The Future of Nuclear Power

The Future of Nuclear Power

 In 1933, a Hungarian-American physicist Leó Szilárd  conceived the nuclear chain reaction and patented the idea of a nuclear reactor jointly with the American-Italian Enrico Fermi. It took 18 years for electricity to be first generated by a nuclear reactor at an experimental station near Arco, Idaho. The world’s first commercial reactor was the Calder Hall station in England and the first plant to generate electricity for a power grid was the Obninsk nuclear power plant in theSoviet Union in 1954.

 

During the last 60 years, nuclear energy became an important component in the energy mix used by mankind. It supplies about 5% of the total global energy consumption or about 13.5% of the electricity we use. In theUnited Statesnuclear energy is the source of about 8% of the total energy consumption or about 20% of the electricity used.

 

The nation most dependent on nuclear electricity isFrance(75%), followed byBelgiumandSlovakia(52%), whileChinais the least dependent on it (around 2%). To date the only nation that has decided to shut down all its nuclear power plants (by 2022) isGermany. That nation today obtains 28% of it’s electricity from nuclear reactors.

 

Globally, 435 nuclear power plants are in operation and 60 are under construction. In the United States 104 are in operation, one is under construction and 28 have been shut down. Globally, due to ageing, 138 nuclear power plants have been shut down, but because of the high cost of dismantling and decontamination of the sites, only about 17 been fully decommissioned. In theUSAthe decommissioning of 13 plants is in progress. In addition to serving power generation, there are 240 reactors serving research and 150 reactors supplying energy for nuclear submarines and other ships around the world.

 

Earlier nuclear plants were often located near populated areas and these early plants were designed for only 30 years of operation. The life expectation of newer plants is usually 40 years and today, the average age of all operating plants is 27 years. The age of 138 operating plans is between 30 and 40 years, while 24 are already over 40 years old. 

 

As of 2008, the installed capacity of all the operating plants in the world amounted to 413 GW (119 GW in theUnited States), while their actual electricity production rate was about 300 GW (~ 100 GW in theUnited States).

 

To date, the global investment to build nuclear power plants amounted to about $3 trillion (approximately $0.75 trillion in theUnited States). The cost of their eventual decommissioning is expected to be about another trillion dollars. If we also consider the associated costs of building and operating the uranium mines and also the cost of the temporary and eventually the permanent nuclear waste storage facilities, the total investment in the global nuclear industry is estimated to be about $5-$6 trillion. For comparison purposes, the global GWP today is about $65 trillion (USAabout $16 trillion).

 

 

The history of the last 60 years shows that after the accidents at 3 Mile Island and Chernobil the building of new nuclear power plants slowed down and the percentage of global electricity consumption that is met by nuclear power dropped from about 18% in the early 1990s to 13.5% today. It seems that this trend will continue after Fukushima, because of the ageing of the operating plants, the risks associated with cyber and conventional terrorism, military attacks, earthquakes and other causes, plus because the permanent storage of nuclear waste is still unresolved. Yet another concern is the increase of radiation in our global environment – including the doubling of the concentration of nuclear radiation in the atmosphere.

 

While these concerns are all valid, it is also a fact that the use of nuclear power can not abruptly be terminated, but has to be phased out gradually. Fortunately, it is also a fact that the operation of nuclear power plants can now be made much safer. Yet, in many respects they are not! Let me give some examples:

 

The nuclear power generation process is a relatively simple one: First the heat from the fuel rods is transferred into high pressure water that carries it into a boiler where steam is generated. Next, the energy of the steam is converted into electricity, while the waste heat from the turbines is taken to cooling towers to be rejected into the atmosphere.

 

Keeping such a process safely in operation requires only three things. Two of these are self-evident: 1) The need to  keep the fuel rods covered by water to protect them from overheating and 2) To maintain the integrity of the containment building to prevent radiation from escaping. The third requirement is not so obvious, yet it was a main contributor to the accidents at 3 Mile Island, Chernobil and alsoFukushima. Let me briefly review all three causes:

 

Keeping the fuel rods from overheating and melting is guaranteed so long as the flow of cooling water is uninterrupted. As the operation of the cooling water pumps requires energy, that must be made available even if it’s outside source fails. This means not only that properly sized diesel and battery backup systems must be provided and must be located at safe elevations, but also means that the steam which, even during an accident is still being generated, must not be wasted, but must be made useable to drive backup cooling water pumps.

 

The second requirement is that the containment buildings must withstand both external and internal impacts. External impacts can originate from earthquakes, terrorist or military attacks, while internal impacts can be caused by events as like hydrogen explosions. Such explosions must be prevented by filling the containment building with inert gas, so that there is no oxygen present to support an explosion. In addition, automatic pressure release must also be provided and be furnished with filters to protect from the release of radioactive particles into the atmosphere.

 

The third requirement to achieve safe operation is the most neglected today. It is the need to protect the power plant from human error. In an age, when we can safely operate a nuclear powered robot on Mars, it is inexcusable to see that the safety systems protecting nuclear power plants are not fully automated. We have seen that in the cases of 3 Mile Island, Chernobil and Fukushima, the windows of opportunity for safe shut-down were lost, because the decisions on what to do were left up to panicked operators and PR oriented managers and because of their hesitation the window of opportunity for corrective action was not utilized.

 

Therefore, it is time for full automation, it is time for using measurement devices that can be trusted, it is time to install “firewalls” to completely isolate the operating controls from potential cyber attacks and most importantly, it is essential to fully automate the safety systems, so that for example, when an earthquake is detected, flooding of the reactors is automatic and immediate, instead of time being wasted until the tsunami waves arrive.    

 

I agree with the environmentalists, who argue that we can not continue to live with energy sources that are inherently dangerous, because of the radioactivity or global warming that they cause. I also agree with them that resources are wasted on “scraping the bottom of the fossil barrel” or on waging “oil wars”. On the other hand, I disagree, if they believe that just by voting out denier politicians, we can switch to a safe energy-economy overnight. No, we can not! The transition to a safe energy economy has to be gradual no matter who is in the White House. It will take a decade or even a generation until this new “Marshall Plan” is completed.

 

Therefore, it is in the interest of all to increase the safety of today’s energy industry by replacing manual controls with full automation during the coming transition period.

 

Béla Lipták PE

Safety and automation consultant

www.belaliptakpe.com    

 

 

 

 

 

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CONTRIBUTORS WANTED

Dear Colleague,

We are working on the 5th edition of my Instrument Engineer’s Handbook and are looking for experts to update existing or prepare new chapters in Volume 1, which deals with Measurement and Analysis.

