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Module 2 Steady State Simulation

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1 Module 2 Steady State Simulation
Program for North American Mobility in Higher Education (NAMP) Process Integration for Environmental Control in Engineering Curricula (PIECE)

2 Steady State Process Simulation
Module 2 Steady State Process Simulation

3 This module has been developed
Propose This module has been developed to help the students: Understand and simulate processes in steady state. Solve technical and economic problems more quickly, efficiently and successfully.

4 The student will. Statement of intent
Review basic concepts used in steady – state simulation. Understand the purpose of steady – state simulation. Develop models of a processes in steady state. Simulate processes with help of computer simulators.

5 This module is divided in 3 tiers
Contents This module is divided in 3 tiers Tier 1. Introduction to simulation tool. Tier 2. How to use computer tool. Tier 3. How to apply in real world.

6 Process Simulation tool
Tier 1 Introduction to Steady State, Process Simulation tool

7 Tier 1 is divided in 3 sections
Contents Tier 1 is divided in 3 sections Basic concepts. Steady – state simulation in a process integration context. Steady – state simulation in a broader context.

8 1 Basic Concepts

9 Basic concepts Statement of intent
Show the basic concepts of steady – state simulation. Improve process simulation skills. Create your own simulation flowsheets. Recognize why simulation is useful in the process industries.

10 Basic Concepts Contents Steady – state. Models and simulation.
Creating models. Unit efficiencies. Stream components. Units. Performing a steady – state simulation study.

11 Steady – state Steady – State By steady state we mean, in most systems, the conditions when nothing is changing with time. Mathematically this corresponds to having all time derivatives equal to zero, or to allowing time to become very large (go to infinity).

12 Steady – State Steady – state
The design of process systems requires both: Steady – state model. Dynamic models. One use for the steady – state models is in determining the possible region of steady – state operation for a process that can be limited by constraints such as safety, product quality, and equipment performance.

13 Models & simulation Model A model is an abstraction of a process operation used to build, change, improve or control a process. Uses of a model: Equipment design, sizing and selection. Comparison of possible configurations. Evaluation of process performance against limits (e.g. Concentrations, effluent discharge rates). De-bottlenecking and optimization. Control strategy development and evaluation.

14 The model is an abstraction of the real word
Models & simulation Model The model is an abstraction of the real word Models vary by: Phenomena represented (energy, classifications phase change). Level of detail and granularity Assumptions (perfect mixing, zero heat loss). Kind of input required Functions performed (constraint satisfaction, optimization). Nature of output generated

15 Models vary by purpose and category
Models & simulation Models vary by purpose and category Purpose Operator training simulator. Control strategy evaluation. Investment justification (e.g. new equipment purchase). Other… Category Physical (e.g. mimic panel) vs. Mathematical. Qualitative vs. Quantitative. Empirical vs. First principle based. Steady state vs. Dynamic state.

16 Physical Model Mathematical Model
Models & simulation Physical Model Mathematical Model From a balance:

17 Quantitative Qualitative
Models & simulation Quantitative Qualitative Using non – numeric descriptors. Fuzzy, logic. Expert system. Turn an alarm on. Using numbers, and quantifying the magnitude of the response.

18 First – principle based
Models & simulation Empirical First – principle based Derived from observation. Often simple. May or may not have theoretical foundation. Valid only within range of observation. Derived from fundamental physical laws. Most reliable, but we often don’t have them.

19 Steady – State Dynamic Models & simulation
Snapshot of a unit operation or plant Movie of plant operation Balance at equilibrium condition Time dependent results Equilibrium results for all unit operations Equilibrium conditions not assumed for all units Equipment sizes, in general not needed Equipment sizes needed Amount of information required: small to medium Amount of information required: medium to large

20 Requirements of a good model
Models & simulation Requirements of a good model Accuracy: close enough to the target. It is required in quantitative and qualitative models. Validity: we must consider the range of the model. The model must have a solid foundation or justification. Right level of complexity: models can be simple, usually macroscopic, or detailed, usually microscopic. The detail level of phenomena should be considered. Easy to understand. Computational efficiency: the models should be calculable using reasonable amounts of time and computing resources.

21 Simulation Models & simulation
Predicts the behavior of a plant by solving the mathematical relationships that describe the behavior of the plant’s constituent components. Involves performing a series of experiments with a process model.

