Unit Procedures Page 1 of 13 Unit Procedures The Unit Procedures menu offers the following commands (choose any of the following options and then click anywhere on the flowsheet to add a new procedure of the type selected). The procedures with an asterisk (*) are not available in EnviroPro Designer: Batch Vessel Procedure Continuous Reaction Stoichiometric In a Reactor A set of sequential reactions described by stoichiometry only kinetics, occurring in a stirred-jacketed vessel and performed in batch mode. Equipment sizing based on volume of material processed per cycle. In a Seed Reactor A set of sequential reactions described by stoichiometry only, occurring in a seed reactor and performed in batch mode. Equipment sizing based on volume of material processed per cycle. In a Bioreactor * A set of sequential reactions described by stoichiometry only, occurring in a bioreactor and performed in batch mode. Equipment sizing based on volume of material processed per cycle. In a Seed Bioreactor * A set of sequential reactions described by stoichiometry only, occurring in a seed bioreactor and performed in batch mode. Equipment sizing based on volume of material processed per cycle. In a Disposable Bioreactor * A set of sequential reactions described by stoichiometry only, occurring in a disposable bioreactor and performed in batch mode. Equipment sizing based on volume of material processed per cycle. In a Disposable Seed Bioreactor * A set of sequential reactions described by stoichiometry only, occurring in a disposable seed bioreactor and performed in batch mode. Equipment sizing based on volume of material processed per cycle. In a Fermentor * A set of sequential reactions described by stoichiometry only, occurring in a stirredjacketed vessel and performed continuously (or semi-continuously). Equipment sizing based on residence time of material in tank. In a Seed Fermentor * A reaction described by stoichiometry only, occurring in a plug flow reactor. In an Air Lift Fermentor * A fermentation described by stoichiometry only, performed in batch mode. Equipment sizing based on volume of material processed per cycle. In a CSTR A set of sequential reactions described by stoichiometry only, occurring in a stirredjacketed vessel and performed continuously or semi-continuously. Equipment sizing based on volume of material processed in tank. In a PFR A set of sequential reactions described by stoichiometry only, occurring in a stirredjacketed vessel and performed continuously (or semi-continuously). Equipment sizing based on residence time of material in tank. In a Fermentor * A fermentation described by stoichiometry only, performed continuously or semi-continuously in a fermentor. Equipment sizing based on volume of material processed in tank. In a Seed Fermentor * A fermentation described by stoichiometry only, performed continuously or semi-continuously. mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Page 2 of 13 Equipment sizing based on residence time of material in tank. In an Air Left Fermentor * A fermentation described by stoichiometry only, performed continuously or semi-continuously in a Air Lift fermentor. Equipment sizing based on volume of material processed in tank. In a Raceway Pond * A photo-bioreaction described by stoichiometry only, performed continuously or semicontinuously in a Raceway Pond. Equipment sizing based on volume of material processed in pond. In a CSTR A set of sequential and parallel reactions described by stoichiometry and kinetics, occurring in a stirred-jacketed vessel and performed continuously or semi-continuously. Equipment sizing based on volume of material processed in tank. In a PFR A reaction described by stoichiometry and kinetics, occurring in a plug flow reactor. In a Fermentor * A set of sequential and parallel reactions described by stoichiometry and kinetics, occurring in a fermentor and performed continuously (or semi-continuously). Equipment sizing based on residence time of material in tank. In a seed Fermentor * A set of sequential and parallel reactions described by stoichiometry and kinetics, occurring in a seed fermentor and performed continuously (or semi-continuously). Equipment sizing based on residence time of material in tank. Equilibrium In a CSTR A set of reactions described by equilibrium data, occurring in a stirred-jacketed vessel and performed continuously (or semi-continuously). Equipment sizing based on residence time of material in tank. Environmental / Stoichiometric Stoichiometric WM Aerobic BioOxidation A set of bio-transformation reactions (describing biodegradation of organics) performed continuously in a well-mixed basin. Stoichiometric PF Aerobic BioOxidation