempt
Rise Time - 183s
System stayed at setpoint for 30s
Control Effort does not saturate and
remains stable
Setpoint Change - Raising Setpoint
Time to reach new setpoint:
120 s
Setpoint Change - Lowering Setpoint
Time to reach setpoint - 100 s
Disturbance - Load Cell
Jump in Concentration - 69 g/L to 147 g/L
Time to Return to Setpoint - 210 s
Final Thoughts
Challenges
1. Not able to directly measure sugar concentration
2. Building around the load cell
a. Placement of hot plate
b. How to build a platform on load cell
c. Determining our batch size
3. Flow meter
4. Pump start up
5. The ALBERT II
6. How to dissolve sugar
7. PID tuning
VI Improvements
-Add a sequence structure to the VI that will turn off the pump and load cell once
the PID system is turned off
-Find a way to tare the load cell at the beginning of each batch
-Program the system so that the auger and pump turn on simultaneously instead of
turning them both in separately
- Find a way to incorporate the flow meter
- Figure out why we couldn’t start with an integral time right away
Hardware Improvements
-Develop a way to more permanently attach the auger screw to the stepper motor
-Develop a method that allows for aggressive agitation of the brewing vessel in
order to increase the rate at which sugar dissolves into the unsweetened tea
-Stronger pump for faster addition of unsweetened tea
-Stop sugar from escaping out the back of the system and prevent it from getting
into the auger shaft
Conclusion
-We feel that our project performed in a satisfactory manner.
-We were able to complete all of our goals, namely we were able to control the
sugar concentration of a batch of sweet tea.

More Related Content

What's hot (8)

Regulator – inspection & testing
Regulator – inspection & testingRegulator – inspection & testing
Regulator – inspection & testing
 
Lpg reticulated gas system (cylinder bank) digital energy
Lpg reticulated gas system (cylinder bank) digital energyLpg reticulated gas system (cylinder bank) digital energy
Lpg reticulated gas system (cylinder bank) digital energy
 
Synchronising the 210MW unit to the 220KV grid
Synchronising the 210MW unit to the 220KV gridSynchronising the 210MW unit to the 220KV grid
Synchronising the 210MW unit to the 220KV grid
 
Renovation
RenovationRenovation
Renovation
 
Principle of operation bowl mill
Principle of operation bowl millPrinciple of operation bowl mill
Principle of operation bowl mill
 
THERMAL POWER PLANT OPERATIONS
THERMAL POWER PLANT OPERATIONSTHERMAL POWER PLANT OPERATIONS
THERMAL POWER PLANT OPERATIONS
 
Breakdown of Eco-Friendly Shipping
Breakdown of Eco-Friendly ShippingBreakdown of Eco-Friendly Shipping
Breakdown of Eco-Friendly Shipping
 
drain pit(1)
drain pit(1)drain pit(1)
drain pit(1)
 

Viewers also liked

SelectJobs - Presentation for Induction
SelectJobs - Presentation for InductionSelectJobs - Presentation for Induction
SelectJobs - Presentation for Induction
Select Jobs
 
historia del carnaval
historia del carnavalhistoria del carnaval
historia del carnaval
patGM
 
Tecnologias na educação atividade 4
Tecnologias na educação atividade 4Tecnologias na educação atividade 4
Tecnologias na educação atividade 4
waleriadonizetti
 
Catarina do 7º1
Catarina do 7º1Catarina do 7º1
Catarina do 7º1
Mayjö .
 

Viewers also liked (12)

Turismo
TurismoTurismo
Turismo
 
RESUME
RESUMERESUME
RESUME
 
SelectJobs - Presentation for Induction
SelectJobs - Presentation for InductionSelectJobs - Presentation for Induction
SelectJobs - Presentation for Induction
 
Act 12 equipo
Act 12 equipoAct 12 equipo
Act 12 equipo
 
Aula segundo sexo (1)
Aula segundo sexo (1)Aula segundo sexo (1)
Aula segundo sexo (1)
 
Journalisme de marque et légitimités iscpa nov 2010
 Journalisme de marque et légitimités iscpa nov 2010 Journalisme de marque et légitimités iscpa nov 2010
Journalisme de marque et légitimités iscpa nov 2010
 
historia del carnaval
historia del carnavalhistoria del carnaval
historia del carnaval
 
Logos
LogosLogos
Logos
 
Tecnologias na educação atividade 4
Tecnologias na educação atividade 4Tecnologias na educação atividade 4
Tecnologias na educação atividade 4
 
Real Estate Investing 101: Leasing
Real Estate Investing 101: LeasingReal Estate Investing 101: Leasing
Real Estate Investing 101: Leasing
 
Butler e Bourcier
Butler e BourcierButler e Bourcier
Butler e Bourcier
 
Catarina do 7º1
Catarina do 7º1Catarina do 7º1
Catarina do 7º1
 

Similar to “Say When” Sweet Tea Sweetness Control

Project-Final-Report
Project-Final-ReportProject-Final-Report
Project-Final-Report
Andrew Wu
 
CEIE 440-540 – Homework HW#09 Assignment Assign.docx
CEIE 440-540 – Homework   HW#09 Assignment  Assign.docxCEIE 440-540 – Homework   HW#09 Assignment  Assign.docx
CEIE 440-540 – Homework HW#09 Assignment Assign.docx
zebadiahsummers
 