22 Importance of steady – state simulation
Models & simulation Importance of steady – state simulation Better understanding of the process. Consistent set of typical mill data. Objective comparative evaluation of options for return on investment etc. Identification of bottlenecks, instabilities, etc. Ability to perform many experiments cheaply once model built. Avoidance of ineffective solutions.

23 Constructing a model ò Models & simulation
When we try to represent a phenomena, to predict future conditions, or to know how the process will behave in certain situation, it is common to use mathematical expressions. ò + × - = V S dV B dS n F b dt d

24 Constitutive relations
Creating models Constitutive relations Relate the diffusive flux of a certain quantity with the local properties of the material and with the transport driving force. Express the movement of a certain quantity in the decreasing gradient direction of the quantity.

25 Constitutive relations
Creating models Constitutive relations Fick’s first law: Mass diffusion Fourier’s law: Thermal diffusion Newton’s law: Kinematic viscosity

26 Variation Equations Conservation Equations or Equations of change
Creating models Variation Equations Conservation Equations or Equations of change Those relate the accumulation of a quantity with the rate of entrance or formation of the same quantity in a specific volume. Those are based in fundamental principles and have universal description.

27 Conservation of mass Creating models
It is common practice to express the balance in a differential element, and convert the equation to a differential form. In a differential element:

28 Conservation of chemical species:
Creating models Conservation of mass For a pure component: Conservation of chemical species: Note: steady – state no change in the time.

29 Conservation of energy
Creating models Conservation of energy Where HV is rate of heat generated by external source (electricity, compression, chemical reactions, etc.). Note: steady – state no change in the time.

30 Unit efficiencies Unit efficiencies
An engineer may define energy efficiency in a very restrictive equipment sense. Energy efficiency has been used to describe what actually may be conservation. Energy efficiency in a more subjective sense may refer to the relative economy with which energy inputs are used to provide services.

31 Typical Efficiencies Values
Unit efficiencies Typical Efficiencies Values Compressors e = 0.8 Motor e = 0.9 Pump e = 0.5 Turbine e = 0.8

32 Stream Components Stream components
Overall stream flows and components are calculated based on physical and chemical properties such as: Ideal gas law and equations of state. Solubility relations (solid in liquid and gas in liquid). Reaction stoichiometry and equilibrium. Simple vapor/liquid relationships such as Raout’s law.

33 Conversion of stream components
Via chemical reaction. A B C Mechanical work. Heat. A B A B

34 Engineering Units Units
The official international system of units is the SI . But older systems, particularly the centimeter – gram – second (cgs) and foot – pound – second (fps), are still in use. It was originated in France, in 1790 by the French Academy of Science. The units should be based on unvarying quantities in nature. Multiples of units should be decimal. The base units should be used to derive other units.

35 Units Engineering Units

36 Performing a Steady – State simulation Study
Performing a SS simulation study Performing a Steady – State simulation Study Steady state model derivation. Calculation order. Recycle streams. Convergence and iteration. Recycle convergence methods. Granularity model.

37 Steady state model derivation
Performing a SS simulation study Steady state model derivation 1.- Define Goals. a)      Specific design decisions. b)      Numerical values. c)      Functional relationships. d)      Required accuracy. 2.- Prepare information. a)      Sketch process and identify system. b)      Identify variables of interest. c)      State assumptions and data.

38 Steady state model derivation
Performing a SS simulation study Steady state model derivation 3.- Formulate model. a)      Conservation balances. b)      Constitutive equations. c)      Rationalize (combine equations and collect terms). d)      Check degrees of freedom. e)      Dimensionless groups (Pr, Nu, Re, etc.). 4.- Determine solution. a)      Analytical. b)      Numerical.

39 Steady state model derivation
Performing a SS simulation study Steady state model derivation 5.- Analyze results a) Check results for correctness Limiting and approximate answers Accuracy of numerical method b) Interpret results Plot solution Relate results to data and assumptions Evaluate sensitivity Answer “what if questions”

40 Steady state model derivation
Performing a SS simulation study Steady state model derivation 6.- Validate model. a)      Select key values for validation. b)      Compare with experimental results.

41 Calculation Order Performing a SS simulation study
In most process simulators, the units are computed (simulated) one at a time. The calculation order is automatically computed to be consistent with the flow of information in the simulation flowsheet, where the information flow depends on the specifications for the chemical process. 1 2 3 4

42 Recycle Flows Performing a SS simulation study
A simulation flowsheet usually contains information recycle loops. That is, cycles for which too few streams variables are known to permit the equation for each unit to be solved independently. 1 2 3 4 For these processes, a solution technique is needed to solve the equations for all the units in the recycle loop.