A set of bio-transformation reactions (describing biodegradation of organics) performed continuously in a plug-flow basin. Stoichiometric Anaerobic Digestion A set of bio-transformation reactions (describing anaerobic digestion of activated sludge and transformation of other compounds) performed continuously in a well-mixed basin. Stoichiometric Trickling Filtration A set of biological transformations performed continuously in a trickling filter. Stoichiometric Anoxic Reaction A set of biological transformations performed continuously in a well-mixed basin under anoxic conditions. Stoichiometric Neutralization A set of sequential neutralization reactions performed continuously or semi-continuously in a well-mixed tank. Stoichiometric Wet Air Oxidation A set of oxidation reactions performed continuously or semi-continuously under high temperature and pressure and in the presence of water vapor. Kinetic Stoichiometric Incineration Destruction of organic compounds via combustion. mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Page 3 of 13 Environmental / Kinetic Inoculum Preparation Filtration Stoichiometric UV Radiation Sterilizaton of liquid stream via UV radiation. Kinetic WM Aerobic BioOxidation A set of bio-transformation reactions (describing biodegradation of organics) performed continuously in a well-mixed basin. Kinetic PF Aerobic BioOxidation A set of bio-transformation reactions (describing biodegradation of organics) performed continuously in a plug-flow basin. Kinetic Anaerobic Digestion A set of bio-transformation reactions (describing anaerobic digestion of activated sludge and transformation of other compounds) performed continuously in a well-mixed basin. Kinetic Anoxic Reaction A set of biological transformations performed continuously in a well-mixed basin under anoxic conditions. In a Roller Bottle This procedure simulates sets of operations that take place in disposable roller bottles for inoculum preparation and other applications. In a T-Flask This procedure simulates sets of operations that take place in disposable T-flasks for inoculum preparation and other applications. In a Shake Flask This procedure simulates sets of operations that take place in disposable shake flasks for inoculum preparation and other applications. In a Test Tube This procedure simulates sets of operations that take place in disposable test tubes for inoculum preparation and other applications. In a Rocking Bioreactor This procedure simulates sets of operations that take place in a disposable rocking bioreactor for inoculum preparation and for a other applications Microfiltration (Batch) * A microfiltration procedure operating in batch concentration mode. Microfiltration (Feed and Bleed) A microfiltration procedure operating in continuous (feed and bleed) mode. Ultrafiltration (Batch) * An ultrafiltration procedure operating in batch concentration mode. Ultrafiltration (Feed and Bleed) An ultrafiltration procedure operating in continuous (feed and bleed) mode. Reverse Osmosis (Batch) * A reverse osmosis procedure operating in batch concentration mode. Reverse Osmosis (Feed and Bleed) A reverse osmosis procedure operating in continuous (feed and bleed) mode. Diafiltration * A diafiltration procedure operating in batch mode. Dead End Filtration * A polishing cartridge filter. Nutsche Filtration * A filtration/drying procedure performed in batch mode in a Nutsche filter. Plate and Frame Filtration A filtration procedure performed in batch mode in a Plate & Frame filter. Rotary Vacuum Filtration A filtration procedure performed in batch mode in a Rotary Vacuum filter. Air Filtration A filtration procedure for removing particulate components from a gas stream. Belt A filtration procedure for dewatering activated sludge. mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Page 4 of 13 Centrifugation Screw Press A filtration procedure through a screw press Granular Media A filtration procedure for removing suspended particles from a liquid stream by passing it through a set of granular media beds. Baghouse A filtration procedure for removing particles from a gas stream. Electrostatic Precipitation A separation procedure for removing particles from a gas stream with the help of an electric field. Decanter Solid/liquid or liquid/liquid separation in a decanter centrifuge based on density difference and particle size. Disk-Stack * Solid/liquid or liquid/liquid separation in a diskstack centrifuge based on density difference and particle size. Bowl * Solid/liquid or liquid/liquid separation in a bowl centrifuge based on density difference and particle size. Centritech * Solid/liquid separation in a centritech centrifuge based on density