Introduction to P&ID Reading and Design Process Engineering Process engineering is often a synonym of chemical engineering. It focuses on design, operation and maintenance of chemical and material manufacturing processes. Process engineering also involves developing new processes, project engineering and Process troubleshooting. Services in Process Engineering Process conceptual and feasibility study Process project scope definition Process design, evaluation and modification PFD and P&ID development Process modeling and simulation Process equipment sizing and selection Process safety analysis Process troubleshooting Applications of Process Engineering Chemical plants Biotech plants Crude oil refineries Fertilizer production Oil & gas processing Food processing Pharmaceutical manufacturers Pulp paper mills Mineral processing Water treatment plants Nuclear power plants ...... Type of Flow Diagrams in Process Engineering Mass Flow Diagram Block Flow Diagram (BFD) Also known as Information Flow Diagram Process Flow Diagram (PFD) Piping and Instrumentation Diagram (P&ID) Also known as Mechanical Flow Diagram (MFD). Utility Flow Diagram This is a type of P&ID for common plant utilities (steam, utility air, fuel oil, etc.) An Example of Block Flow Diagram (BFD) Diluent Diluted Bitumen NHT CDU Kerosene DHT Diesel Upgrader Naphtha LVGO VDU Sour Gas HC HVGO SCO Treating FG (upgrader) Naphtha SDA DAO Pitch EB SRU Diesel GO Sulfur Gasifier H 2S GSFR H2 (upgrader) Syn Gas Composed of only blocks (rectangles) and straight lines Each block represents one or more unit operations The lines represent the major process flow streams (material/ energy flows) Process Flow Diagram (PFD) A PFD is a schematic representation of a process using symbols to illustrate major operation units and major process flow lines. A PFD also tabulates process design values for the streams in different operating modes (minimum, normal and maximum). A PFD is typically the first drawing developed for a process, often in the pre-conceptual or conceptual design phase. What should be included in a PFD A PFD should include: Major equipment (symbols, names and identification #) Main process piping and flow direction Operating pressure and temperature Major bypass and recirculation lines Major control and instrumentation (optional) A PFD should not include: Pipe line numbers Minor components and minor bypass lines Isolation and shutoff valves Maintenance vents and drains Relief and safety valves Code class information A Sample of PFD Piping & Instrumentation Diagram (P&ID) – Scope It is a detailed symbolic representation of process interconnection, including all equipment, piping, and instrumentation. All items are identified using a standard numbering system. It should be developed at the Basic Engineering stage. It is the basis for all Detail Engineering work in plant design. Piping & Instrumentation Diagram (P&ID) – Synonyms Process and instrument diagram (P&ID) √ Piping and Instrument diagram (P&ID) √ Mechanical flow diagram (MFD) Engineering flow diagram (EFD) Piping and wiring diagram (P&WD) Pipe and identification diagram (P&ID) Piping & Instrumentation Diagram (P&ID) – Multidisciplinary Technical contents of P&IDs rely on multidisciplines: Process Mechanical Piping Control and Instrumentation Plant Operation P&ID – Classification Process P&ID Utility Plant P&ID Show the distribution of utilities within a given process. Valving and instrumentation on piping are shown for main headers up to and including branch root valves. Interconnecting (Rack) P&ID Define utility units such as cooling towers, air compressors, boilers, unit drain collection systems, fire water systems, and water treatment plants. Utility Distribution P&ID Define on-plot process unit design, as well as off-plot tankage and shipping systems They are the connecting link between individual process, utility plant, and utility distribution P&IDs. They are usually prepared for the offsite pipe racks and link the various process and utility plants. Vendor P&ID Prepared for systems that support major equipment packages. Piping & Instrumentation Diagram (P&ID) – Format There are no universal format to be used in developing P&IDs. The P&ID formats vary with industry segments and contractors. In reality, every industrial company that develops or uses P&IDs has its unique formats/guidelines for P&IDs. The P&ID preparation should follow the formats from individual clients. The P&ID formats are similar for different companies in the same industry. Two Key Elements in P&IDs Piping: Physical elements that interconnect equipment and process flow. In different sizes, normally expressed as nominal sizes In different materials. The most common material is carbon steel. Other metals, such as various grades of stainless steel, and plastic materials, such as PVC, Teflon, are also used. With thermal insulation, if required. Instrumentation Devices used to measure, control, and monitor the process variables. These variables can be flowrate, temperature, pressure, liquid level, viscosity, and others. Control valves and relief valves are also an important part of the instrumentation. Relationship between PFD and P&ID For a process, a PFD is a simple representation, while a P&ID is a definitive and comprehensive representation. A PFD shows major equipment and major process lines, while a P&ID shows all equipment and all process lines. A PFD shows major operating conditions (flow, temperature and pressure), while a P&ID shows piping, valves and instruments that monitor and control