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CE-307 – CHEMICAL ENGINEERING DESIGN

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Page 1: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

CE-307 – CHEMICAL ENGINEERING DESIGN

Page 2: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

CE-307 – Chemical Engineering Design

Instructor – University at Buffalo Mattheos Koffas

Teaching Assistant Chin Giaw (Ryan) Lim

Page 3: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Course Information Lectures

Mondays, Wednesdays 5:00-6:20 pm10 Capen

Office Hours Mondays 6:30-8:00 pm 904 Furnas Hall By appointment

TA office hours Friday 4:00- 6:00 pm, 903 Furnas Hall

Page 4: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

ISBN: 0-471-00077-9

Page 5: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Course Grade Homework assignments 30% Mid-term Class Tests 40% Final examination 30%

Average will be set as C.

Note on Academic Integrity: Copying is not allowed!

Page 6: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Homework 10 homework sets will be handed during

the semester.

Almost all homework (with the exception of 1) will be handed on Wednesday and will be due on Monday, 5:00 pm in class.

No homework will be accepted after 5:01 pm.

Page 7: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Course Outline Introduction Process Dynamics Laplace Transforms Transfer Function Block Diagrams Dynamic Behavior of Typical Process

Systems Feedback Control Stability of Control Loops

Page 8: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Course Objectives Review of basic process modeling.

Develop dynamic models for processes and solve them.

Obtain a realistic understanding of industrial process control practice.

Page 9: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Introduction to Process Control

The continuous change of measurements in a chemical or biological process leads to the conclusion that processes are dynamic.

Process dynamics refer to an unsteady-state or transient behavior.

Steady-state vs. unsteady-state behaviori. Steady state: variables do not change

with time So far, your ChE curriculum has emphasized

steady-state or equilibrium situations.

Page 10: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Process Dynamics Only with an understanding of transient

behavior of physical systems can an engineer design good processes.

This is exactly what process control does: it provides the expertise needed to design plants that function well in a dynamic environment.

Bottom Line: process control has a major impact on profitability

Page 11: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Examples

Continuous processes with examples of transient behavior:

i. Start up & shutdownii. Major disturbance: e.g., refinery during

stormy or hurricane conditionsiii. Equipment or instrument failure (e.g., pump

failure)iv. Batch Processes- Batch reactor

i. Composition changes with time

Page 12: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Multidisciplinary Field

Process control is used in many engineering fields: Chemical Electrical Mechanical

Page 13: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Control The following definition of control

will be used in this course: To maintain desired conditions in a

physical system by adjusting selected variables in the system.

Page 14: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

What does a control system do?

As an example, consider the heating system of a house.

We need to maintain the house temperature at a certain point.

This is done by circulating hot water through a heat exchanger.

The temperature is determined by a thermostat that compares the value of the room temperature to a desired range.

If the temperature is in the desired range, the pump halts water circulation.

The temperature can exceed the limits, because the furnace and heat exchanger cannot respond immediately.

Page 15: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Common features in process control cases

There is always a specific value (or range) as a desired value (referred to as set point) for the controlled variable.

The conditions of the system are measured; that is, all control systems use sensors to measure the physical variables that are to be maintained near the desired values.

There is always a control calculation, or algorithm , which uses the measured and desired values to determine the correction to the process operation.

The results of this calculation are implemented by adjusting some item of equipment in the system, which is termed the final control element.

Page 16: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Some more definitions Input: input does not necessarily refer to

material moving into the system. In Process Control, input denotes the effect of the surroundings on the chemical or biochemical process.

Output:denotes the effect of the process on the surroundings.

Input variables cause the output variables.

Page 17: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Example In the heated room example, what

are: The Input variable The Output variable

Page 18: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Important terms Controlled variable: it is the variable that

needs to be maintained or controlled at some desired value or range. Sometimes also referred to as process variable.

Set Point: it is the desired value of the controlled variable. Thus the job of a control system is to maintain the controlled variable at its set point.

Manipulated variable: is the variable used to maintain the controlled variable at its set point.

Disturbance: any variable that causes the controlled variable to deviate from its set point. Also referred to as upset.

Page 19: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Example In the room heating example, what

are the: Controlled variable Manipulated variable Possible Disturbance variable(s)

Page 20: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Why is Control necessary? Control is necessary because during

its operation, a chemical plant must satisfy several requirements imposed by its designers and the general technical, economic, and social conditions in the presence of ever changing external influences (disturbances). Such requirements are the following:

Page 21: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Safety The safe operation of a chemical process is

a primary requirement for the well-being of the people in the plant and for its continued contribution to the economic development.