difference. Basket (Top Discharge) * Solid/liquid separation (filtration) in a basket centrifuge based on particle size. Basket (Bottom Discharge) Solid/liquid separation (filtration) in a basket * centrifuge based on particle size. In a Cyclone Solid/gas separation in a cyclone based on density difference and particle size. In a Hydrocyclone * Solid/liquid or liquid/liquid separation in a hydrocyclone based on density difference and particle size. In a Centrifugal Sieve* Oversized solids/undersized solids separation in a centrifugal sieve based on physical states. High Pressure * Cell disruption of microorganisms and homogenization of fluid (primarily food) materials Bead Milling * Cell disruption of microorganisms and homogenization of fluid (primarily food) materials. Nano Milling * Thorough homogenization and mixing of suspension mixtures. Gel filtration * Separation of large molecules based on molecular size. PBA Chromatography (Simplified) * This unit procedure simulates any type of adsorptive chromatography (e.g., ion exchange, affinity, HIC, reverse phase, etc.) that takes place in a packed bed column PBA Chromatography (Detailed) In Bind-and-Elute Mode * This unit procedure simulates any type of adsorptive chromatography (e.g., ion exchange, affinity, HIC, reverse phase, etc.) that takes place in a packed bed column in bind-and-elute mode. PBA Chromatography (Detailed) In Flow-Through Mode * This unit procedure simulates any type of adsorptive chromatography (e.g., ion exchange, affinity, HIC, reverse phase, etc.) that takes place in a packed bed column in flow-through mode. EBA Chromatography * This unit procedure simulates any type of adsorptive chromatography (e.g., ion exchange, Homogenization/ Milling Chromatography/ Adsorption mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Page 5 of 13 affinity, HIC, reverse phase, etc.) that takes place in a expanded bed column. Drying/ Granulation Sedimentation Membrane Adsorption In Flow-Through Mode * This unit procedure simulates membrane adsorption in flow-through mode. The procedure can be executed in a batch/semi continuous mode only. Membrane Adsorption In Bind-and-Elute Mode * This unit procedure simulates membrane adsorption in bind-and-elute mode. The procedure can be executed in a batch/semi continuous mode only. Ion Exchange (for demineralization) Separation of compounds based on electric charge. This version of affinity chromatography can only handle a single elution step and a single wash/regeneration step. GAC Adsorption (for liquid streams) Separation of compounds based on biological affinity. This version affinity chromatography can handle any number of elution, wash, equilibration, and regeneration steps. GAC Adsorption (for gaseous streams) Separation of compounds based on biological affinity. This version affinity chromatography can handle any number of elution, wash, equilibration, and regeneration steps. Tray Drying * Spray drying is preferred for heat sensitive products that require short drying times and relatively low contact temperatures. Freeze * Dehydration (or other volatile solvent removal) under short residence time in a fluid bed dryer. Freeze (Discrete) * Drying of heat sensitive materials present in vials or other containers, in a discrete freeze dryer. Double Cone Drying * Drying of high value materials, such as pharmaceuticals and dyes, in a double cone dryer. Cone Screw Drying * Drying of high value materials, such as pharmaceuticals and dyes, in a cone screw dryer. Sphere Drying * Drying of high value materials, such as pharmaceuticals and dyes, in a sphere dryer. Drying-Granulation * Drying and granulation of a mixture containing suspended and dissolved solids Spray * Drying and lyophilization of heat sensitive materials, such as proteins and vitamins, based on sublimation of water. Fluid Bed * Drying of valuable materials, such as pharmaceuticals and dyes, in a tray dryer. Drum * Dehydration in a drum dryer under atmospheric pressure or vacuum. Rotary * Drying operation suitable for handling large throughputs. Used extensively in the agricultural, food, and mining industries. Sludge Drying of activated sludge. Decanting Liquid/liquid separation based on density difference, occurring continuously or semicontinuously in a horizontal tank. Clarification Solid/liquid separation based on density difference and particle size, occurring continuously or semi-continuously in a clarifier. IP Clarification Solid/liquid and liquid (oil) / liquid (water) mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Page 6 of 13 separation based on density difference and particle (or oil globule) size, occurring continuously or semi-continuously in an inclinedplate