the process. P&IDs are more important in the design process, but PFDs provide a basis for P&IDs development. PFDs and P&IDs use the same symbols and formats. What should be included in a P&ID? All equipment with names and identification numbers Piping with flow direction and line numbers (pipe specifications and line sizes are included in line numbers) All valves All instrumentation with controlling devices and signal inputs and outputs Interconnection references (from one P&ID to another P&ID) Miscellaneous – vents, drains, special fittings, sample lines, and reducers Permanent start-up and flush lines Interfaces for class changes Vendor and contractor interfaces Identification of components and subsystems delivered by others Intended physical sequence of the equipment What should not be included in a P&ID? Manual switches Equipment rating or capacity Pressure, temperature and flow data Supplier package piping which is internal to the package and has no operational interface Elbows, tees and similar standard pipe fittings Extensive explanatory notes Physical details and dimensions Piping connections and type (e.g. threaded, flanged, etc.) Basic Steps for P&ID Preparation Show all equipments with necessary piping to carry out the process Show all connecting process piping necessary to carry out the process Show all other piping required for auxiliaries Show all required valves and major non-standard fittings Show all required instruments and control loops Mark size, fluid code, material code & identification numbers of all pipe lines Mark interlock numbers as per interlock description Review P&ID considering all operational, startup /shutdown, safety, maintenance & aesthetic aspects Three Key Types of Symbols in P&IDs Equipment symbols: Process operation units for mass transfer, heat transfer, momentum transfer and chemical reaction Piping symbols: Relevant to pipe, valves, and connections Instrumentation symbols: Sensing, monitoring and controlling The symbology follows the ISA standard ANSI/ISA5.1-1984 (R1992). Equipment Symbols in P&IDs Pumps Compressors Fans & blowers Mixers & agitators Conveyors & feeders and other material handling Separation equipment (liquid-liquid, liquid-gas, liquid-solid, gas-solid, gas-gas) Tanks & drums (storage) Heat exchangers Heating & cooling elements Reactors Turbines, generators and motors Transportation equipment Examples of Equipment Symbols Piping Symbols in P&IDs Process flow lines (often combined with signal lines for instrumentation) Valves P&ID connectors Reducers/Increasers Caps Connections In-line items Fire and safety Miscellaneous labels Examples of Piping Symbols Instrumentation Symbols in P&IDs General instrument or function symbols Signals and lines Sensors (four basic instrument groups) Temperature (T) Pressure (P) Flowrate (F) Level (L) Self-actuated devices Pressure (regulators, relief/safety valves) Temperature, flow, and level (regulators) Valve actuators Pneumatic & electric (solenoid, diaphragm, cylinder, motor, etc.) With & without positioners Miscellaneous labels Signal/Line Symbols Some Sensor & Control Valve Symbols Exercise: Identification of P&ID Symbols General Instrument Symbols Instrument Symbol Instrument Location Solid line: Control room panel No line: Field Double solid: Remote panel Dash line: Behind panel in control room Double dash line: Behind remote panel A circle -- individual measurement instruments such as transmitters, sensors, and detectors for pressure, temperature, flow, level A square with a circle inside -instruments that both display measurement readings and perform some control function (e.g. DCS connection and control) A hexagon -- computer functions. A square with a diamond -- PLC (Programmable Logic Control) functions. Instrument Identification – Tag Number Instrument symbols should contain letters and numbers. The letters indicate the instrument type, and the numbers identify the control loop. PI PI PI 217 217 217 a b c Usually 2 or 3 letters are used. Examples of Instrument # The first letter identifies the measured or initiating variable, The second is a modifier, The remaining letters identify the function. Normally a plant # should be prefixed to the Tag#. e.g. 265-PI217 (265 is a plant #) a. b. c. Pressure indicator, Loop 217, located in the field. Pressure indicator, Loop 217, on control panel, located in the control room. Pressure indicator, Loop 217, signal to DCS. Instrument Identification Letters First Letter Measured or Initiating Variable Modifier Succeeding Letters Readout or Passive Function Output Function Modifier User’s Choice User’s Choice A Analysis Alarm B Burner, Combustion User’s Choice C User’s Choice D User’s Choice E Voltage F Flow Rate G User’s Choice H Hand I Current J Power Scan K Time Time Rate of Change L Level M User’s Choice N User’s Choice User’s Choice O User’s Choice Orifice P Pressure, Vacuum Test Point Q Quantity R Radiation S Speed, Frequency T Temperature U Multivariable V Vibration, mechanical analysis W Weight, Force X Unclassified x-axis Y Event, State or presence y-axis Relay, Compute, Convert Z Position, Dimension z-axis Driver, Actuator Control Differential Sensory (Primary) Ratio Glass, Viewing Device High Indicate Control Station Light Low Momentary Middle User’s Choice User’s Choice Integrate, Totalize Record Safety Switch Transmit Multifunction Multifunction Multifunction Unclassified Unclassified Well Unclassified Some Combinations of Instrument Letters PC Pressure controller TA Temperature alarm PI Pressure indicator TI Temperature