critical variables program2307.ppt author: przybylskic created date: 8/21/2020 10:29:52 pm

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CRITICAL VARIABLES PROGRAM Get plant operating results with an inexpensive and simple implementation using only PI-ProcessBook and PI-DataLink (NO Programming and LOW maintenance!)

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  • CRITICAL VARIABLES PROGRAM

    Get plant operating results with aninexpensive and simple

    implementation using onlyPI-ProcessBook and PI-DataLink

    (NO Programming and LOW maintenance!)

  • AGENDA

    • Introduction

    • Problem: Unit Operating Settings

    • Proposed Solution & Game Plan

    • Details of Critical Variables Program

    – Displays for current plant status

    – Reports for deviation tracking

    • Results: Successes & Failures

  • GENERAL INFO

    • Carolyn Przybylski (sha–BILL–skee)– B.S. Chemical Engineering (1987)

    – Started with Cytec as Process Engineer -> Production Engineer -> Process Control Engineer

    – Currently Sr. Manufacturing Systems Engineer

    – PI System Manager (4 years)

    • Cytec Industries – Fortier Plant– New Orleans, LA

    – Chemical Manufacturing plant

    – Continuous Processes (24/7/365)

    – 440+ Cytec employees & 150+ contractors onsite

  • PI SYSTEM LAYOUT

    • Separate Networks (Process & Office)

    • Two 50K tag servers with PI-to-PI interface

    • Interfaces:– 6 DCS (GSE D/3 & Yokogawa)

    – 20+ PLC (Square D, Allen Bradley)

    – 2 APC Systems

    – Laboratory Mgmt System (LIMS)

    – Environmental Mgmt System (EMIS)

    PROCESS NETWORK OFFICE NETWORK

    Routers/Firewall

    DCS & PLC

    Process PI Server

    (50k)APC

    Office PI Server

    (50k)

    PI-to-PI Server

    EMIS

    LIMS

    Clients

  • PROBLEM

    • Spent a lot of time & money improving control loops to enable finer control closer to constraints

    • Plant was still being run at “easy” settings rather than economical

    • Some settings could be detrimental to process (plugging) or equipment (corrosion) over the long term

    • Advanced Control option too expensive

  • “CHEAP & EASY” SOLUTION

    Needed a system to maintain the plant at

    target operating points and

    to track excursions from target

    • CHEAP – used existing PI Clients of ProcessBook and DataLink

    • EASY – no special programming required, just standard ProcessBook, DataLink, and Excel functions

    • Focused effort on developing list of key parameters and their targets/limits and then following up to ensure that unit was run within those limits

  • WHY USE PI INSTEAD OF DCS?

    • Lab sample results do not reside in DCS, but do reside in PI

    • Some key parameters are calculations that are done in PI, not on DCS

    • Future parameters from other units that were in PI

    • Limited DCS screens used for control; can use PC screen for PI

    • Easy to make changes (more people trained on PI-ProcessBook and Excel than on DCS)

  • GAME PLAN

    • Step 1: Establish list of critical variables as key indices for the plant and include ranges for TARGET, HI/LO, and HIHI/LOLO

    • Step 2: Develop ProcessBook display to show where plant is currently operating in relation to established targets (snapshot view)

    • Step 3: Develop daily DataLink report to show how much time was spent in each range (% of time) for monitoring off-shift periods

  • HOW ARE WE DOING RIGHT NOW?

  • NO VBA PROGRAMMING:MULTISTATE SYMBOLS, ONLY

  • HOW HAVE WE DONE IN THE PAST?

  • PI TIME FILTER FUNCTION

  • TIME INTERVAL FORMATTING

    =($B$4-$B$3)*24&"h"

  • CRITICAL LIMITSENTRY FOR REPORT

    Cell “$L10” used in Time Filter Formula

  • TIME FILTER FUNCTION EXPRESSION (LO/HI)

  • TIME FILTER FUNCTION EXPRESSION (LOLO/HIHI)

  • • % Time in Target Ranges:

    – Unit 1 = 95%

    – Unit 2 = 80%

    • Steam Savings of M$1.6

    • Long term savings: TBD

    – Extend equipment life?

    – Reduce outages due to plugging?

    • Communication key to success (supervisors, operators, engineers)

    RESULTS

  • • Originally one display and one report applied to operating parameters for one unit

    • Now three units using displays and reports for operating parameters

    • As successes are realized, more units should begin similar implementations

    • Have added displays and reports for Cooling Tower Operation and Quality Control

    ADDITIONAL STEPS

  • COOLING TOWER DISPLAY

  • USED DATASETS TODISPLAY LIMITS ON TRENDS

  • QUALITY CONTROL DISPLAY

  • SUMMARY OFCRITICAL VARIABLES PROGRAM

    • Simple method to maintain key variables on target using basic functionality of PI & Excel

    • Can be applied to multiple areas such as production, cooling towers, & quality control

    • KEY COMPONENT: COMMUNICATION!

    – Tool just helps to provide FOCUS on key issues & problem areas

    – Once target deviations are identified, operators, engineers, and supervisors MUST work together to apply solutions (specific communications/training)

  • QUESTIONS / COMMENTS?

    Thank you for your time and interest!

    Email: [email protected]

    Phone: (504) 431-6468