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Measurement and Control Basics 3rd Edition (complete book)

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Chapter 8 – Analytical Measurement and Control

235

electrochemical signal that is proportional to the concentration of CO gas in the ambient air. The resulting electrical signal is temperature compensated. The signal is also amplified by an electronic circuit to drive a frontpanel meter on the instrument for the purpose of indicating the percentage of CO.

Sulfur Dioxide Analyzers

Several types of general-purpose analyzers are available for measuring sulfur dioxide. Most utilize some form of spectrophotometry. Ultraviolet spectrophotometers provide high accuracy and sensitivity. Ranges as narrow as 0 to 100 ppm are encountered, but instruments can also detect concentrations up to 100 percent by volume. Ultraviolet analyzers are capable of fast response, that is, 1 s or less.

Infrared analyzers can also be used to measure sulfur dioxide. The instruments lack the sensitivity and response of ultraviolet devices, but are more versatile and less costly.

Fluorescence analyzers are used for sulfur dioxide monitoring in ranges from 0 to 0.25 ppm and 0 to 5,000 ppm. Such analyzers emit light when exposed to ultraviolet radiation, with an intensity that varies with the concentration of sulfur dioxide.

Nitrogen Oxide Analyzers

Nitrogen oxides are measured with spectral or electrochemical analyzers. Which instrument you select often depends on whether you desire data that show nitric oxide, nitrogen dioxide, or total oxides of nitrogen.

Chemiluminescence instruments are accurate and sensitive. These analyzers respond directly to nitric oxide; nitrogen dioxide must be reduced for detection to be possible. Chemiluminescence occurs when the samples react with ozone. Intensities, which are measured with photomultipliers, are correlated with nitric oxide concentration. Detection ranges vary from 0 to 0.1 ppm and 0 to 10,000 ppm. Instruments can be specified for concentrations as low as 0.5 ppm.

Ultraviolet analyzers are capable of monitoring oxide as well as dioxide. The lower detection limits are only 10 ppm for nitric oxide; therefore, converting the nitric oxide to the dioxide usually raises sensitivity. You should take measurements before and after the oxidation to compensate for initial nitrogen dioxide concentrations.

236 Measurement and Control Basics

Infrared analyzers are sensitive to nitric oxide but not to dioxide. Units are available for measurements from 0 to 1,000 ppm and 0 to 10,000 ppm. Ranges can also be specified for 0 to 1 percent and 0 to 10 percent.

Hydrogen Sulfide Analyzers

Hydrogen sulfide is difficult to monitor accurately and often must be conditioned chemically. Some analyzers expose sample gases to chemically treated paper tape. Hydrogen sulfide reacts with the tape, and the resulting color change is used to infer hydrogen sulfide concentration.

Conventional fluorescence analyzers are also used to monitor hydrogen sulfide, but the hydrogen sulfide is first converted to sulfur dioxide. Automatic titrators are also employed to determine hydrogen sulfide concentrations.

Ultraviolet analyzers respond to hydrogen sulfide, but their sensitivities are low. Polarographic instruments can also be used, but filters must be used to remove unsaturated hydrocarbons.

Analyzer Measurement Applications

We will close the discussion of analyzers with a measurement system application that uses a gas analyzer. A typical SO2 stack analyzer instrument loop is shown in Figure 8-19. The system consists of an SO2 analyzer, a temperature element, and a flow measurement system. The temperature and flow signals are used in this system to obtain the amount of SO2 in pounds per hour. The computation is made in the control unit (AIT). Note that electrical heat tracing has been used on the analyzer sample line to keep the SO2 in the gaseous state.

The analyzer’s operation is based on the absorption of light by the sample gas. Rigidly defined, light is only that narrow band of electromagnetic radiation visible to the naked eye, as discussed earlier. However, in this discussion the term light is used to refer to electromagnetic radiation over the specific wavelengths covered by the analyzer. Wavelengths used for SO2 analysis are in the 280to 313-nm range for the measuring channel and 578 nm for the reference channel.

Figure 8-20 shows a block diagram of a typical SO2 analyzer. The optical system operates as follows: radiation from the light source (A) passes through the sample (B) by flowing through a sample cell. Some light of the measuring wavelength is adsorbed by SO2 in the sample. Light transmitted through the sample is divided by a semitransparent mirror (C) into two beams (D and H). Each beam then passes through its own optical filter

Chapter 8 – Analytical Measurement and Control

237

AE

Electrical

 

100

 

Heat Tracing

 

 

 

 

 

AT

 

 

100

Sample Tube

SO2

 

TT

 

AIT

100

 

100

FT 100

Pitot Tube

Figure 8-19. SO2 stack gas analyzer

(E or I). Each filter permits only a particular wavelength to reach its associated phototube (G or K).

Optical filters in one beam permit only radiation at the measuring wavelength (J) to pass through. The measuring wavelength is chosen so that light intensity reaching the photomultiplier tube or phototube (K) varies greatly when SO2 concentration changes.