If you feel qualified or if you know colleagues who are experts  in the various areas of measurement and analysis, please review the Contents below and contact the Volume Editor, Mrs. Kriszta Venczel at: kvenczel@gmail.com (not me!) indicating which existing chapter you would like to update or which new one you would like to prepare?

Béla Lipták, PE
President of Béla Lipták Associates, PC
Automation and Safety Consultants
84 Old N. Stamford Rd, Stamford CT. 06905
T/F: 203-357-7614, E: liptakbela@aol.com
www.BelaLiptakPE.com

 

 

IAEH, 5th Edition: CONTENTS

(299-137 unassigned~50%)

General Considerations  1

(14 Total – 1 Unassigned)

 

New Ch. No.

Old Ch. No.

Title

4th Ed. Author

5th Edition Author

Assigned

1

1.6

Accuracy

Lipták

Lipták

1a

 

Accracy, Stochiastic and Economic

 

Bagajewich

2

1.12

Binary Logic Diagrams (ISA 5.2)

Gilbert

Gilbert

3

1.8

Calibration

Hashemian

Becker

 

4

1.6

Configuring Intelligent Devices

Berge

Has..

Pinceti

5

1.11

Evaluation and Life Cycle

Smith

Berge

L.Rajagopalan

7

1.7

Installation

Gibson

 

Yuwono

9

-

Maintenance

None

 

Becker

 

10a

-

Performance

-

Moreno

11

1.9

Response Time and Drift Testing

Hashemian

 

 

12

7.18

Soft Sensors

Bain

ROMEL S BHULLAR

13

1.3

Terminology and Testing

Lipták

Lipták

 

 

14

1.5

Uncertainty: Estimation, Propagation, and Reporting

Dieck

Rheinhart

 

 

 

Flow Measurement Devices  2

(42 – 17 Unassigned)

 

 

New Ch. No.

Old Ch. No.

Title

4th Edition Author(s)

5th Edition Author(s)

Assignedr 2

15

2.1

Flowmeter Selection

Lipták

Lipták

 

16

-

Service: Abrasive, Corrosive, Slurry, Viscous

-

Connella

17

-

Service: Bi-Directional Flows

 

 

 

18

-

Service: High and Low Temperature

 

 

 

19

-

Service: Semi-filled Pipes or Multi-Phase Flows

-

Gambir

20

2.17

Service: Polyphase Flows of Oil, Water and Gas

Gibson

Gambhir

21

-

Service: Non-contact, Non-Penetrating Designs

 

 

 

22

-

Installation: D/P Sensors and Transmitters

-

Conella

23

-

Installation: Types of Manifolds

-

Ofoh

Conella

24

-

Maintenance and Calibration

-

Ohof

Wagelin

25

2.2

Anemometers

Lipták

 

 

26

2.3

BTU Flowrate in Heat Exchangers

Lipták

 

 

27

2.4

BTU Flowrate Provided by Gaseous Fuels

Lipták

 

 

28

2.5

Cross Correlation Design

Hashemian

 

 

29

2.6

Elbow Taps

Gibson

 

 

30

2.7

Flow Switches

Boyes

Muhammad Fahad

31

2.8

Jet Deflection Design

Lipták

 

 

32

2.9

Laminar Flow Measurement

Arant

 

 

33

2.10

Magnetic Flowmeters

Eren

Thomson,

 

34

2.11

Mass Flow – Coriolis

Anklin/Drahm

Martin Anklin/Wolfgang Rahm

 

35

2.12

Mass Flow – Miscellaneous

Jamison

 

 

36

2.13

Mass Flow – Thermal

Baan

Baan

 

37

2.14

Metering Pumps

Boyes

 

 

37a

-

Multiphase Measurement

-

Gambhir

38

2.15

Orifice Plates, and Their Sizing

Arant

Connella,

39

-

Orifices for Restriction

-

Yuwono,

 

40

2.16

Pitot and Area Averaging Tubes

Lipták

 

 

41

2.18

Positive Displacement Gas Meters

Yoder

Ofoh

 

42

2.19

Positive Displacement Liquid Meters and Provers

Lipták

Ofoh

 

43

2.20

Purge Flow Regulators

Lipták

Djkman

Von Goethem

 

44

2.21

Segmental Wedge

Lipták

 

 

45

2.22

Sight Flow Indicators

Sanders

 

 

46

2.23

Solids Flowmeters and Feeders

Lipták

 

 

46a

-

Sonar Flowmeter

-

Muhammad Fahad

47

2.24 

Target Meters

Boyes

 

 

48

2.25 

Turbine and Rotary Element Designs

Arant

Von Goethem

 

49

2.26 

Ultrasonic Meters: Transit-Time and Doppler

Yoder

Baker

50

2.27 

Variable Area (Rotameters), Gap and Vane Designs

Baan

Von Goethem

Djkman

 

51

2.28 

V-Cone

Boyes

Voss

 

52

2.29 

Venturi Tubes, Flow Tubes and Flow Nozzles

Arant

Connella

 

53

2.30 

Vortex and Fluidic Meters

Boyes

Connella

54

2.31 

Weirs and Flumes for Open Channels

Pawlowski

 

 

 

 

 

 

3 Level Measurement

(27 – 9 unassigned)

 

New Ch. No.

Old Ch. No.

Title

4th Edition Author(s)

5th Edition Author(s)

Assignedtus

55

3.1

Selection of Level Detectors

Roede

Mark H. Murphy

√√

55a

-

Installation considerations

 

Oscar Castañeda Vazquez

56

-

Applications – Interface, foam, boiling services

 

Rob E.V. Koene, Simon

57

-

Applications – Non-contacting, non-penetrating

 

Mark H. Murphy

58

-

Applications: – Water level in nuclear reactor core

 

Lipták,

58a

-

Applications: – Oil and LNG Tank Gauging

-

 

 

59

 

Applications: Slurry, sludge, coating fluids

 

Murphy

 

60

 

Applications: Solids Including Sticky Solids

 

Murphy

 

60a

-

Application – Sulfur

-

Alejandro Varga

 

61

 

Accessories: Manifords

 

Murphy

 

62

 

Accessories: Chemical Seals

 

Murphy

 

63

3.2

Bubblers

Langford

Cullen Langford,

 