Thus the operating pressures, temperatures, concentration of chemicals and so on should always be within allowable limits.

Page 22: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Production specifications A plant should produce the desired

amounts and quality of the final products.

For example, we may require the production of 2 million pounds of ethylene per day, of 99.5% purity. Therefore, a control system is needed to ensure that the production level and the purity specifications are satisfied.

Page 23: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Production specifications Product certification procedures

(e.g., ISO9000) are used to guarantee product quality and place a large emphasis on process control. http://www.iso.ch/iso/en/

ISOOnline.openerpage

Page 24: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Environmental regulations Various federal and state laws may specify

that the temperatures, concentrations of chemicals and flow rates of the effluents from a plant be within certain limits.

Such regulations exist for example on the amounts of SO2 that a plant can eject to the atmosphere, and on the quality of the water returned to a river or lake.

Page 25: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Operational constraints

The various types of equipments used in a chemical plant have constraints inherent to their operation. Such constraints should be satisfied throughout the operation of a plant.

For example, pumps must maintain a certain net positive suction head; tanks should not overflow or go dry; distillation columns should not be flooded; the temperature in a catalytic reactor should not exceed an upper limit since the catalyst will be destroyed. Control systems are needed to satisfy these operational constraints.

Page 26: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Economics The operation of a plant must conform

with the market conditions, that is, the availability of raw materials and the demand of the final products. Furthermore it should be as economical as possible in its utilization of raw materials, energy, capital and human labor. Thus, it is required that the operating conditions are controlled at given optimum levels of minimum operating cost, maximum profit and so on.

Page 27: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Why is control necessary? All the previous requirements

dictate the need for continuous monitoring of the operation of a chemical plant and external intervention (control) to guarantee the satisfaction of the operational objectives.

Page 28: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

How is control done

Control is accomplished through a rational arrangement of equipment (measuring devices, valves, controllers, computers) and human intervention (plant designers, plant operators), which together constitute a control system.

Page 29: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

The short answer to this question is:

Sensors, local indicators and valves are in the process.

Displays of all plant variables and control calculations are in a centralized facility.

Where is control implemented?

Page 30: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

What does control engineering “engineer”? Most of the engineering decisions

are introduced in the following five topics: Process Design Measurements Final elements Control structure Control calculations

Page 31: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Process Control Design We want to design a process that

we can then control well and easily. For example, we would like a

chemical plant to be more responsive.

By responsive we mean that the controlled variable responds quickly to adjustments in the manipulated variable.

Page 32: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Measurements A key decision is the selection and

location of sensors, because one can control only what is measured.

The engineer should select sensors that measure important variables rapidly and with sufficient accuracy.

Page 33: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Final elements

We will typically consider control valves as the final elements, with the percentage opening of these valves determined by a signal sent to the valve from a controller.

Page 34: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Control structure

The engineer must decide some very basic issues in designing a control system.

For example, which valve should be manipulated to control which measurement?

Page 35: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Control calculations

After the variables and control structure have been selected, equations are chosen that use the measurement and desired values in calculating the manipulated variable.

As we will see, we only need to develop a few equations that we will then use to control many different types of plants.

Page 36: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Duties of a Control Engineer Tuning controllers for performance

and reliability Selecting the proper PID mode

and/or advanced PID options Control loop troubleshooting Multi-unit controller design Documentation of process control

changes

Page 37: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Characteristics of Effective Process Control Engineers

Use their knowledge of the process to guide process control applications

Have a fundamentally sound picture of process dynamics and feedback control

Work effectively with the operators

Page 38: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Operator Acceptance

A good relationship with the operators is a NECESSARY condition for the success of a control engineer

Build a relationship with the operators based on mutual respect

Operators are a valuable source of plant experience

A successful control project should make the operators job easier, not harder

Page 39: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Process Control and Optimization

Control and optimization are terms that are many times erroneously interchanged

Control has to do with adjusting flow rates to maintain the controlled variables of the process at specified set-points

Optimization chooses the values for key set-points such that the process operates at the “best” economic conditions

Page 40: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Background needed for Process Control To be successful in the practice of automatic

process control, the engineer must first be familiar with the basic principles of thermodynamics, fluid flow, heat transfer, separation process, reaction processes etc.

Another important tool for the study and practice of process control is computer simulation. Many of the equations developed to describe processes are nonlinear in nature and consequently, the most exact way to solve them is by numerical methods. The computer simulation of process models is called simulation.

Page 41: CE-307 – CHEMICAL ENGINEERING DESIGN. CE-307 – Chemical Engineering Design Instructor – University at Buffalo Mattheos Koffas Teaching Assistant Chin

Example Book example