Isa Cap

Front 1

KPI

Back 1

Key Performance Indications

A business metric used to evaluate factors that are crucial to the success of an organization. Considerations include time, cost, and performance.

Front 2

CPI

Back 2

Cost Performance Index

The ratio of earned value to actual cost. No consideration for time or performance

Front 3

MES

Back 3

Manufacturing Execution System

Utilized to schedule production activites. Level 3 activities, example could be a batch system.

Front 4

ERP

Back 4

Enterprise Resource Planning

Use to collect, store, manage, and interpret data from many business activites, including production planning, purchase, manufacturing of service delivery. Level 4 activites.

Front 5

ROI

Back 5

Return on Investment

The accumulated cash inflows minus the initialinvestment. Achieved after a period of time where the total cash inflows equalsthe total cost of the initial investment. Non-Discounted- Does not consider the time value ofmoney.

Front 6

NPV

Back 6

Net Present Value(NPV)– The current value of an expected time series of cash flows minus the initialinvestment. Discounted - Doesconsider the time value of money.

Front 7

Feasibility Study

Back 7

Feasibility Study – Evaluate the alternativesolutions along with the associated benefits and cost. Used as the basis onwhich to decide to proceed to the next step.

Front 8

Success Triangle

Back 8

Success Triangle – Quality, Profit, Cost

Front 9

Project Constraints

Back 9

Project Constraints – Time & Money. Time drivenprojects will increase the cost, Cost driven projects will increase the time.The same amount of work will be done to complete.

Front 10

Cost-Plus

Back 10

Guarantees a profit for the seller in return forfull control over the project from the buyer.

Front 11

Time and Material

Back 11

Similar to cost plus exceptmaterial is involved

Front 12

Time & Material Not to Exceed

Back 12

Same as T&M except the stipulation is not toexceed max cost limit.

Front 13

Fixed Price

Back 13

High risk,high reward. Contingency is usually a factor when biding

Front 14

Project Life Cycle

Back 14

FeasibilityStudy-> Project definition-> System Design-> Software Development->Deployment-> Support

Front 15

Management Tools

Back 15

Scope of Work, Estimate, Design Schedule, Status Report, Management of Change (MOC)

Front 16

P&ID

Back 16

Piping and instrument Diagram(P&ID) - the principal document used todefine the process, equipment, piping, and components. Very detailed

Front 17

PFD

Back 17

Process Flow Diagrams (PFD) – Continuous process plants. Showswhat and how much product, typical temperatures, flows, pressures, etc.. Can beentire plant in scope: from raw material to final product.

Front 18

Specification Sheets

Back 18

Data sheet provided by the supplier.

Front 19

Instrument List

Back 19

Listing ofall instruments in alphanumeric order.

Front 20

Loop Diagrams

Back 20

A schematic representation of a completehydraulic, electrical, magnetic, or pneumatic circuit the circuit is called aloop.

Front 21

Location Plan

Back 21

instrument location drawing

Front 22

Probabilityof success

Back 22

the probabilitysystem will perform as intended

Front 23

Reliability

Back 23

the measured performance of successful operation. Success must bedefined by: intended function, time of function, satisfactory performance,design limits, operating time.

Front 24

MTTF

Back 24

Mean time to Failure(MTTF) – Most widely used Metric of reliability. If the failure rate is constantthen (MTTF=1/Failure Rate)

Front 25

MTTR

Back 25

Mean time to Restore(MTTR) – Expected time to repair, also known as “mean dead time”

Front 26

MTBF

Back 26

Mean Time BetweenFailure (MTBF) – The average time of a failure + repair cycle. MTBF=MTTF+MTTR

Front 27

MTBE

Back 27

Mean Time BetweenExplosions (MTBE) - The average time of an Explosion + repair. (for Hazardlocations)

Front 28

Availability

Back 28

the probability that a device is successful at a time when needed. A =MTTF/(MTTF+MTTR)

Front 29

Unavailability

Back 29

the probability that a device is not successful.U = 1 – A

Front 30

Fail-Safe

Back 30

failure state that causes or increases the probability that the systemwill go to a safe state.

Front 31

Fail-danger

Back 31

failure state that causes or increases the probability that the systemwill go to a hazardous state.

Front 32

Fail-Noeffect

Back 32

failures does not effect the safety function. Not included in analysisor calculations.

Front 33

Prob. of failure safely (PFS)

Back 33

Prob. of failuresafely (PFS) – probability that a safety function will trip the processspuriously. (False Trip)

Front 34

Prob. of failure on demand (PFD)

Back 34

Prob. of failure ondemand (PFD) – probability that function cannot respond to danger condition.

