ikwesi is a mobile sharing platform that send vital and exciting information alerts to its users. It runs on a website portal which connects users to the platform.
Maximizing the return on your control investment meet the experts sessions pa...Emerson Exchange
The design and commissioning of the controls associated with a continuous or batch process directly impact plant operating efficiency and production quality and throughput. In this session we review techniques that may be used to identify control opportunities to reduce production costs, minimize variations in product quality and to maximize production within the limits set by market demand. Several common application examples from the process industry will be used to illustrate how plant production rate and product quality are directly influenced by process control variation and constraints in plant operation. Starting with an assessment of control loop utilization and automatic control performance, a step by step process is outlined that may be used to identifying and addressing areas where it is possible to justified the time and material costs required to improve control performance. In particular, information will be provided on how to quickly tune single loop control of self-regulating or integrating process and to recognize when variations in control loop performance are not associated with loop tuning. An overview will be provided of tools and techniques that may be used to achieve best control performance over a wide variety of operating conditions. Also, guidance will be provided on when it is possible to justify the cost associated with the installation and commissioning of multi-loop techniques such as feedforward control, ratio and override control. The steps required to commission multi-loop control strategies will be address along with common mistakes to avoid. Also, input will be provided on how to recognize when advanced control techniques such as Fuzzy logic or MPC are needed to achieve the desired control performance. At the end of this session a drawing will be held to give away 10 copies of “Control Loop Foundation – Batch and Continuous Processes”. Many of the ideas discussed in this session are addressed in this book.
ikwesi is a mobile sharing platform that send vital and exciting information alerts to its users. It runs on a website portal which connects users to the platform.
Maximizing the return on your control investment meet the experts sessions pa...Emerson Exchange
The design and commissioning of the controls associated with a continuous or batch process directly impact plant operating efficiency and production quality and throughput. In this session we review techniques that may be used to identify control opportunities to reduce production costs, minimize variations in product quality and to maximize production within the limits set by market demand. Several common application examples from the process industry will be used to illustrate how plant production rate and product quality are directly influenced by process control variation and constraints in plant operation. Starting with an assessment of control loop utilization and automatic control performance, a step by step process is outlined that may be used to identifying and addressing areas where it is possible to justified the time and material costs required to improve control performance. In particular, information will be provided on how to quickly tune single loop control of self-regulating or integrating process and to recognize when variations in control loop performance are not associated with loop tuning. An overview will be provided of tools and techniques that may be used to achieve best control performance over a wide variety of operating conditions. Also, guidance will be provided on when it is possible to justify the cost associated with the installation and commissioning of multi-loop techniques such as feedforward control, ratio and override control. The steps required to commission multi-loop control strategies will be address along with common mistakes to avoid. Also, input will be provided on how to recognize when advanced control techniques such as Fuzzy logic or MPC are needed to achieve the desired control performance. At the end of this session a drawing will be held to give away 10 copies of “Control Loop Foundation – Batch and Continuous Processes”. Many of the ideas discussed in this session are addressed in this book.
5. Why Not A Hardly Used Category?
• Actual operation is less than 10% of:
– Emissions (PTE)
– Fuel Usage
– Capacity Factor
– 3-year average of hours of operation
6. Emission Limits
Emissions Must Not Exceed, except
Pollutant
during startup and shutdown…
CO 10 ppmvd @ 3% O2
PM 0.0075 lb/MMBtu
HCl 0.00033 lb/MMBtu
Hg 3.6 × 10-6 lb/MMBtu
D/F 4 ng/dscm (corrected to 7% O2)
7. Carbon Monoxide
• EPA Database
– Results range from 1.67 ppm to 700+ ppm
• 58 Stack Tests
– 8 Below 10 ppm
– 27 reported at 100 ppm (Detection Limit?)
9. Control Options
• Gas is King!
– Only Requirement is an Annual Tune-Up
– No Emission Limits for Gas
– No Annual Stack Tests or Fuel Analyses
– No Requirement for an “Energy Assessment”
– Conversion Costs Only $300,000
– Future Gas will be Cheap, Right?
16. Malfunction Abatement Plan
• Focus on Detailed Summary Tables
– Less on Lengthy Narratives That
Most Will Probably Not Read
• Summary Tables – Simplifies MAP
Requirements for Plant Staff and
AQD Personnel
17. Preventive Maintenance (Baghouse)
Control Device Spare Parts on
PM Activity Daily Weekly Annually
(Emission Unit) Hand
CE004 (baghouse)
Visible
Check photohelic Replacement
Emissions,
gauge for proper belts, Bearings,
CE008 (baghouse) Visual Non-certified Check oil /
operation and and Filter bags
Inspections, VE readings replace bags
pressure drop for each
Maintenance
range Baghouse model
Activities
CE010 (baghouse)
18. Malfunction Response (Baghouse)
Possible Corrective Steps to
Control Device Operating Parameter
Malfunction Possible Malfunctions Return Unit to Proper
(Emission Unit) Parameters Range
Detection Operation
Unit will be brought off-
0 - 20% Visible Emission Bag(s) may have failed or
Baghouses Opacity line and the bags
max. exceed 20% are not properly seated
checked
Unit will be brought off-
One or more bags may
CE004 line and the bags
be plugged or blinded
checked
Unit will be brought off-
Air to the cleaning jets line and air pulse
CE008 Differential 0.5 - 5" Pressure drop
maybe plugged cleaning system will be
Pressure water above 5"
inspected
Maintain spare
Magnehelic unit may
CE010 magnehelic gauge for
have failed
possible replacement
19. Preventive Maintenance (Scrubber)
Control Device Spare Parts on
PM Activity Daily Weekly Monthly
(Emission Unit) Hand
Visible
Emissions, Level
Check site gauges
Fermentation Visual Non-certified Pump oil transmitter,
for liquid flow
Scrubber Inspections, VE readings reservoir full Pump rebuild
and liquid level
Maintenance kit, Valve
Activities
Visible
Emissions, Pressure
Check site gauges
Visual Non-certified Pump oil transmitter,
Vent Gas Scrubber for liquid flow
Inspections, VE readings reservoir full Pump rebuild
and liquid level
Maintenance kit
Activities
20. Malfunction Response (Scrubber)
Possible Corrective Steps to
Control Device Operating Parameter
Malfunction Possible Malfunctions Return Unit to Proper
(Emission Unit) Parameters Range
Detection Operation
Water flow loop
Pressure less
Water flow to scrubber instrumentation will be
Vent Gas Differential 50 -150" than 50
repaired
Scrubber Pressure water
Pressure greater
Plugged packing Unit will be cleaned
than 150
Visible Emissions
Opacity 0 - 20% Loss of water flow
exceed 20%
Pressure less
Water flow to scrubber
Differential 50 -150" than 50 Water flow loop
Fermentation Pressure water instrumentation will be
Scrubber Pressure greater repaired
Plugged packing
than 150
Water 50 - 100
Flow rate <50 Flow loop failure
Flowrate gpm
Ultra low sulfur, No. 2 Fuel Oil20.9 MMBtu per hour Vs. EGU at 1,650 MMBtu per hour
HCl, Hg, D/F should be met by using No. 2 Fuel OilPM might be met with No. 2 Fuel OilCO will require hope and faith
Retrofit Kit = PM is expected at 0.025 PPM, more than 3 times the EPA limitPM Controls = Cartridge dust collector = $320,000Oxidizer = As long as starting CO levels are less than 200 ppm, then 95% is good enoughIf not, this control must be combined with Low Emissions Kit“Removal” is not magic, it converts to CO2