64

3.3

Capacitance and Radio Frequency Admittance

Roede

David L. Ubert

65

3.4

Conductivity and Field Effect Level Switches

Lipták

 

 

66

3.5

Diaphragm Type

Roede

 

 

67

3.6

Differential Pressure, Hydrostatic Designs

Nay

Allen D. Houtz,

68

3.7

Displacer Devices

Langford

Cullen Langford,

 

69

3.8

Float Type Sensors

Langford

Michael Connella III

70

3.9

Laser Sensors

Vujicic

Michael Connella III

71

3.10

Level Gauges Including Magnetic

Nyce

David S. Nyce

71a

-

Magnetostrictive

-

David S. Nyce

72

3.11

Microwave  Switches

Boyes

 

 

73

3.12

Optical Level Sensors

Lipták

 

 

74

3.13

Radar, Non-Contacting

Boyes

GAMBHIR/Yadav

 

75

3.14

Radar, Contacting Designs (TDR, GWR, PDS)

Carsella

Robert J. Botwinski

 

76

3.15

Radiation Type Sensors

Rodgers

Andrew J. Livingston

77

3.16

Resistance Tapes

Lipták

 

 

78

3.17

Rotating Paddle Switches

Boyes

 

 

79

3.18

Tape and Float Designs

Lipták

SREENEVASAN

80

3.19

Thermal Sensors

Lipták

 

 

81

3.20

Ultrasonic Detectors

Jamison

Michael Connella III

82

3.21

Vibrating Switches

 

Lipták

 

 

 

 

Temperature Measurement    4

(21 – 10 unassigned)

 

New Ch. No.

Old Ch. No.

Title

4th Edition Author(s)

5th Edition Author(s)

Assignedus

83

4.1

Selection of Temperature Sensors

Adler/Moore

Deepak Deore

84

 

Applications – Cryogenic

 

Jesús Gallego Otero

85

 

Applications – High Temperature

 

Huaichun Zhou

86

 

Applications in Hostile Environments

 

 

 

87

 

Applications to Eliminate Interferences

 

 

 

88

4.3

Calibrators and Simulators

Edvi/Jamison

John Thompson,

 

89

4.14

Installation Considerations and Thermowells

Lipták

Michael Connella III

 

90

4.2

Bimetallic Thermometers

Edvi/Jamison

Michael Connella III

91

4.4

Cones, Crayons, Labels, Paints and Pellets

Edvi/Jamison

 

 

92

4.6

Filled Bulb and Glass Stem Thermometers

Jamison

 

 

93

4.7

Integrated Circuitry (IC), Transistor and Diode Designs

Lipták

 

 

94

4.8

Miscellaneous Sensors

Sloneker/Jamison

 

 

94a

-

Multipoint Sensors

 

Bhagyashree Pataskar

95

4.5

Optical Fiber Thermometers (OFT)

Lipták

Dennis Horwitz

96

4.9

Pyrometers – Radiation and Infrared (IR)

Lipták

 

 

97

4.10

Resistance Temperature Detectors (RTDs)

Lipták

Michael Connella III

98

4.11

Temperature Switches and Thermostats

Adler/Moore

 

 

99

4.12

Thermistors

Giráo

 

 

100

4.13

Thermocouples (TC)

Lipták

Daniel Alonso-Alvarez

 

100a

4.14

Thermowells

Lipták

Mark H. Murphy

101

4.15

Ultrasonic and Sonic Thermometers

Lipták

 

 

 

Pressure Measurement    5

(23 – 13 unassigned)

New Ch. No.

Old Ch. No.

Title

4th Edition Author(s)

5th Edition Author(s)

Assignedatus

102

5.1

Orientation and Selection

Nay

 

 

103a

5.2

Accessories: Calibrators

Nay

Pantay Patel???

Alejandro Varga ???

 

103b

5.2

Accessories: Chemical Seals

Nay

Pantay Patel???

Alejandro Varga ???

 

104

5.3

Bellows Type Sensors

Jamison/Edvi

 

 

105

5.4

Bourdon and Helical Sensors

Jamison/Edvi

 

 

106

 

Capacitance Sensors

 

Ajay V. Deshmukh

107

5.5

Diaphragm or Capsule Elements

Jamison

 

 

108

5.6

Differential Pressure (D/P) Detectors

Lipták

Michael Connella III

109

8.20

Differential Vapor Pressure Sensors

Lipták

 

 

110

-

D/P Installations and Manifolds

-

Emmanuel Ujiro

 

111

5.7

Electronic Pressure Sensors

Lipták

Keith Sommers???

 

112

5.8

High Pressure Sensors

Lipták

 

 

113

 

Magnetic (Inductive, Reluctive and LVDT)

 

Ajay V. Deshmukh

114

5.9

Manometers

Welch

 

 

115

 

Optical detectors

 

 

 

116

 

Piezoelectric Detectors

 

Ajay V. Deshmukh

117

 

Potentiometric Sensors

 

Mehul Pancholi

118

5.11

Pressure Gauges

Jamison/Edvi

Mark H. Murphy

119

5.12

Pressure Repeaters

Lipták

 

 

120

5.10

Pressure Scanners

Lipták

 

 

121

5.13

Pressure and D/P Switches

Lipták

John W Thompson

122

 

Resonant Wire Elements

 

 

 

123

 

Strain Gauge Type Sensors

 

Mehul Pancholi

124

5.14

Vacuum Sensors

Gilbert

 

 

 

 

 

DENSITY    6

(12 – 6 unassigned)

New Ch. No.

Old Ch. No.

Title

4th Edition Author(s)

5th Edition Author(s)

Assignedus

125

6.1

Application and Selection

Jamison/Edvi

Victor Vagelin

126

-

Accoustic Densitometers

-

 

 

127

6.2

Displacement and Float Densitometers

Jamison/Edvi

 

 

128

6.10

Gas Densitometers Including Position Based

Langford

Cullen Langford

129

6.3

Hydrometers

Lipták

 

 

130

6.4

Hydrostatic Densitometers

Lipták

Hesham Fandy

131

6.5

Coriolis Densitometer

Jamison

Emmanuel Ujiro

132

6.6

Nuclear Radiation Densitometers

Livingston

Andrew J. Livingston

 

133

6.7

Ultrasonic Sludge and Slurry Densitometers

Lipták

 

 

134

 

Torsional Vibration Type

 

 

 

135

6.8

Vibrating and Resonance Densitometers

Murer

Martin Apschner

136

6.9

Weight Based Densitometers

Lipták

 

 

 

 

SAFETY SENSORS    7

(26-7 unassigned)

New Ch. No.