Front 35

Risk Reduction Factor (RRS)

Back 35

RiskReduction Factor (RRS) – Inverse of PFD

Front 36

PFave

Back 36

PFave – Average probabilityof failure on demand

Front 37

1oo1

Back 37

basic

Front 38

1oo2

Back 38

High Safety

Front 39

2oo2

Back 39

High Availability

Front 40

2oo3

Back 40

High Safety and Availability

Front 41

1oo1D

Back 41

High Safety

Front 42

2oo2D

Back 42

High Availability and Safe

Front 43

1oo2D

Back 43

High Safety and Available

Front 44

HAZAN

Back 44

Hazard Analysis(HAZAN) – Only the analysis of the risk and hazards conditions that exist. Onlythe first step of a risk assessment.

Front 45

HAZOP

Back 45

Hazard Analysis andOperability Study (HAZOP) – An all-encompassing review that analyzes notonly the hazardous conditions but also the operability of the facility orprocess. a structured and systematic examination of a planned or existingprocess or operation in order to identify and evaluate problems that mayrepresent risks to personnel or equipment, or prevent efficient operation.

Front 46

RiskAssessment

Back 46

Ranking the risk of the hazard events as a function of frequency, andseverity.

Front 47

ProtectionLayers

Back 47

– Process -> Process Control -> Alarms-> SIS -> Physical Protection devices-> Physical Protection barriers-> Plant Emergency Response -> Community Emergency Response

Front 48

SIL 1

Back 48

Failure Probability (10%-1%), Typically simplexelements, sensors, transmitters and general PLC.

Front 49

SIL 2

Back 49

Failure Probability (1%-0.1%), Typically redundant orsimplex elements, sensors, smart transmitters and safety PLC.

Front 50

SIL 3

Back 50

FailureProbability (0.1%-0.01%), Typically redundant “smart” elements, redundant smarttransmitters, and redundant safety PLCs.

Front 51

Cause and Effect Diagram

Back 51

a visualization tool for categorizing and identifying the potential causes of a problem and to identify itseffect.

Front 52

Fishbone Chart

Back 52

avisual tool to illustrate how various factors link to potential problems.Similar function to Cause and Effect, but looks like sentence diagram

Front 53

Pareto Chart

Back 53

a quality analysis tool thatdepicts how defects were generated by type of category or identified cause. Contains both bars and a line graph,where individual values are represented in descending order by bars, and thecumulative total is represented by the line.

Front 54

Level 4

Back 54

Business Planning and Integration, Automation:Enterprise Resource Planning (ERP), Network: Business/Enterprise, Time:Months, Weeks, Days, Standard: ISA 95

Front 55

Level 3

Back 55

Operation Management, Automation: ManufacturingExecution System (MES), Network: Operation, HMI, DMZ (level 3.5), Time:Day, Hours, Minute, Sec. Standard: ISA-88, 95

Front 56

Level 2

Back 56

Automation and Control, Automation: PLC, DCS, Network:Control, Time: Minutes, Seconds, SubSeconds. Standards: IEC 61311,IEC 61508, ISA 84

Front 57

Level 1

Back 57

Sensors and Manipulating, Network: Device,Sensor, Standards: ISA-20, 75, 76

Front 58

Level 0

Back 58

PhysicalProcess

Front 59

NEMA Type 1

Back 59

Indoor, protection from falling solid object.

Front 60

NEMA Type 2

Back 60

Indoor, protection from falling solids and dripping or splashing water.

Front 61

NEMA Type 5

Back 61

Indoor, protection from falling solids & settlingairborne dust, lint, fibers and drippingor splashing water.

Front 62

NEMA Type 12

Back 62

Indoor withoutknockouts, protection from falling solids & settling airborne dust,lint, fibers and dripping or splashing water.

Front 63

NEMA Type 13

Back 63

Indoor without knockouts, protection from fallingsolids & settling airborne dust, lint, fibers and dripping or splashingwater. Protection from spraying splashingand seepage of oil and coolants.

Front 64

NEMA Type 3

Back 64

Indoor/Outdoor, protection from windblown dust & falling solids and frozen water (sleet, rain, snow).

Front 65

NEMA Type 3x

Back 65

Indoor/Outdoor, protection from windblown dust & fallingsolids and frozen water (sleet, rain, snow), Corrosion resistant.

Front 66

NEMA Type 4

Back 66

Indoor/Outdoor, protection from windblown dust & fallingsolids and frozen water (sleet, rain, snow), and hose directed water.

Front 67

NEMA Type 4x

Back 67

Indoor/Outdoor, protection from windblown dust & fallingsolids and frozen water (sleet, rain, snow), and hose directed water, Corrosion resistant.