The optical filter in the second beam permits only light at the reference wavelength (F) to pass through. The reference wavelength is chosen so that light intensity reaching the reference phototube (G) varies little or not at all when SO2 concentration changes. Each phototube sends a current to its logarithmic amplifier (log amp) that is proportional to the intensity of the light striking the phototube. The signal output of the analyzer circuit is the voltage difference produced by the log amps.

If SO2 concentration increases, light arriving at the measuring phototube decreases, as does the measuring phototube current. The reference circuit is unaffected. Since voltage generated in the measuring circuit increases with the drops in phototube current, the output voltage (measuring voltage minus reference voltage) rises with a concentration increase.

This analyzer’s design also provides inherent compensation for changes in overall light intensity. Factors such as light source variations or dirt on the

238 Measurement and Control Basics

 

Semi-transparent mirror

Sample Out

 

Phototube

 

 

 

 

 

 

 

 

Light

J

H

C

 

 

Source

 

 

 

 

K

I

 

 

B

A

 

Optical filter

D

 

 

 

 

 

 

 

 

 

 

 

 

Sample In

 

 

 

E

Optical filter

 

Log Amplifier

 

F

 

 

 

 

 

 

 

 

 

 

G

Phototube

 

Analyzer

 

Log Amplifier

 

 

 

Circuitry

 

 

 

 

 

 

 

 

 

Recorder

 

 

 

 

 

Figure 8-20. SO2 analyzer block diagram

cell windows, which affect equally the intensities of both the measuring and reference wavelengths, will change the output voltages to an equal extent. Therefore, these variations have minimal net effect on the difference or the final output voltage.

EXERCISES

8.1Given the following resistance values: (a) 50,000 , (b) 200,000 ,

(c) 250,000 for a given solution, calculate the conductance of each solution.

8.2The [OH] ion concentration of an aqueous solution is 10–11. What is the value of the H+ ion concentration and pH? Is the solution basic or acidic?

8.3The specific gravity of a lead-acid cell in a 12-v (six-cell) battery is 1.24. Calculate the no-load voltage of the battery.

8.4Calculate the span in inches of a differential-pressure density instrument if the minimum specific gravity is 1.0, the maximum

Chapter 8 – Analytical Measurement and Control

239

specific gravity is 1.25, and the difference in liquid elevation is 50 in.

8.5If the air temperature is 80°F and the atmospheric pressure is 29.92 inHg, what is the maximum moisture content of the air?

8.6What is the frequency of an electromagnetic radiation source that has a wavelength of 100 meters?

8.7Find the photon energy and calculate the number of photons in an EM pulse that has an energy of 1 joule and a frequency of 1 x 109Hz.

8.8What is the intensity of a 1000-w point light source at 10 meters and 20 meters?

8.9What is the maximum wavelength for a resistance change by photon absorption for a CdS semiconductor?

8.10A photovoltaic cell generates 0.3 volts open-circuit when it is exposed to 10 w/m2 of radiation intensity. What is the open-circuit voltage of the cell at 20 w/m2?

BIBLIOGRAPHY

1.Considine, D. M. (ed.). Process Instruments and Controls Handbook, 3d ed., New York: McGraw-Hill, 1985.

2.Foxboro Company. Conductivity Cells. Technical Information, Foxboro, MA: The Foxboro Company, 1962.

3.Foxboro Company. Ion-Selective Measuring Electrodes. Technical Information, Foxboro, MA: The Foxboro Company, 1965.

4.Foxboro Company. Fundamentals of Ion-Selective Measurements. Technical Information, Foxboro, MA: The Foxboro Company, 1972.

5.Foxboro Company. pH Electrodes and Holders. Technical Information, Foxboro, MA: The Foxboro Company, 1979.

6.Foxboro Company. Theory and Application of Electrolytic Conductivity Measurement. Technical Information, Foxboro, MA: The Foxboro Company, 1982.

7.Kirk, F. W., and N. F. Rimboi. Instrumentation, 3d ed. Homewood, IL: American Technical Publishers, 1975.

8.Moore, R. L. Basic Instrumentation Lecture Notes and Study Guide. Volume 2, Process Analyzers and Recorders, 3d ed., Research Triangle Park, NC: ISA, 1982.

9.Quagliano, J. V. Chemistry, 2d ed., Englewood Cliffs, NJ: Prentice-Hall, 1963.

9

Flow Measurement

Introduction

We begin this chapter by discussing the basic principles of flow, then move on to derive the basic equations for flow velocity and volumetric flow. The chapter concludes with a discussion of the common types of flow-measur- ing devices and instruments, such as orifice plates, venturi tubes, flow nozzles, wedge flow elements, pitot tubes, annubars, turbine flowmeters, vortex shedding devices, magnetic flowmeters, ultrasonic flowmeters, positive-displacement flowmeters, mass flowmeters, and rotameters.

The study of fluids in motion, or flow, is one of the most complex branches of engineering. This complexity is reflected in such familiar examples as the flow of a river during a flood or a swirling cloud of smoke from a process plant smokestack. Each drop of water or each smoke particle is governed by Newton's laws, but the equations for the entire flow are very complicated. Fortunately, idealized models that are simple enough to permit detailed analysis can represent most situations in process control.