Old Ch. No.

Title

4th Edition Author(s)

5th Edition Author(s)

Assigned

136a

-

Alarm System Management

-

Lipták

137

 

Air – Quality and Safety

 

 

 

139

8.16

Combustibles

Tatera

Gupta

140

8.19

Corrosion Monitoring

Lipták

 

 

141

7.5 

Excess Flow and Regular Check Valves

Lipták

 

 

141a

-

Deluge Systems

-

Jef Snoeys

142

-

Explosion Proofing

-

Simon Lucchini

143

7.6 

Explosion Suppression and Deluge Systems

Lipták

Raju

144

7.7 

Flame Arresters, Emergency Vents

Lipták

 

 

145

7.8 

Flame, Fire and Smoke Detectors

Lipták

Hesham Fandy

146

-

Inert Gas Purging

-

Kumar

147

7.2 

Intrinsic Safety

Rohr

Hesham Fandy

148

7.9  

Leak Detectors

Lipták

Simon Lucchini

148a

-

Nuclear Radiation Detectors

-

Dr. Ajay V. Deshmukh

149

-

Pipe Condition Detectors, “Pigs”

-

Béla Lipták

150

1.10

Redundant and Voting Systems

Berge

Simon Lucchini

151

7.15 

Relief Valves – Capacity Determination

 

Mark Murphy,

 

152

7.16 

Relief Valves – Sizing, Specification, Installation

 

Mark Murphy

 

153

7.17 

Rupture Discs

Miller

Dean Miller

154

-

Safety – Fracking

-

 

 

155

-

Safety – Nuclear Power Plants

-

 

 

156

-

Safety – Offshore Drilling

-

ROMEL S BHULLAR

157

-

Safety – Pipeline Operation

-

ROMEL S BHULLAR

157a

-

SIS Systems, SIL Calculations

-

Wright

 

158

8.59

Toxic Gas Monitoring

Jarvis

Gupta

158a

-

Vacuum Breakers and Air Release

-

 

 

159

7.22 

Vibration, Shock, Acceleration

Eren

Bapat Jayprakash Gajanan

 

        

 

 

  ENERGY INDUSTRY INSTRUMENTS     8

(18 – 11 unassigned)

New Ch.No.

Old Ch. No.

Title

4th Edition Author(s)

5th Edition Author(s)

Assigned

161

8.14 

Coal Analyzers

Lipták

 

 

162

8.21

Dioxin Analysis

Lipták

 

 

163

 

Electric Meters – Bi-Directional

 

 

 

164

7.3   

Electric Meters – Conventional

Giráo

 

 

165

 

Electric Meters – Smart 

 

 

 

166

7.4    

Energy Management, Load Shedding

Lipták

ROMEL S BHULLAR

167

 

Fuel Cell Sensors

 

 

 

168

 

Geothermal Sensors

 

 

 

169

8.8   

Heating Value Calorimeters

Lewko

 

 

169a

-

Multiphase Oil & Gas Sensors

-

Ofoh Emmanuel Ujiro

170

-

Natural Gas Measurements

-

David Gallego

171

-

Nuclear Reactor Measurements

-

 

 

172

-

Oil Quality Analyzers

-

 

 

174

-

Solar -  Collector Positioning Sensors

-

Daniel Alonso-Alvarez

175

-

Solar – Converters

-

Seethepalli

176

-

Solar – Insolation Sensors

-

 

 

177

8.3   

Stack Particulate Sampling

Lipták

 

 

178

-

Wind Turbine Instruments 

-

Ramirez, Raul Garduno

 

 

PROPERTIES and CONDITIONS    9

(45-29 unassigned)

New Ch. No.

Old Ch. No.

Title

4th Edition Author(s)

5th Edition Author(s)

Assigned

178a

8.7

BOD, COD, TOD

Tatera

 

 

179

7.1

Boroscopes, Visual Inspection Tools

Lipták

 

 

180

 

Coagulation Related Measurements

 

 

 

181

8.17 

Conductivity Measurement

Gray

 

 

182

8.15 

Colorimeters

Reed

 

 

183

8.18

Consistency Measurement

Waller

 

 

184

 

Earthquake Monitoring, Tremor Seismographs

 

 

 

185

8.23

Fiber-Optic Probes

Reed

 

 

187

8.27

Infrared, IR and NIR Measurements

Baughman

Ajay V. Deshmukh

188

8.28

Ion-Selective Electrodes

Durden

 

 

189

7.11 

Machine Vision Technology

Reed

 

 

190

8.29

Mass Spectrometers

Gilbert

 

 

191

7.12 

Metal Detectors

Lipták

 

 

192

8.35

Molecular Weight

Lipták

 

 

192a

-

Multiple Gas FTIR Monitors, Spectrometers

-

 

 

193

7.13 

Noise Sensors

Lipták

Bapat Prakash

194

-

Nuclear Radiation

-

Ajay V. Deshmukh

195

8.38 

Odor Detection

Durden

 

 

195a

8.41

Oxidation-Reduction Potential (ORP)

Lipták

Michael Connella III

196

8.46

Particulates, Smoke, Dust  and Opacity

Lipták

 

 

197

8.47 

Particle Size and Distribution

Lipták

Simon Wilson

197a

8.48

pH Measurement

Gray(2003)

McMillan (1995)

Michael Connella III

198

8.50 

Physical Properties – ASTM Methods

Verhappen

Ian Verhappen

199

7.10 

Position, Linear and Angular

Berge

Dennis Horwitz

200

7.14 

Proximity Sensors and Limit Switches

Lipták

Paul Katende

 

201

8.51

Raman Analyzers

Sethi

Ajay V. Deshmukh

202

8.52

Refractometers

Lipták

 

 

203

8.53

Rheometers

Magda

 

 

203a

-

Sand and Erosion Detection

-

HARVINDAR S GAMBHIR and Satish Yadav

204

8.40

Spectrometry, Open Path (FT-IR, IR, UV)

Jarvis

Ajay V. Deshmukh

205

7.19 

Tachometers and Angular Speed Detectors

Lipták

 

 

206

8.57

Thermal Conductivity Detectors

Lipták

 

 

207

7.20 

Thickness and Dimension

Lipták

 

 

208

-

Thickness, Conditon of  Pipeline Walls (PIGs)

-

 

 

209

7.21 

Torque and Force

Giáro

 

 

209a

8.58

Total Carbon Analyzer (TOC)

Lee-Alvarez

 

 

210

8.60 

Turbidity, Sludge and Suspended Solids

Lipták

SREENEVASAN

 

211

8.61

Ultraviolet and Visible Analyzers

Lipták

Phil Harris

212

8.62

Viscometers – Application and Selection

Lipták

Victor Wegelin

213

8.63

Viscometers – Laboratory

Lipták

Victor Wegelin

214

8.64

Viscometers – Industrial

Jamison

Martin Apschner

215

7.23 

Weather Stations

Lipták

 

 

216

7.24 

Weight – Design and Application

Lipták

 

 

217

7.25 

Weight – Load Cells

Lipták

Paul Katende

 

218

8.66

Wet Chemistry and Autotitrator

Baughman

 

 

 

FTIR (Fourier Transform Infrared Spectrometer)

 

ANALYZERS     10

(41-18 unassigned)

New Ch. No.