clarifier. Phase Change Distillation Extraction Liquid Extraction Absorption/ Stripping Storage/Blending Bulk - Batch Thickening Solid/liquid separation based on density difference and particle size, occurring continuously or semi-continuously in a thickener. Flotation Dissolved-air flotation that separates suspended solid particles or liquid globules from a continuous liquid phase. Oil Separation Oil/water separation in an API oil separator. Flash * Single-stage fractionation based on differences in volatility. Condensation * Recovery (capture) of volatile compounds based on condensation. Multi-Effect Evaporation * Solution concentration via solvent evaporation, performed in batch mode in a stirred vessel. Thin-Film Evaporation * Solution concentration via solvent evaporation, performed in batch mode in a thin film evaporator. Crystallization (Continuous) * Separation via crystallization, performed in batch mode in a stirred vessel. Batch * Batch, multi-stage fractionation based on differences in volatility. Continuous (Short-Cut) * Multi-stage fractionation based on differences in volatility using a short-cut model. Continuous (Rigorous) * Multi-stage fractionation based on differences in volatility using a rigorous model. In a Mixer-Settler * Phase split (extraction) based on partition coefficients or component splits, occurring in a stirred vessel in batch mode. In a Differential Extractor * Phase split (extraction) based on partition coefficients, occurring continuously (or semicontinuously) in a differential extractor. Centrifugal Extractor * Phase split (extraction) based on partition coefficients, occurring continuously (or semicontinuously) in a centrifugal extractor. Solids Leaching * Partitioning of solutes between two liquid phases in a mixer-settler extractor. Absorption Removal of components from a gaseous stream through contact with a liquid stream. Stripping Removal of components from a liquid stream through contact with a gaseous stream. Degasification Removal of organics from a gaseous or liquid stream through adsorption on activated carbon (or other suitable adsorbent). In Blending Tank Mixing and batch storage of material in an agitated tank. Equipment sizing based on volume of material processed per cycle. In a Flat Bottom Tank Batch storage of material in a flat bottom tank. Equipment sizing based on volume of material processed per cycle. In a Receiver Tank Batch storage of material in a receiver tank. Equipment sizing based on volume of material processed per cycle. mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Page 7 of 13 In a Horizontal Tank Batch storage of material in a horizontal tank. Equipment sizing based on volume of material processed per cycle. In a Vertical On Legs Tank Batch storage of material in a vertical tank. Equipment sizing based on volume of material processed per cycle. In a Drum Batch-wise storage in a drum. In a Tote Batch-wise storage in a tote. In a Silo (for Bulk Solids) * Batch storage of bulk solids in a silo. Equipment sizing based on volume of material processed per cycle. In a Bin (for Bulk Solids) * Batch-wise storage of bulk solids in a bin. In a Drum (for Bulk Solids) Batch-wise storage of bulk solids in a drum. * Bulk - Continuous In a Tote (for Bulk Solids) * Batch-wise storage of bulk solids in a tote. In a Blending Tank Mixing and continuous storage of material in an agitated tank. Equipment sizing based on residence time of material in tank. In a Flat Bottom Tank Continuous storage of material in a flat bottom tank. Equipment sizing based on residence time of material in tank. In Receiver Tank Continuous storage of material in a receiver tank. Equipment sizing based on residence time of material in tank. In a Horizontal Tank Continuous storage of material in a horizontal tank. Equipment sizing based on residence time of material in tank. In a Vertical On Legs Continuous storage of material in a vertical tank. Equipment sizing based on residence time of material in tank. In a Drum Storage of a continuous flow in a drum In a Tote Storage of a continuous flow in a tote. In a Silo (for Bulk Solids) * Continuous storage of bulk solids in a silo. Equipment sizing based on residence time of material in silo. In a Hopper (for Bulk Solids) * Continuous, short time, storage of bulk solids in a hopper. Equipment sizing based on residence time of material in vessel. In a Bin (for Bulk Solids) * Storage of a continuous flow of bulk solids in a bin. In a Drum (for Bulk Solids) Storage of a continuous flow of bulk solids in a * drum. Discrete - Batch In a Tote (for Bulk Solids) * Storage of a continuous flow of bulk solids in a tote. Equalization Damping of flowrate and