43 Solution technique Performing a SS simulation study
Consist in guessing a value for the recycle stream. This value is generally not going to equal the calculated value, this represent another problem which is solved by “iteration”. Calculation Initial guessing values New values from The calculation

44 Iteration Performing a SS simulation study
Convergence units use convergence subroutines to compare the newly computed variables (in the feed stream to the convergence unit) with guessed values (in the product stream from the convergence unit) and to compute new guess values when the two streams are not identical to within convergence tolerances. This procedure is call iteration. It involves re – calculating the flowsheet.

45 Convergence Performing a SS simulation study
Is the process to compare the guessed value with the computed value, until find a value within the tolerance range. Guess value No Yes Guess value – calculated value < Tolerance Convergence When the criteria is achieve, the solution is found, and is time to stop the iteration.

46 t = 0, k = 0 Guess torn streams
Performing a SS simulation study Start t = 0, k = 0 Guess torn streams Initialize each unit no Convergence? Convergence Xij yij k = k + 1 no Stop

47 Recycle convergence methods
Performing a SS simulation study Recycle convergence methods Where is the vector of guesses for n recycle (tear) variables and is the vector of the recycle variable computed from the guesses after one pass through the simulation units in the recycle loop. Clearly, the objective of the convergence unit is to adjust so as to drive toward zero.

48 Successive substitution as the basic and obvious method
Performing a SS simulation study Successive substitution as the basic and obvious method Also call direct iteration. In this method the new guess for x is simply made equal to f(x*). x0* x1* f(x*) Locus of Iterates When the slope of the locus of iterates (f(x),x) is close to unity, a large number of iterations may be required before convergence occurs

49 Other convergence methods
Performing a SS simulation study Other convergence methods When the method of successive substitutions requires a large number of iterations, another methods are used to accelerate convergence: Wegstein’s method. Newton – Raphson method. Broyden’s quasi – Newton method. The dominant – eigenvalue method.

50 Wegstein’s method Performing a SS simulation study
In this method, the two previous iterates of f(x*) and x* are extrapolated linearly to obtain the next value of x as the point of intersection. Locus of Iterates f(x*) x0* x1*

51 Granularity of modeling
Is the level of detail taken into account in a simulation. With the advance in technology, it is possible to combine on a single computer the full capability of a high fidelity simulation models. High fidelity process simulation is commonly used by many industries in the design of a process.

52 Comparing Coarse vs. Fine models
Granularity of modeling Comparing Coarse vs. Fine models A coarse model represent the equipment with few detail. Bleaching tower Coarse:

53 Fine model Granularity of modeling
The same equipment is divided in 3, and the substances into account are more than just an approximation. Bleaching tower More than 1 direction PFR CSTR Liquors Fibers Chromophores Chemicals

54 Benefits Coarse Models Fine Models Granularity of modeling
The detail level is low The time involve is less The solution effort is few The solution is approximated The detail level is big Time require is big The solution effort is big The solution is exact Coarse Models Fine Models

55 2 Steady state simulation in a process integration context

56 Steady state simulation in a process integration context
Statement of intent Steady state simulation in a process integration context Recognize the components in a simulation flowsheet. Check the procedure to create a process. What is the importance of the computer. What can we obtain as a result of a simulation.

57 Steady – state simulation in a process integration context
Table of content Steady – state simulation in a process integration context Process flowsheets. Simulation flowsheets. Process synthesis methodologies. Minimal time and expense. Computer – based process. Data reconciliation. Process insights resulting from simulation.

58 Process flowsheets Process flowsheets
Process flowsheets are the language of chemical processes. Like a work of art, they describe an existing process or a hypothetical process in sufficient detail to convey the essential features.

59 Process flowsheet Process flowsheets
A process flowsheet is a collection of icons to represent process units and arcs to represent the flow of materials to and from the units. Fresh Feed Steam Heater Reactor Flash Distillation Product

60 Simulation Simulation flowsheets
The analysis of a simulation, is the tool chemical engineers use to interpret process flowsheets, to locate malfunctions, and to predict the performance of the process.

61 Simulation Flowsheet Simulation flowsheets
A simulation flowsheet, on the other hand, is a collection of simulation units, each representing a computer program (subroutine or model) that simulates a process unit, and arcs to represent the flow of information among the simulation units. Mixer Heater Reactor Flash Column Mathematical Convergence Unit

62 Process synthesis methodologies
Total enumeration of an explicit space: is the most obvious. Here we generate and evaluate every alternative design. We locate the better alternative by directly comparing the evaluations. Evolutionary methods: follow from the generation of a good base case design. Designers can then make many small changes, a few at a time, to improve the design incrementally. Structured Decision Making: following a plan that contains all the alternatives.