Old Ch. No.

Title

4th Edition Author(s)

5th Edition Author(s)

Assigned

219

8.1 

Analyzer Application and Selection

Ullman

ROMEL S BHULLAR

220

8.2 

Analyzers, Process Sampling

Lipták

Ian Verhappen

221

-

Air – Automatic Remote Monitoring

-

 

 

222

-

Air – Particulates

-

 

 

223

8.5 

Air – Quality Monitoring, Sampling

Lipták

 

 

224

-

Ammonia

-

David Gallego

224a

8.6

Biometers

Lipták

 

 

225

8.9 

Carbon Dioxide

Lipták

 

 

225a

-

Carbon Dioxide in Liquidsz

-

Martin Apschner

225a

8.10

Carbon Monoxide

Lipták

 

 

226

8.11

Chlorine

Lipták

 

 

227

8.12

Chromatographs – Gas

Annino

ROMEL S BHULLAR

228

8.13

Chromatographs – Liquid

 

Lipták

ROMEL S BHULLAR

228a

-

Cyanide Analysers – Weak-Acid Dissociable (WAD)

-

SREENEVASAN

229

8.4 

Electrochemical Analyzers

Lipták

Sury Vedula

230

8.22

Element Monitors

Lipták

 

 

231

8.24

Fluoride Analyzers

Lipták

 

 

232

8.25

Hydrocarbon Analyzers

Verhappen and Martin

Ian Verhappen

232a

-

Hydrogen Cyanide (HCN) Monitors

-

SREENEVASAN

233

 

Hydrogen in Steam or Air

 

 

 

234

8.26

Hydrogen Sulfide

Lipták

Phil Harris

235

8.30

Mercury in Ambient Air

Saltsman

PHIL HARRIS

236

8.31

Mercury in Water

Lipták

 

 

236a

-

Metal Particle Detection in Lubricant Oil

-

Simon Wilson

237

 

Methane in Air and Water

 

 

 

238

8.32

Moisture in Air: Humidity and Dew Point

Lipták

Victor Wegelin

239

8.33

Moisture in Gases and Liquids

Tatera

Sury Vendula

300

8.34

 

Moisture in Solids

Lipták

 

 

301

8.36

Nitrate and Total Nitrogen

Lee-Alvarez

 

 

302

8.37

Nitrogen Oxide Analyzers

Lipták

Phil Harris

302a

8.39

Oil in or On Water

Verhappen

Ian Verhappen

303

-

Oil Sand Composition

-

Ian Verhappen

304

8.42 

Oxygen in Gases

Tatera

David S. Nyce

305

8.43 

Oxygen in Liquids (Dissolved Oxygen)

Dztewatkoski

 

 

306

8.44 

Ozone in Gases

Bollyky

L.J. Bollyky

307

8.45 

Ozone in Water

Bollyky

L.J. Bollyky

308

8.49 

Phosphorus Analyzer

Lipták

 

 

309

8.55

Sulfur-in-Oil Analyzers

Lipták

 

 

310

8.56

Sulfur Oxide Analyzers

Lipták

Phil Harris

311

8.54

Streaming Current or Particle Charge Analyzer

Lipták

Alcala Francisco????

 

315

8.65

Water – Quality Monitoring

Lipták

Emmanuel Ujiro

     

 

UNIQUE SENSORS FOR SPECIAL TASKS 11

          (In this Section, please describe ONLY those sensors which are unique to the particular industry or application and give only an overview of these specialized sensors)

(21-13 unassigned)

New Ch. No.

Old Ch. No.

Title

5th Edition Author(s)

Assigned

320

-

Agriculture

Mudhalwadkar

321

-

Automobiles

-

 

321a

-

Biomedical

-

 

322

-

Coal Power

-

 

323

-

Computer Chip Manufacturing

Béla Lipták

 

323a

-

Custody Transfer

-

 

324

-

Drilling for Oil or Gas 

Romel Bullhar

325

-

Fracking 

Béla Lipták

326

-

Home Automation 

-

 

327

-

HVAC

-

 

328

-

Hydrogen Industry

-

 

329

-

Medical Applications

Mehul Pancholi

 

330

-

Military Examples

-

 

331

-

Mining Safety

-

 

332

-

Oil – Deep Sea Drilling

Béla Lipták

Romel Bullhar

332a

 

Oil Platform Remote Data Monitoring

Guha

333

-

Oil Sand Processing

Ian Verhappen

334

-

Pipelining, Intelligent “Pigs”

-

 

335

-

Robotics

-

 

336

-

Transportation

Curt Wendt

336a

-

Unmanned aerial vehicle (UAV)

-

 

 

 

 

TRANSMITTERS      12

(9 – 3 unassigned)

(

New Ch. No.

Old Ch. No. In Volume 2

Title

4th Edition Author(s)

5th Edition Author(s)

Assigned

337

V2-3.5

Telemetering Systems

Eren

David L. Ubert

338

V2-3.6

Transmitters: Electronic

Nyce

 

 

339

V2-3.7

Transmitters: Fiber-Optic

Lipták

Dennis Horowitz

339a

-

Transmitter Installation for SIF Applications”. 

-

Seethepalli

340

 

Transmitters – Miniature

 

 

 

341

V2-3.8

Transmitters: Pneumatic

Lipták

Allen D. Houtz

342

V2-3.9

Transmitters: Self-Checking

Berge

 

 

343

V2-3.10

Transmitters: Smart, Multivariable

Berge

Bhagyashree (Shree) Pataskar

344

-

Transmitters – Wireless

-

Dick Caro

 

 

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Scraping of the Bottom of the Barrel — Fracking

Scraping of the Bottom of the Barrel — Fracking

Proponents Believe Fracking Gas Could Meet U.S. Energy Needs for a Century. Opponents Say the NG Supply Will Be Exhausted in Just a Few Decades

12/30/2011

Bela Liptak
About the Author

Béla Lipták, PE, is the editor of the Instrument Engineers’ Handbook.