concentration variations through the use of a buffer basin. Junction Box Mixing Mixing (combination) of wastewater streams in a junction box. In a Bin Storage of discrete entities in a bin. In a Drum Storage of discrete entities in a drum. In a Tote Storage of discrete entities in a tote. mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Page 8 of 13 In a Disposable Heat Exchange Mixing Bulk Flow Discrete Flow On a Rack Storage of discrete entities in a rack. On a Tray Storage of discrete entities in a tray. Generic Container Batch storage of material in disposable containers. Equipment sizing based on volume of material processed per cycle. Large Bag (on a Skid) Batch storage of material in a disposable large bag mounted on a skid. Heating Temperature increase using a heat transfer agent. Electric Heating Temperature increase using electricity. Cooling Temperature decrease using a cooling transfer agent. Electric Cooling Temperature decrease using electricity. Heat Exchanging Continuous exchange of heat in a heat exchanger. Cooling in a Tower Continuous water cooling in a Cooling Tower. Heat Sterilization * Continuous heat sterilization. Pasteurization * This unit procedure simulates a pasteurizer and calculates microorganism inactivation and food component degradation kinetics. Frying Industrial frying of potato chips and other products. Freezing-Thawing * This unit procedure can simulate freezingthawing of bulk material in a Freeze-Thaw Module Freezing-Thawing (Discrete) * This unit procedure can simulate freezingthawing of discrete entities in a Discrete FreezeThaw Module 2-Stream Mixing of two bulk streams. 3-Stream Mixing of three bulk streams. 4-Stream Mixing of four bulk streams. 5-Stream Mixing of five bulk streams. 6-Stream Mixing of six bulk streams. 7-Stream Mixing of seven bulk streams. 8-Stream Mixing of eight bulk streams. 9-stream Mixing of nine bulk streams. Custom Mixing of two streams under flow and composition specifications. Flow Adjusting Intelligent mixing of two streams under flow and composition specifications, in order to adjust the output flow. Mixture Prep Intelligent mixing of two-five streams under flow and composition specifications. In a Batch Tumble Mixer * Batch-wise mixing of powders. 2-Stream * Combination (mixing) of two discrete streams that carry the same discrete entity 3-Stream * Combination (mixing) of three discrete streams that carry the same discrete entity mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Splitting Page 9 of 13 Bulk Flow Discrete Flow 4-Stream * Combination (mixing) of four discrete streams that carry the same discrete entity 5-Stream * Combination (mixing) of five discrete streams that carry the same discrete entity 6-Stream * Combination (mixing) of six discrete streams that carry the same discrete entity 7-Stream * Combination (mixing) of seven discrete streams that carry the same discrete entity 8-Stream * Combination (mixing) of eight discrete streams that carry the same discrete entity 9-stream * Combination (mixing) of nine discrete streams that carry the same discrete entity 2-Way Splitting of a bulk flow into two streams based on user-defined split fractions. 3-Way Splitting of a bulk flow into three streams based on user-defined split fractions. 4-Way Splitting of a bulk flow into four streams based on user-defined split fractions. 5-Way Splitting of a bulk flow into five streams based on user-defined split fractions. 6-Way Splitting of a bulk flow into six streams based on user-defined split fractions. 7-Way Splitting of a bulk flow into seven streams based on user-defined split fractions. 8-Way Splitting of a bulk flow into eight streams based on user-defined split fractions. 9-Way Splitting of a bulk flow into nine streams based on user-defined split fractions. Custom Splitting of a bulk flow into two streams based on output flowrate specifications. 3-Way Flow Distribution Splitting flow up to three streams. The stream flowrate is specified either by the user, or the downstream process. It can be used to represent a distribution panel. 5-Way Flow Distribution Splitting flow up to five streams. The stream flowrate is specified either by the user, or the downstream process. It can be used to represent a distribution panel. 10-Way Flow Distribution Splitting flow up to ten streams. The stream flowrate is specified either by the user, or the downstream process. It can be used to represent a distribution panel. 2-Way * Splitting of a discrete entity flow into two discrete streams based on user-defined split fractions. 3-Way * Splitting of a discrete entity flow into three discrete streams based on user-defined split fractions. 