63 Process synthesis methodologies
Design to target: these have been especially useful in designing heat recovery and reactor networks. The utility requirements become the targets for the design. Problem abstraction: Here the search for better design alternatives begins by formulating a less detailed problem statement and attempting to solve this more abstract problem first.

64 Minimal time Minimal time and expense
With a simulation, you can simulate one day of process operation in just seconds, and make as many changes as you want. Fresh Feed Steam Heater Reactor Flash Distillation Product Change in Reactor Properties Change composition In feed Change in Heat Duty Change in Column Properties

65 Minimal expense Minimal time and expense
Is easy to model the process with different kind of equipment without having to invest in it. Simulated “learning experiences” are much less costly than making real mistakes in the real plant.

66 Computer – Based process representation which can be re - used
Most of the times, there are already models which can be adapted to the process under study, with minimal changes. This minimizes the time needed to set up complicated equations. Re-using models is much easier than building new ones, specially if the process is being modeled for the first time.

67 Data reconciliation Data reconciliation
Data reconciliation is a technique for improving the quality of measured plant data. These measurements are inherently inaccurate due to instrument failures, limitations of measurement techniques, etc. As a result, data are obtained that violate mass and energy balance constraints of describe a physically infeasible process.

68 How Data reconciliation works
Find a set of data that: Constitutes some kind of “best fit” (least squares) to the observed data. Satisfies mass – energy balance and other criteria. t F Reconciling errors

69 Opportunity to do data reconciliation
This amounts to validation of the process data using knowledge of the plant structure and the plant measurement system

70 Process insights resulting from modeling
Identification: We can find the structure and parameters in the model. Estimation: If the internal structure of model is known, we can find the internal states in model. Design: If the structure and internal states of model are known, we can study the parameters in the model. MODEL

71 Process insights resulting from modeling
If the model is known, we have two uses for our model: Direct: input is specified, output is studied (simulation). Inverse: output is specified, input is studied. Used when an objective must be met (production, composition).

72 3 Steady – State Simulation in a Broader Context

73 Steady – State Simulation in a Broader Context
Statement of intent Steady – State Simulation in a Broader Context Show how to take a decision to create a process. Know if the process is viable, in terms of stability and economic. Taking in count security aspects.

74 Aspects of Process Design
Table of content Aspects of Process Design Process design. Stability and sensitivity. Process optimization. Economic evaluation of alternatives. Operator training.

75 Process design Process design
The design of chemical products begins with the identification and creation of potential opportunities to satisfy societal needs and to generate profit. The scope of chemical product is extremely broad. They can be roughly classified as: basic chemical products. Industrial products. Consumer products.

76 Process design Process design Natural Basic chemical Manufacturing
Resources Basic chemical Products Basic Chemical Industrial Industrial Products Consumer

77 Motivation for design projects
Process design Motivation for design projects Desires of customers for chemicals with improved properties for many applications. New inexpensive source of a raw material with new reaction paths and methods of separation. New markets are discovered.

78 Steps in a Process Design
Process Design – Questions to Answer Is the chemical structure known? Is a process required to produce the chemicals? Is the gross profit favorable? Is the process still promising after further elaboration? Is the process and/or product feasible?

79 Steps in a Process Design
Process Design – Steps Create and assess primitive problem. Find chemicals or chemical mixtures that have the desired properties and performance. Process creation. Development of base case. Detailed design, equipment sizing, and optimization. Startup assessment. Reliability and safety analysis. Written design report and oral presentation. Plant design, construction, startup and operation.

80 Process Design – Procedure

81 Detailed Process Synthesis Using Algorithmic Methods
Process design Detailed Process Synthesis Using Algorithmic Methods Create and evaluate chemical reactor networks for conversion of feed to product chemicals. Separation trains for recovering species in multi-component mixture. Reactor separator recycle networks. Locate and reduce energy usage. Create and evaluate efficient networks of heat exchangers with turbines for power recovery. Networks of mass exchangers to reduce waste.

82 Feasible Region Stability and Sensitivity
The region within which the process can be operated is called the operating window or feasible operating region. Feasible region g3=0 g2=0 g1=0

83 Feasible Region Stability and Sensitivity
One can not in general say a priori how a thermodynamic model will behave when extrapolated beyond the region in which data were available for determining its empirical parameters.