By Béla Lipták, PE, Columnist 

In the United States, natural gas (NG) is the source of about 25% of the total energy consumption, and shale gas is the source of about 20% of the NG consumed. During the next years, hydraulic fracturing, or “fracking,” to produce NG will continue to rise, and will increase from today’s 20% to about 45% of American consumption by 2035. To date, just in Pennsylvania, there are some 4000 fracking wells in operation, and their number nationwide is projected to approach 100,000 within a few decades. The size of American recoverable shale gas deposits is debated. Until 2011, industry estimated the Marcellus Reserves (from Virginia to New York state) to be over 400 trillion cubic feet (tcf), while this year the U.S. Geological Survey reduced that estimate to 84 tcf.

The Process

Many of the natural gas wells in the United States use fracking to produce gas at economic rates. Large trucks, blenders, tanks and multistage pumps are used to inject millions of gallons of water at pressures of up to 20,000 psig into these wells that can be drilled to the depths up to 20,000 feet. Hydraulic fracturing can be performed in vertical or horizontal wells. In horizontal drilling, the terminal drill-hole is completed as a “lateral” that extends 1500 to 5000 feet parallel with the shale layer, while vertical wells extend only 50 ft to 300 ft into it. Horizontal drilling also reduces surface disruptions, as fewer wells are required.

After drilling the well, high-pressure liquids are injected into the shale rock or coal beds (Figure 1). When the “down-hole” pressure exceeds the fracture strength of the rock, it cracks, and the fracture fluid (FF) travels farther into the rock, extending the crack.

 

How fracking works

Figure 1. As the fracking fluids (FF) cracks the stone, the natural gas (NG) escapes through the fractures and travels up the well.

 

After cracks are formed, they have to be kept open. Proppants are solid particulates, such as grains of silica sand, resin-coated sand or harder materials such as ceramics. They serve to prevent the reclosing of the fractures when the injection phase is completed.

In the FF, sometimes, naturally radioactive minerals are also used in order to help to measure the depth of the fractures along the wellbore. Ninety-nine percent of the FF is usually water, while the rest consists of chemical additives used to protect the well and improve its operation. Initially, the injected FF is acidic to increase permeability. This phase is followed by injecting FF-containing proppants with gradually increased size solids, and the operation is completed by flushing the well with water.

When the fracking phase is over, most of the FF and drill cuttings are processed for reuse, trucked away, treated on-site before being released into the environment or stored on-site either in large tanks or in “frack ponds” that are several acres in size. Since these ponds are on the surface, and their wastewater can contaminate ground waters, wells and rivers, these ponds are sealed with plastic lining. Usually 30% to 40% of the FF can not be removed from the underground fractures and stays down in the shale, creating small and often toxic lakes.

During the removal of the FF, large amounts of NG, including methane, escape from the well or dissolve in the FF and enter the frack pond. After the removal of as much FF as possible, the actual production starts, and the drilling equipment is moved to drill another well. 

Arguments Pro and Con

Some representatives of the gas industry and some politicians believe that the amount of recoverable fracking gas could meet the American energy needs for a century or more, while opponents argue that the NG that is recoverable will be exhausted in a few decades. Proponents argue that fracking creates jobs and reduces energy imports, while opponents argue that these jobs are temporary, and more permanent jobs could be created if the same investment was made in renewable energy. Industry representatives also argue that NG is inexpensive, while opponents say that the cost would be much higher if the value of the water used, reduced real estate values, increased mortgage costs, expenses associated with health effects, the cost of wastewater treatment and legal expenses were included.

The gas industry advertises NG as the cleanest fossil fuel. Opponents claim that during the lifetime of a well, 3% to 8% of the produced methane is leaked into the atmosphere and, because methane is such a potent greenhouse gas, the greenhouse-gas footprint of NG is worse than that of coal or oil. The tradeoff is that, while the burning of NG releases fewer allergy- and cancer-causing solids and other pollutants than coal, the released methane contributes several times more greenhouse gases.

Proponents argue that the forces generated by fracking are insufficient to cause earthquakes, even when applied to unstable geological formations. Opponents point to the tremors and small earthquakes that have already been caused and to the potential damage to buildings. Last year, nine quakes occurred, unclamping ancient faults (geophones) near the Mahoning River in Ohio and others were reported in Arkansas and Colorado.

Proponents also argue that the drilling of wells should not affect the real estate values and should not invalidate mortgages. Opponents argue that this is a new industry, and its costs of operation will change if, in the future, businesses are required to compensate the landowners for water contamination or damage to livestock and crops. They also point to cases such as the Ohio bank warning the state’s lawmakers in September 2011 that if the borrowers do not obtain the consent of the bank before signing drilling leases, they will be violating the terms of their mortgage.

Environmental and Health Concerns

In 2005, Congress passed legislation prohibiting the federal government from regulating fracking under the Safe Drinking Water Act. This federal legislation is still in effect; therefore, companies do not have to disclose what chemicals they are putting into the ground, although some states, such as Wyoming, do require it. It is generally not known which company is using what chemicals, but in general the following are used: heavy metals, salts (bromides, chlorides), acetone, radionuclides (strontium, barium), arsenic and volatile substances (methane, benzene, alcohol, toluene, phenol, ethylene glycol).  These substances can enter the ground waters from leaking plastic transfer piping or due to damage to plastic liners of the frack ponds.

The industry claims that fracking and water contamination has never been definitely linked. Yet, in a 2011 report,  MIT scientists found that “there is evidence of natural gas migration into freshwater zones in some areas, most likely as a result of substandard well completion practices by a few operators. Also, there are additional environmental challenges, particularly the effective disposal of fracture fluids.

According to the industry, the harmful effects of fracking are no worse than those of conventional drilling. Opponents point to environmental effects, including the contamination of water supplies, air pollution, migration of gases and fracturing chemicals to the surface or the potential mishandling of toxic waste. They point to cases in Pennsylvania, where farmhouses and homes were abandoned because of animals dying, people getting blisters, dizziness, nosebleeds, etc. from the toxic and carcinogenic chemicals (New York Times Magazine, Jan. 20, 2011) and the class action lawsuits by landowners in Pennsylvania, Oklahoma, Texas, Wyoming and Virginia (New York Times Dec. 2 and Dec. 9, 2011).  