4-Way* Splitting of a discrete entity flow into four discrete streams based on user-defined split fractions. 5-Way * Splitting of a discrete entity flow into five discrete streams based on user-defined split fractions. 6-Way * Splitting of a discrete entity flow into six discrete streams based on user-defined split fractions. mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Page 10 of 13 Component Flow Screening Washing Size Reduction Formulation & Packaging 7-Way * Splitting of a discrete entity flow into seven discrete streams based on user-defined split fractions. 8-Way * Splitting of a discrete entity flow into eight discrete streams based on user-defined split fractions. 9-Way * Splitting of a discrete entity flow into nine discrete streams based on user-defined split fractions. 2-Way Splitting of a stream into two streams based on user-defined component split fractions. 3-Way Splitting of a stream into three streams based on user-defined component split fractions. 4-Way Splitting of a stream into four streams based on user-defined component split fractions. 5-Way Splitting of a stream into five streams based on user-defined component split fractions. 6-Way Splitting of a stream into six streams based on user-defined component split fractions. 7-Way Splitting of a stream into seven streams based on user-defined component split fractions. 8-Way Splitting of a stream into eight streams based on user-defined component split fractions. 9-Way Splitting of a stream into nine streams based on user-defined component split fractions. Stationary This procedure can simulate a stationary screen (grizzly) (i.e., a grid of parallel metal bars set in an inclined frame) used for the separation of solids that are larger that a defined mesh size (e.g. 50mm). Vibrating This procedure can simulate a vibrating screen used for the separation of solids that are larger that a defined mesh size. Bulk * Washing of bulk flow to remove contaminants Discrete * Washing of discrete flow to remove contaminants Grinding (Bulk) * Size reduction of bulk solids in a grinder. Grinding (Discrete) * Size reduction of discrete solid entities in a grinder. Shredding (Bulk) * Size reduction of bulk solids in a shredder. Shredding (Discrete) * Size reduction of discrete solid entities in a shredder. Extrusion * Mixing, melting, and homogenization of polymeric resins and additives in an extruder. Same operation can represent extrusion of food products. Blow Molding * Formation of plastic containers from polymeric resins in a blow molder. Injection Molding * Formation of plastic parts from polymeric resins in an injection molder. Trimming * Removal of extra material from molded objects. Filling * Filling of containers with bulk material. Assembly * Formation of a discrete entity from the combination of two other discrete entities. mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Transport (near) Page 11 of 13 Printing * Printing on a discrete entity using bulk ink. Labeling * Attachment of a label on a discrete entity. Boxing * Placement of discrete objects in a box or formation of a pallet. Tableting (General) * Conversion of bulk, solid material into tablets or any other discrete entities. Tableting (Pharma) * Conversion of bulk, solid material into tablets or any other discrete entities using a tablet press (pharma) Tablet Coating * Coating of tablets or other discrete entities. Centrifugal Pump Transport of liquid materials using a centrifugal pump. Diaphragm Pump Transport of liquid materials using a diaphragm pump. Gear Pump Transport of liquid materials using a gear pump. Peristaltic Pumping Transport of liquid materials using a peristaltic pump. Compressor Transport of gaseous materials using a centrifugal compressor. Fan Transport of gaseous materials using a fax. Vacuum Pumping Transport of gaseous material via vacuum pumping. Belt Conveyor (bulk) * Transport of bulk solids using a belt conveyor. Belt Conveyor (discrete) * Transport of discrete objects using a belt conveyor. Pneumatic Conveyor (bulk) * Transport of bulk solids using a pneumatic conveyor. Pneumatic Conveyor (discrete) * Transport of discrete objects using a pneumatic conveyor. Screw Conveyor (bulk) * Transport of bulk solids using a screw conveyor. Screw Conveyor (discrete) * Transport of discrete objects using a screw conveyor. Bucket Elevator (bulk) * Vertical transport (lift) of bulk solids using a bucket elevator. Bucket Elevator (discrete) * Vertical transport (lift) of discrete objects using a bucket elevator. Truck (bulk) * Transport/distribution of bulk materials using a truck. Truck (discrete) * Transport/distribution of discrete objects using a truck. Train * Transport/distribution of bulk materials and/or discrete