indicator PT Pressure transmitter TR Temperature recorder PR Pressure recorder TY Temperature I/P converter PY Pressure converter TW Temperature well PIC Pressure indicating controller TIC Temperature indicating controller PRC Pressure recording controller TRC Temperature recording controller PSV Pressure safety valve/ Pressure relief valve TCV PCV Pressure control valve I/P: Current to Pneumatic. Temperature control valve Some Combinations of Instrument Letters FA Flow alarm LA Level alarm FE Flow element LAH Level alarm high FI Flow indicator LAL Level alarm low FR Flow recorder LC Level controller FT Flow transmitter LG Level glass FY Flow I/P converter LI Level indicator FF Flow ratio LIC Level indicating controller FCV Flow control valve LRC Level recording controller FRC Flow recording controller LCV Level control valve A Control Loop Example in P&ID FT123: field-mounted flow transmitter FIC123: panel-mounted flow indicating controller located in a shared control/display device TY123: temperature I/P converter located in an inaccessible location TT123: filed-mounted temperature transmitter TIC123: field-mounted temperature indicating controller. Its output is connected via an internal software or data link to the setpoint (SP) of FIC123. YIC123: an event indicating controller. All inputs and outputs are wired to a PLC accessible to the operator. YIC typically indicates a controlled on/off valve. Rules of Thumb in P&ID Design P&IDs are typically developed from PFDs, so that understanding the designed process is a key basis for P&ID design. P&IDs do not have a drawing scale and usually present only the functional relationship, not the relative physical locations of components. P&IDs are done in a “single line” format that represents all piping and ductwork as a single line regardless of size. P&IDs should be specific to one system only, i.e. no more than one system should be shown on a single diagram. P&IDs should be configured such that major flow should generally be from left to right and from top to bottom, if possible. Primary flow paths should not suffer major changes in directions on P&IDs. P&IDs should start simple and then be enhanced in several revisions to address the real process by various disciplines. Following the style from the existing P&IDs for the same client. Line Designation (Line Number) in P&IDs Line # is required for piping in P&IDs Position of the line #: normally above piping lines Different formats of line # for different companies A line # contains the following basic information: Plant # Commodity symbol Line serial # Piping/Line size Piping/Line class (optional) An example: 6N1-4”-CA2B Plant 6, Nitrogen line 1, 4” pipe, piping class – CA2B Styles for Flow Direction in P&IDs 1. Flow arrow at each turning point 2. 3. Flow arrow at the end of each line Flow arrow at the middle of each line Valve Status for Bypass Lines It’s better to mark the valve status on the bypass lines including safety relief lines: NC – Normal Closed NO – Normal Open CSC – Car Seal Closed CSO – Car Seal Open LC – Lock Closed LO – Lock Open Relief valves need to indicate their set pressures e.g. SET @125 PSIG Accompanying Deliverables from P&IDs Equipment List Line List (Line Designation Table - LDT) Valve List Instrument List Tie-In List A Tie-in List shall be issued indicating the extent of the Vendor package battery limits each time a P&ID issue is made starting with IFA. For plant modification, the tie-in point is the point where from process or utility is connected in the existing systems. “Holds” List A "Holds" list must be issued each time a P&ID issue is made starting with IFD. The "Hold" indicates where the information used as input to the P&ID is preliminary and the item is used with risk in the downstream design. Revision list A Revision List defines the changes made in the design so that appropriate action can be taken to accommodate those changes. A Revision List must accompany any issue of P&IDs after IFH if the changes are too extensive to be distinguished in the revision box and by clouding. (IFA - Issued for Approval, IFD - Issued for Design, IFH - Issued for HAZOP) “As-Built” P&IDs When there are modifications done in construction, commissioning, qualification, or at any other time after the facility has been validated and operating, the P&ID must be modified to indicate the latest information. Frequently these modifications arise from construction, post-construction, and C&Q walk-downs prior to the system turn-over from IQ, OQ and PQ. All changes must be processed through the Quality Management System (QMS). All changes on a P&ID must be bubbled, signed and dated. Often a new revision number should be assigned to a “AsBuilt” P&ID. Software for Developing P&IDs AutoPLANT P&ID – AutoCAD-based (Bentley) PlantSpace P&ID – MicroStation-based (Bentley) SmartPlant P&ID – Able to convert AutoCAD or MicroStation based P&ID to SmartPlant P&ID (Intergraph) CADWorx P&ID – AutoCAD-based (CodeCAD Inc.) AutoCAD P&ID – AutoCAD-based (Autodesk) CADPIPE P&ID – AutoCAD-based (AEC Design Group) AutoFLOW – AutoCAD-based (PROCAD) HexaCAD P&ID – (Hexagon Software) AutoCAD P&ID 2007 for Developing P&IDs 1. Industry standard P&ID symbols 2. Dynamic process and signal lines 3. Dynamic components 4. Report and list generation 5. Import and export to MS Excel 6. Tag generation and uniqueness 7. Search and edit using a spreadsheet interface 8. Easy symbol creation and substitution 9. Review and approve data edits http://www.autodesk.com/us/autocadpid/interactiveoverview2008/index.html