 
The National Academy of Sciences determined in 2011 that groundwater contains much higher concentrations of methane near fracking wells, causing potential explosion hazards. In Dimock, Penn., 13 water wells were contaminated with methane, and Cabot Oil & Gas had to compensate residents financially and construct a pipeline to bring in clean water to the town. Elsewhere the landowners had to install water purifiers or drink bottled water. In Pennsylvania, the fracking fluid at 116 of 179 deep gas wells contained materials with high levels of radiation, and in March 2010, Congress directed the EPA  to examine claims of water pollution related to hydraulic fracturing.
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Preventing Nuclear Accidents by Automation

Preventing Nuclear Accidents by Automation

 

To date there were only two „level 7” nuclear power plant accidents, one at Chernobil and the other at Fukushima (even Three Mile Island was only level 5). Prior to the accident, m54 nuclear power plants generated 30% of Japan’s electricity. In the íuSA 104 plants generate 18% of America’s electricity.

 

At Fukushima the cooling water pumps stopped at around 4 PM on March 11, 2011. At that time the cooling water level in the No. 1 reactor was 4 meters above the top of the fuel rods. By 9 PM it dropped 8 meters, fully uncovering the fuel rods. During that same time period the core temperature increased from about 300 ˚C to nearly 3,000 ˚C and by the morning of March 12 the reactor core melted, dropped to the bottom of the reactor’s containment vessel and probably burned a hole through its wall. The window of opporunity to prevent meltdown lasted for 5 hours, a time period, which would have been sufficient to prevent it. (Figure 1).

 

 

Figure 1: The sequence of events at Fukushima (Tokyo Power Co. May 15, 2011)

 

Reactors #1 and #2 at Fukushima were 40 years old GE units. Several American BWR nuclear power plants are of similar age or older and their designs are similar to the Fukushima ones. They are accidents waiting to happen. On the other hand, if their outdated sensors are replaced and their safety systems are automated, this need not happen, but if they are kept under manual control, if accident response remains to be a function of the judgment of hesitant or panicked operators, The Fukushima events will be repeated.

 

In this article I will concentrate on the automatic safety controls and will not discuss the details of design errors, such as the false assumptions that (1) simultaneous grid and backup failure could not occur, (2) that an 8 hour battery backup is sufficient (to my knowledge, of the 104 American reactors, 93 are provided with only four hours of battery backup), (3) that elevated water storage, providing cooling by gravity flow is not required, (4) that nitrogen purging capability of the primary containment is not required, (5) that power supply backup equipment need not be located at elevations that are safe from flooding, (6) that fresh water ponds are not required if sea water is available or (7) that it is not necessary to have installed piping, which makes it easy to pump cooling water from the outside, directly into the reactors by fire trucks.

 

In addition to the above design errors, at the Fukushima plant some 10,000 spent fuel rods were kept in the temporary storage pools, (ten times the original design), requiring continuous cooling to protect against their meltdown. Similar conditions exist today at many American plants.

 

In this article I will show that in spite of the above design errors, melt-down could have been prevented, if the plant was provided with properly automated safety controls. I will both point to the specific control system errors and to the unsafe nature of depending on manual operator response to unsafe conditions. In case of Fukushima these included: (1) the delayed start of injecting fresh water (March 12 at 5:50 AM) and later sea water (March 12 at 8 PM), when the cooling water pumps stopped some 14 hours earlier at around 4 PM on March 11. This delay, caused by the hesitation of the operators, would not have occurred under automatic control. (2) The 4 weeks delay (March 11 to April 7) of starting the nitrogen purging of the primary containment vessel,. Similarly, (3) the delay in relieving the excessive hydrogen and steam pressure outside the building, after filtering out radioactive solids (Figure 5). In case ofFukushima, relief was initiated manually and only after a delay of 7 hours.

 

Naturally, it is essential that the operators trust the various sensors and alarms. Therefore, they must be redundant and reliable. This was not the case at Fukushima. In the reactor, water levels were not reliably measured, but were only assumed by the operators. The false readings suggested that the levels were several meters above the actual and in the primary containment vessels they were not even measured. In a properly designed plant, detectors that are monitoring critical variables should have not only been accurate, but should have been triple redundant, configured in a voting arrangement, so that if one sensor disagrees with the “majority”, it’s reading is immediately disregarded and it’s recalibration is automatically requested.

 

Unreliable Cooling Water Level Measurement

Operators must know if the fuel rods are covered with water or not and safe plant operation requires automatic response if this level drops too low. This requires reliable level measurement! Today we know that atFukushimathe operators assumed the level to be much higher than they really were. It was only two months later (in May), when the water level gauge for the Reactor was calibrated and it was found that the actual level was much below the actual.

 

Similarly, the operators did not know the steam/water ratios, nor the degrees of meltdown in their reactors (nor in their spent fuel rod storage ponds). This resulted in the operators’ guessing at the level of cooling water, and because they guessed wrong, they drastically delayed the start of emergency cooling. If reliable sensors were used and water injection was started automatically, the meltdown would have been prevented. In this article I will describe the sensors that American plants should install in order to provide reliable information during both normal and emergency operation of BWR plants.

The BWR reactors are designed so that the core is surrounded by a shroud. The cooling water enters into this “jacket-like” space between the shroud and the wall of the reactor (Figure 2) and water travels down on the outside of the core and then rises up inside it. As it rises, the fuel rods heat the water until it starts to boil. As steam bubbles form, the water “swells” (its steam-to-water ratio rises).

The goal of the level control system is to keep the fuel rods always covered in order to protect against their overheating and melting. In many BRW reactors, the water level and the steam/water ratios (STR) are measured only “ex-core”, between the shroud and the reactor wall (Figure 2). Under emergency conditions (when the “ex-core” level drops below the suction of the jet disperser, because the cooling water pumps stopped) this measurement no longer reflects the water level inside the core, because there no longer is a reliable relationship between the in and ex core levels. Consequently, the out-core level measurement can be useless during emergencies caused by loss of cooling.