objects using a train. By Sea By Sea * Transport/distribution of bulk materials and/or discrete objects by sea. By Air By Air * Transport/distribution of discrete objects by airplane. Liquids Gate Valve Liquid Flow through a gate valve. Globe Valve Liquid Flow through a globe valve. Butterfly Valve Liquid Flow through a butterfly valve. Liquids Gases Solids Transport (far) Pressure Drop (Valves) By Land mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Page 12 of 13 Gases Power Generation Generic Boxes Bulk Flow Continuous Bulk Flow - Batch Gate Valve Gas Flow through a gate valve. Globe Valve Gas Flow through a globe valve Butterfly Valve Gas Flow through a butterfly valve. in a Straight Flow Steam Turbine-Generator * Power generation using a straight flow steam turbine. in an Extraction Steam Turbine-Generator * Power generation using a steam extraction turbine. in a Gas ExpanderGenerator * Power generation using a gas expansion turbine. in a Gas TurbineGenerator * Power generation using a gas turbine in an IC Engine-Generator * Power generation using an IC Engine in a Fuel Cell * Power generation with a fuel cell. Steam Generation * Steam generation by fuel burning. Gasification * Gasification of carbonatious fuel into fuel gas. 1x1 Pass Through 1x1 Pass Through Useful for representing continuous processing steps that are not explicitly available in the current version of ProDesigner. It can handle simple pass-through steps. 1x1 Reaction Useful to represent continuous processing steps that are not explicitly available in the current version of Pro-Designer. It can simulate material transformations (reaction) and / or simple pass through steps. 1x2 Reaction / Separation Useful for representing continuous processing steps that are not explicitly available in the current version of Pro-Designer. It can simulate material transformations (reaction) and / or simple pass through steps as well as flow or component splitting. 2x2 Reaction / Separation Useful for representing continuous processing steps that are not explicitly available in the current version of Pro-Designer. It can simulate material transformations (reaction) and / or simple pass through steps as well as flow or component splitting. 3x2 Reaction / Separation Useful for representing continuous processing steps that are not explicitly available in the current version of Pro-Designer. It can simulate material transformations (reaction) and / or simple pass through steps as well as flow or component splitting. 5x2 Reaction / Separation Useful for representing continuous processing steps that are not explicitly available in the current version of Pro-Designer. It can simulate material transformations (reaction) and / or simple pass through steps as well as flow or component splitting. 1x1 Useful for representing batch processing steps that are not explicitly available in the current version of Pro-Designer. 3x3 Useful for representing batch processing steps that are not explicitly available in the current version of Pro-Designer. mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021 Unit Procedures Page 13 of 13 Discrete Flow Design Spec 5x5 Useful for representing batch processing steps that are not explicitly available in the current version of Pro-Designer. 10x10 Useful for representing batch processing steps that are not explicitly available in the current version of Pro-Designer. Pass Through * Useful in simulating processing steps of discrete entities that involve no physico-chemical transformation, yet they incur some cost (e.g. inspection, weighing, etc.). Pass Through / Bulk Separation * Useful in simulating processing steps of discrete entities that involve no physico-chemical transformation, yet they incur some cost (e.g. inspection, weighing, etc.). It can simulate a simple pass through of discrete entities and component splitting. Bulk to Discrete * Converts flow of bulk material into flow of discrete entities. Discrete to Bulk * Converts flow of discrete entities into flow of bulk material. Flow Useful for expressing design specification constraints that will set a stream’s flow. User must select an input stream whose flow is to be adjusted to achieve the design goal. Composition Useful for expressing design specification constraints that will set a stream’s composition. User must select an input stream whose flow is to be adjusted to achieve the design goal. Temperature Useful for expressing design specification constraints that will set a stream’s temperature. User must select an input stream whose flow or temperature is to be adjusted to achieve the design goal. mk:@MSITStore:C:\Program%20Files%20(x86)\Intelligen\SuperPro%20Designer\v11e\... 13/05/2021