Flow Principles

Our discussion in this chapter will consider only a so-called ideal fluid, that is, a liquid that is incompressible and has no internal friction or viscosity. The assumption of incompressibility is usually a good approximation for liquids. A gas can also be treated as incompressible if the differential pressure driving it is low. Internal friction in a fluid gives rise to shearing stresses when two adjacent layers of fluid move relative to each other, or when the fluid flows inside a tube or around an obstacle. In most cases in

241

242 Measurement and Control Basics

process control, these shearing forces can be ignored in contrast to gravitational forces or forces from differential pressures.

All flow involves some form of energy. Energy can be expressed in many different forms, including thermal, chemical, and electrical. However, flow measurement focuses on two main types of energy: potential and kinetic. Potential energy (U) is defined as force (F) applied over a distance (d), or

U = Fd

(9-1)

Kinetic energy (K) is defined as one-half the mass (m) times the square of velocity of the body in motion, or

K =

1

mv2

(9-2)

 

2

 

 

Potential Energy

The term potential energy probably came from the idea that we give an object the “potential” to do work when we raise it against gravity. The potential energy of water at the top of a waterfall is converted into a kinetic energy of motion at the bottom of the fall.

Potential energy is usually applied to the work that is required to raise a mass against gravity. Force is defined as mass (m) times acceleration (a):

F = ma

(9-3)

Therefore, the work (W) required to raise a mass through a height (h) is expressed as follows:

W = Fh = mgh

(9-4)

where g is the acceleration of the object due to gravity. The term mgh is called gravitational potential energy, or

U = mgh

(9-5)

This energy can be recovered by allowing the object to drop through the height h, at which point the potential energy of position is converted into the kinetic energy of motion.

Work and Kinetic Energy

The work that a force does on a body is related to the resultant change in the body's motion. To develop this relationship further, consider a body of mass m being driven along a straight line by a constant force of magnitude

Chapter 9 – Flow Measurement

243

F that is directed along the line. Newton’s second law gives the acceleration of a body as follows:

F = ma

(9-6)

Suppose the speed increases from v1 to v2 while the body undergoes a displacement d. From standard analysis of motion, we know that

v12 = v22 + 2ad

(9-7)

or

 

 

 

 

 

 

 

a =

v22 v12

 

 

(9-8)

 

2d

 

 

 

 

 

Since F = ma,

 

 

 

 

 

 

 

F = m

v22 v12

 

(9-9)

2d

 

 

 

 

 

therefore,

 

 

 

 

 

 

 

Fd =

1

mv22

1

mv12

(9-10)

 

 

2

 

2

 

 

 

 

The product Fd is the work (W) done by the force (F) over the distance d. The quantity 1/2mv2—that is, one-half the product of the mass of the body and the square of its velocity—is called its kinetic energy (KE).

The first term on the right-hand side of Equation 9-10, which contains the final velocity v2, is the final kinetic energy of the body, KE2, and the second term is the initial kinetic energy, KE1. The difference between these terms is the change in kinetic energy. This leads to the important result that the work of the external force on a body is equal to the change in the kinetic energy of the body, or

W = KE2 KE1 = ∆ KE

(9-11)

Kinetic energy, like work, is a scalar quantity. The kinetic energy of a moving body, such as fluid flowing, depends only on its speed, not on the direction in which it is moving. The change in kinetic energy depends only on the work (W = Fd) and not on the individual values of F and d. This fact has important consequences in the flow of fluid.

For example, consider the flow of water over a dam with height, h. Any object that falls through a height h under the influence of gravity is said to

244 Measurement and Control Basics

gain kinetic energy at the expense of its potential energy. Let's assume that water with mass m falls through the distance h, converting all its potential energy (mgh) into kinetic energy. Since energy must be conserved, the kinetic energy must equal the potential energy. Therefore,

mgh =

mv2

(9-12)

 

2

 

This equation can be solved for velocity v to obtain the following:

v = 2gh

(9-13)

Equation 9-13 shows that the velocity of water at the base of the dam depends on the height (h) of the dam and on gravity (g). Since gravity is constant at about 32 ft/sec 2 or 9.8 m/sec2 on the earth’s surface, the velocity depends only on the height h and not on the mass of the flowing fluid. This is an important property in the study of fluid flow. The following example will illustrate this property.

EXAMPLE 9-1

Problem: A valve is opened on the bottom of a storage tank filled to a height of 4 feet with water. Find the discharge velocity of the water just after the outlet valve is opened.

Solution: The velocity can be found from Equation 9-13 as follows:

v = 2gh

v = 2(32 ft / sec2 )(4 ft) =16 ft / sec

Flow in a Process Pipe

Another example of the relationship between energy and fluid velocity is the flow of fluid in a process pipe of uniform and fixed cross section (A), as shown in Figure 9-1. The differential pressure (∆ P) between the inlet and the outlet causes the fluid to flow in the pipe.

The flow of fluid is maintained by the energy difference between the inlet and the outlet. Let’s find the fluid velocity (v) in terms of the inlet pressure P1 and the outlet pressure P2, assuming no energy loss in the pipe. Since the pipe has a uniform area A, the pressure at the inlet is P1 and the pres-

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