84 Stability of the process
Stability and sensitivity Stability of the process When a process is disturbed from an initial steady state, it will, in general, respond in one of 3 ways. Proceed to a steady state and remain there.

85 Stability of the process
Stability and sensitivity Stability of the process Fail to attain to steady – state conditions because its output grows indefinitely.

86 Stability of the process
Stability and sensitivity Stability of the process Fail to attain steady – state conditions because the process oscillates indefinitely with a constant amplitude.

87 Stability of the process
Stability and sensitivity Stability of the process A steady state system xs is said to be stable if for each possible region of radios e>0 around the steady state, there is an initial state x0 at t=t0 falling within a radius d>0 around the steady state that causes the dynamic trajectory to stay within the region (x-xs)<e for all times t>t0. Region e>0 Steady state xs Radius d State x

88 Sensitivity analysis Stability and sensitivity
In many cases, it is useful to know how a chemical process respond when a equipment parameter or stream variable is varied, rather than running simulation only in few parameters. The sensitivity analysis permits the tabulation of output variables at equal increments over a specified range of parameter or variable values.

89 Sensitivity analysis Stability and sensitivity
Example: Carbon monoxide and hydrogen are reacted to form methanol. The reaction is exothermic; consider an adiabatic reactor. 100% of the carbon monoxide is converted. For a fixed flow rate of carbon monoxide, it is desired to know how the outlet temperature varies with respect to the flow rate of hydrogen in the feed stream.

90 The temperature decreases as the mole flow in feed increases.
Stability and sensitivity Sensitivity analysis The temperature decreases as the mole flow in feed increases.

91 Sensitivity analysis Stability and sensitivity
One of the most important contributions of sensitivity analysis is that it allows one to identify those variables which, when changed, have the greatest impact on the process output.

92 Optimization Process optimization
From a Mathematical point of view, chemical engineers encounter 3 situations when solving equations. Completely specified case. Over-specified case. Under-specified.

93 Completely specified case
Process optimization Completely specified case Nequations = Nvariables When the number of equations is equal to the number of variables, then we can proceed to solve the problem. 3x – 2y + 9z = 3 6x – 11y + z = 7 x – 15y + 4z = 25 In this case, we have 3 equations with 3 unknowns.

94 Over – specified case Process optimization
Many variables are determined in >1 way – values must be reconciled Nvariables < Nequations which is commonly referred to as the reconciliation (data reconciliation and rectification) problem.

95 Under – specified case Process optimization
Some variables are undetermined – can be manipulated to optimize the process. Nvariables > Nequations Also called optimization problems. The optimization is used to maximize or minimize a specified objective function by manipulating decision variables (feed stream, block input, or other input variables).

96 Optimization Process optimization Nvariables – Nequations= ND
The decision variable, d, is iteratively adjusted to achieve the optimal solution to a specified objective. Some methods commonly used are: Successive linear programming (SLP). Successive quadratic programming (SQP). (used by Aspen plus, Hysys.plant) Generalized reduced gradient (GRG).

97 Any optimization problem can be represented as:
Process optimization Optimization Any optimization problem can be represented as: Is the objective function. Is the set of m equations in n variables x. The equality constraints Is the set of r inequality constraints. Those bound the feasible region of operation.

98 Optimize on multiple criteria
Process optimization Optimize on multiple criteria Some common objectives in optimization of an industrial process are: Achieve lower capital cost design. Increase production. Reduce unit operation cost. Reduce environmental impact. Reduce energy consumption.

99 ND = Nequations – Nvariables.
Process optimization Degrees of freedom A degree of freedom analysis is incorporated in the development of each subroutine that simulate a process unit. These subroutines solve sets of Nequations involving Nvariables. ND = Nequations – Nvariables. Degrees of freedom are the number of input variables you need to specify.

100 Quantitative comparison of alternatives
Economic evaluation of alternatives Quantitative comparison of alternatives In almost every case encountered by chemical engineer, there are several alternative methods which can be used for any given process or operation. Formaldehyde production: By catalytic dehydrogenation of methanol. (By controlled oxidation of natural gas) By direct reaction between CO and H2 (under special conditions of catalyst, temperature, and pressure)

101 Optimum Economic Design
Economic evaluation of alternatives Optimum Economic Design If there are two or more methods for obtaining exactly equivalent final results, the preferred method would be the one involving the least total cost. $ Alternative designs do not give final products or results that are exactly equivalent. It then becomes necessary to consider the quality of the product or the operation as well as the total cost.