Front 68

NEMA Type 6

Back 68

Indoor/Outdoor, protection from windblown dust & falling solids and frozen water(sleet, rain, snow), and hose directed water & Temporary Submersion at a limited depth.

Front 69

NEMA Type 6P

Back 69

Indoor/Outdoor, protection from windblown dust & falling solids and frozen water(sleet, rain, snow), and hose directed water & Prolonged Submersion at a limited depth, Corrosion resistant.

Front 70

NEMA Type 7

Back 70

HAZARDOUS Indoor,for use in Class I Division 1

Front 71

NEMA Type 8

Back 71

HAZARDOUS Indoor/Outdoor,for use in Class I Division 1

Front 72

NEMA Type 9

Back 72

HAZARDOUS Indoor,for use in Class II Division 1

Front 73

NEMA Type 10

Back 73

HAZARDOUS MineSafety (MSHA)

Front 74

Class I

Back 74

Gases and Vapors. Easyignition by electric arc or passage of explosion through gap.

Front 75

Class II

Back 75

Combustible Dust. Examples:coal dust, grain dust, sugar dust.

Front 76

Class III

Back 76

Ignitable Flyings. Examples: Wood chips, cotton…

Front 77

Division 1

Back 77

Continuous or Intermittentclass hazard. (Hazard condition likely)

Front 78

Division 2

Back 78

Rare, abnormal or mitigatedclass hazard. Hazard condition less likely, dependent on equipment failure.

Front 79

Zone 0

Back 79

ContinuousClass I Div 1

Front 80

Zone 1

Back 80

IntermittentClass I Div 1

Front 81

Zone 2

Back 81

ClassI Div 2

Front 82

Zone 20

Back 82

Continuous Class II Div 1

Front 83

Zone 21

Back 83

Intermittent Class II Div 1

Front 84

Zone 22

Back 84

ClassII Div 2

Front 85

Globe Valve

Back 85

Linear motion, used for applications requiring throttling and frequentoperation. Since the baffle restricts flow, they are not recommended wherefull, unobstructed flow is required.

Front 86

Pinch Valve

Back 86

Linear Motion, used inapplications where the media needs to be completely isolated from any internalvalve parts or entrapments. They are commonly applied to medical instruments,clinical or chemical analyzers, and a wide range of laboratory equipment.

Front 87

Ball Valve

Back 87

Rotary Motion, durable, performing well after manycycles, and reliable, closing securely even after long periods of disuse. Thesequalities make them an excellent choice for shutoff applications, where theyare often preferred to gates and globe valves, but they lack their fine control inthrottling applications.

Front 88

Characterized Ball Valve

Back 88

Rotary motion, ball valvewith modified ball to improve throttling

Front 89

Butterfly Valve

Back 89

Rotary Motion, the disc is always present within theflow, so a pressure drop is always induced in the flow, regardless of valve position.

Front 90

Type T

Back 90

copper/constantan – (-250C to 350 C)

Front 91

TypeJ

Back 91

iron/constantan- (0C to 750 C)

Front 92

TypeE

Back 92

chromel/constantan - (-200C to 900 C)

Front 93

TypeK

Back 93

chromel/alumel - (-200C to 1250 C)

Front 94

TypeN

Back 94

Nicrosil/Nisil - (270C to 1300 C)

Front 95

TypeS, R, B

Back 95

Platinum Rhodium - (0C to 1450 or 1700 C)

Front 96

TypeC

Back 96

Tungsten/Rhenium - (0C to 2320 C)

Front 97

RTD

Back 97

Resistive Temperature Detector (RTD) – wire that responds to temperature change by changingresistance. Made of platinum, nickel, or tungsten. Advantage: more accurate. Disadvantage:less rugged, cannot be used with hi temperatures (max about 500 Co).

Front 98

Thermistor

Back 98

SemiconductorRTD

Front 99

Resolvers and synchros

Back 99

Resolvers and synchros are transducers thatconvert the angular position and/or velocity of a rotating shaft to anelectrical signal. Used primarily for motion control.

Front 100

SmartInstruments

Back 100

Any instrument that is microprocessor based,programmed, has memory, or remote communications. Usually digital.

Front 101

Single Component Analyzers

Back 101

Moister,pH, LEL

Front 102

GC

Back 102

Gas Chromatograph (GC) – Compositional analyzer

Front 103

TECF

Cooling method

Back 103

Totally Enclosed Fan Cooled

Front 104

TENV

Cooling method

Back 104

Totally Enclosed Non-Ventilated

Front 105

DPFG

Cooling method

Back 105

Drip proof – fully guarded

Front 106

ODP

Cooling method

Back 106

Open Drip proof