CEIE 440-540 – Homework HW#09 Assignment Assign.docx
CEIE 440-540 – Homework   HW#09 Assignment  Assign.docxCEIE 440-540 – Homework   HW#09 Assignment  Assign.docx
CEIE 440-540 – Homework HW#09 Assignment Assign.docx
keturahhazelhurst
 
Increasing economy of scope by increasing throughput
Increasing economy of scope by increasing throughputIncreasing economy of scope by increasing throughput
Increasing economy of scope by increasing throughput
Tobey Houston
 
Development of improved pid controller for single effect evaporator
Development of improved pid controller for single effect evaporatorDevelopment of improved pid controller for single effect evaporator
Development of improved pid controller for single effect evaporator
eSAT Journals
 

Similar to “Say When” Sweet Tea Sweetness Control (20)

Full report of hyperglass cleaner
Full report of hyperglass cleanerFull report of hyperglass cleaner
Full report of hyperglass cleaner
 
Full report of hyperglass cleaner
Full report of hyperglass cleanerFull report of hyperglass cleaner
Full report of hyperglass cleaner
 
Functional Design Specification of Hyperglass Cleaning
Functional Design Specification of Hyperglass CleaningFunctional Design Specification of Hyperglass Cleaning
Functional Design Specification of Hyperglass Cleaning
 
Commissioning highly interactive process an approach for tuning control loops
Commissioning highly interactive process an approach for tuning control loopsCommissioning highly interactive process an approach for tuning control loops
Commissioning highly interactive process an approach for tuning control loops
 
Project-Final-Report
Project-Final-ReportProject-Final-Report
Project-Final-Report
 
Block diagrams
Block diagramsBlock diagrams
Block diagrams
 
CEIE 440-540 – Homework HW#09 Assignment Assign.docx
CEIE 440-540 – Homework   HW#09 Assignment  Assign.docxCEIE 440-540 – Homework   HW#09 Assignment  Assign.docx
CEIE 440-540 – Homework HW#09 Assignment Assign.docx
 
CEIE 440-540 – Homework HW#09 Assignment Assign.docx
CEIE 440-540 – Homework   HW#09 Assignment  Assign.docxCEIE 440-540 – Homework   HW#09 Assignment  Assign.docx
CEIE 440-540 – Homework HW#09 Assignment Assign.docx
 
Industrial automation (cold drink factory)
Industrial automation (cold drink factory)Industrial automation (cold drink factory)
Industrial automation (cold drink factory)
 
Automated Coffee machine
Automated Coffee machineAutomated Coffee machine
Automated Coffee machine
 
PSI Engineering Systems - product presentation
PSI Engineering Systems - product presentation PSI Engineering Systems - product presentation
PSI Engineering Systems - product presentation
 
Scale up of fermentation
Scale up of fermentationScale up of fermentation
Scale up of fermentation
 
Unit I IPII.pdf
Unit I IPII.pdfUnit I IPII.pdf
Unit I IPII.pdf
 
Al moiz unit-ii presentation
Al moiz unit-ii presentation Al moiz unit-ii presentation
Al moiz unit-ii presentation
 
Cooling tower management
Cooling tower managementCooling tower management
Cooling tower management
 
In Apc Training Presentation
In  Apc Training PresentationIn  Apc Training Presentation
In Apc Training Presentation
 
Design Compensator Using Automated PID Tuning for a water tank
Design Compensator Using Automated PID Tuning for a water tank Design Compensator Using Automated PID Tuning for a water tank
Design Compensator Using Automated PID Tuning for a water tank
 
Small Scale Automatic Jaggery Production(AJP) System
Small Scale Automatic Jaggery Production(AJP) SystemSmall Scale Automatic Jaggery Production(AJP) System
Small Scale Automatic Jaggery Production(AJP) System
 
Increasing economy of scope by increasing throughput
Increasing economy of scope by increasing throughputIncreasing economy of scope by increasing throughput
Increasing economy of scope by increasing throughput
 
Development of improved pid controller for single effect evaporator
Development of improved pid controller for single effect evaporatorDevelopment of improved pid controller for single effect evaporator
Development of improved pid controller for single effect evaporator
 

“Say When” Sweet Tea Sweetness Control

Editor's Notes

  1. Sam
  2. Michael explain why the frame is the way it is
  3. Michael had to use the squarejoints becasue the drill piece that is used to thread the metal was broken
  4. Noah Pump- buildup time Auger - 2 parts, screw and stepper motor, pump given constant voltage, stepper motor given pulses
  5. Sam
  6. Sam
  7. Noah Inverse time target - same as frequency, gives linear equation Large tau value due in part to method of measuring flow rate - load cell has own tau value
  8. Michael Load cell gain around the 1180 range Used a 200 ohm resistor to increase the sensitivity
  9. Michael
  10. Michael
  11. Noah - block diagram, Sam - Front Panel
  12. Michael
  13. Sam
  14. Noah Difference due to limitations of stepper motor
  15. Michael
  16. Sam
  17. Sam
  18. Sam
  19. Sam
  20. Sam
  21. Sam
  22. Noah Drop in control effort (period)
  23. Noah Rise in Control effort
  24. Noah
  25. Noah Got around by subtraction, difference in masses Brew location/single screw applying a moment/limitations of load cell Couldn’t get the flow meter to work fed into ln eqn made sure all connections were good heating/stirring discuss strategy again
  26. Sam
  27. Michael DePietro