102 Economic evaluation of alternatives
Throughout the design process, estimates of the cost of equipment and other costs related to the capital investment play a crucial role in selecting from among the design alternatives. The total capital investment (TCI). The annual cost of manufacture (COM).

103 Total capital investment
Economic evaluation of alternatives Total capital investment Is a one – time expense for the design, construction, and start – up of a new plant or a revamp of an existing plant. Estimation of the total capital investment Order – of magnitude estimate based on bench – scale laboratory experiments. Study estimate based on a preliminary process design. Preliminary estimate based on detailed process design studies lading to an optimized process design. Definitive estimate based on a detailed plant design.

104 Investment justification
Economic evaluation of alternatives Investment justification Objective: to evaluate the costs and benefits of investment in process modifications. Inputs and outputs with costs attached must be accurately represented. Differences between candidate solutions must be accurately modelled. Level of detail just enough to enable cost-benefit calculations. Other parts of the process can be a “black box”.

105 Economic evaluation of alternatives
Direct cost Indirect cost

106 Quantify cost – benefit of various possibilities
Economic evaluation of alternatives Quantify cost – benefit of various possibilities When designing a greenfield plant, there are many possibilities which can be evaluated to get the best cost – benefit ratio.

107 Cost sensitivity analysis
Economic evaluation of alternatives Cost sensitivity analysis Sensitivity analysis is important in order to avoid information overload: It usually is best to do an initial analysis using only the data you have, being careful about indicating where the data is weak or you are using best guesses.

108 Cost sensitivity analysis
Economic evaluation of alternatives Cost sensitivity analysis “Planning should stimulate thinking, not overwhelm it”

109 Operator training Operator training
Today, cheap computer power allows virtually any operator to have enough capability to simulate large flowsheets with considerable detail on the desktop. Process flowsheet simulators now have a sophisticated user interface, large physical properties databanks, and many thermodynamic models.

110 Operator training Operator training
Running sophisticated process simulations does not guarantee correct results. You need to understand the thermodynamic assumptions underlying the program and how to ensure proper application. The personnel using the simulators, should be trained beforehand, and be aware of problems that may appear.

111 Operator Training simulation
Objective: to mimic response of displays to simulate process excursion and operator inputs. integration with physical operator console. simplified process representation, just enough to generate appropriate responses. progressive series of exercises as part of system. trainee evaluation as part of system.

112 Operator training Opportunity to increase process and systems awareness in operating personnel A simulated process can be easily executed in a computer, without the expense of real equipment and without the risk of disrupting the real plant’s production. In this virtual world, computer simulations allow all manner of extreme conditions and “what – if” scenarios to be tested safely.

113 Operator training Develop competence in unusual, undesirable, or dangerous process operation conditions The only certain way to test how a proposed control system will handle every conceivable situation is to design it, install it, and try it out.

114 Simulators avoid dangerous process operation
Operator training Simulators avoid dangerous process operation A simulated control system can be installed in a simulated plant without the expense of real equipment and without the risk of disrupting the real plant’s production. Computer simulation allow all manner of extreme conditions and “what if” scenarios to be tested safely.

115 Increase comfort level with advanced technology
Operator training Increase comfort level with advanced technology A simulator trainer substitutes for the real plant and the real control system. If the simulation is realistic, the trainees don’t know the difference.

116 Simulation in Process Design and Operation
Summary Simulation in Process Design and Operation Before constructing a plant, or making any changes to it, it is always desirable to know how it is going to behave. Steady – state simulation, is the tool one use. In this tier, the basics tools to understand a process design, construct it and simulate it in a computer, were shown.

117 Quiz Quiz A first pass simulation using mill data indicates that the boiler is generating more steam than the heating value of the fuel will provide (i.e. efficiency greater than 100 %). An appropriate response would be: Ignore the problem as insignificant. Replace the boiler simulation model with one that will give you realistic results. Recommend a certificate of appreciation for outstanding performance be presented to the boiler operating crew. Double check the accuracy of the measurements and arrange for test to be performed on the boiler fuel.

118 Your simulation flowsheet is failing to converge
Your simulation flowsheet is failing to converge. What would be the most likely cause of this problem? Inaccuracies in the process data. Incompatible process specifications in different parts of the sequential flowsheet that are “fighting” each other. The actual process in fact never balances. Unrealistic assumptions about unit efficiencies. To many recycle loops.

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