 

Figure 2: Unreliable cooling water level measurement used in many existing BRW reactors

 

In most nuclear power plants (Figure 2), the level outside the shroud is measured over two ranges, a narrow (LT-N) one and a wide (LT-W) one. The narrow span transmitter (LT-N) is more sensitive and is a better indicator of the level of the boiling water surface while the wide range transmitter (LT-W) detects the total hydrostatic head in the reactor (the collapsed level). Almost without exception, they both are of the d/p type hydrostatic designs, installed with condensate pots, which provide water filled reference legs (“wet legs”) to the high pressure sides of the d/p cells. In order to cool and condense the steam, the condensate pots are usually un-insulated, and the condensate drains back into the reactor through a sloping connecting pipe from the side of the pot.

 

The level transmitters shown in Figure 2 are inverse-acting (the reference leg is connected to their high-pressure side), and therefore, a maximum level produces a zero-differential reading, while a zero level causes a maximum output signal. The measurement also depends on the assumtion that the wet leg is full with condensate at ambient temperature. During an accident, neither of these assumptions are necessarily correct. In fact, they are likely to be wrong, because once the level in the reactor drops below the low-pressure tap of LT-N, it’s pressure difference reading drops to zero and therefore the level is no longer known.

Also, because the water in the reactor is boiling, these d/p cells detect the hydrostatic head (mass of water) and not the level of the boiling surface. Swelling occurs when the steam pressure drops (the steaming rate increases), and shrinking occurs when the steaming rate is reduced (the steam pressure rises), and bubbles collapse. The more bubbles form (swelling), the higher is the boiling level, but lower is the density and therefore the indication of the level (the hydrostatic head). Inversely, as the steaming rate drops (shrink phase), the density increases, level drops, while the level measurement increases. In other words, when the surface of the boiling water rises (swell condition) the level reading drops, and when the boiling rate is reduced and therefore the level drops, the measurement rises.

Therefore, the d/p cell outputs can indicate the surface level only if the measurement is corrected for density, which was not the case atFukushima and in not the case in many American plants. AtFukushima and at many American plants, this correction was/is inaccurate or nonexistent. Therefore, these level measurements are unreliable or useless. Because of this, the level control loop cannot be closed (cannot be controlled automatically) and therefore are often left under manual control, which is unacceptable. The correction and the properly designed automatic control loop is shown on the right of Figure 4.

In case of Fukushima (and in case of a few old American plants), the design is even worst, because no transmitters are used at all, only d/p indicators and even those are located far away, usually in the control room (Figure 3). What makes this design even worst is that the level gauge (LI) is connected to the reactor by long lead lines which represent the high pressure reference and is supposed to be filled with cold condensate from the condensate pot. This bad design which is no longer in use, because the condensate from these long lead lines can be lost due to leaking, the line can be plugged, be blocked by air or the water can oscillate in them, but 40 years ago they were still in use in some less sophisticated plants. InFukushima, the condensate pot temperature probably reached the boiling point, the condensate in it evaporated and once this lead line was no longer full, the d/p indicator drastically (by several meters) “over-reported” the water level in the reactor. Therefore, the operators assumed that they had more water than they really did and this explains why they did not start water injection for some 14 hours, by which time this window of opportunity to prevent meltdown was gone.

 

 

Figure 3: The level at Fukushima was measured by remote gauges, instead of transmitters

 

 

Correctly Detecting the Water Level in the reactor

 

If theFukushimaoperators knew the correct level, they could have started water injection as soon as the pumps stopped, while the fuel rods were still covered and the meltdown could have been prevented.

Accurate level measurement outside the core (ex-core”) indicates the “in-core” level only until the level drops to the suction of the jet pump diffuser. Therefore, under emergency conditions direct “in-core” measurement is also needed. In Figure 4, the red arrows show the flow direction of the steam and the blue arrows that of the water. The readings of the pressure transmitters P1, P2, etc. to PX can be used to measure the “ex-core” level and steam/water ratio.. These pressure sensors should be installed at an equal vertical distance (A) from each other. The smaller the distance “A”, the higher will be the precision of the measurement. If in Figure 4 the difference between two readings is zero (P2-P1 = 0), indicates that only steam is present at that elevation. If the ΔP is above zero (P3-P2 > 0), that is an indication that some water is also present at that elevation.

 

Figure 4: Sensors required to correctly measure the “ex-core” water levels

 

By this method, the boiling surface (Ls) can be estimated as being between the first detectors where the ΔP is above zero. Under normal operation, the resulting Ls reading will be about the same as the one detected by LT-N in Figure 2 or LI in Figure 3. In addition, the various combinations of these pressures and differential pressure measurements (knowing the steam pressure (Ps) and the specific gravity (SG) of water at the operating temperature), can be used to obtain the following information:

  • Steam/water ratio (S/W) at any elevation is S/W =  ΔP/(A.SG).
  • Collapsed total water level in the reactor is                                                           Lc  =  (PX – P1)/(distance between top and bottom sensors)SG.
  • Steam/water ratio of the boiling column of water in the reactor                            S/Ws = (PX – Ps)/Ls(SG).

The “ex-core” sensor will reflect the “in-core” levels as long as the fuel rods are covered with water. Under emergency conditions, this is not the case, yet the accurate measurement of the in-core level is still needed. AtFukushima(and in many American BWR reactors), the level inside the core was not measured at all. This resulted in the uncertainty concerning the degree of meltdown and the start of hydrogen generation.

 

As to the method of detecting the in-core water level, one method would be to measure the temperature (or thermal conductivity) at the different elevations in the core (green probes shown in Figure 4). These measurements reflect the steam/water ratio at different elevations, because the thermal conductivity of water is higher than that of steam.

One method of doing this was designed by David Nyce for the Knolls Atomic Power Plant. He used a metal probe with ceramic insulation and a reference thermocouple at its tip and located heated thermocouples periodically along the probe length. Because the thermal conductivity of water is much higher than that of steam, the amount of cooling of the heated thermocouples dropped (relative to the reference) as their elevation increased, because the steam/water ratio increased with elevation. Above the surface of the boiling water, the amount of cooling reached a minimum because the heated thermocouple at that elevation was surrounded only by steam. This way, by measuring the temperature elevation of the submerged thermocouples at the different elevations (relative to the reference temperature), both the level and the steam/water ratio at the different elevations in the core can be measured.

 

Yet another method to consider for the detection of „in-core” level is to correlate gamma radiationdistribution inside and outside the reactor pressure vessel withthe water level. The vertical gamma radiation distribution is related to water level, but because it is also a function ofthe neutron flux and the coolant recirculation pump speed, special algorithms are needed to interpret the level based on these radiation measurements.

To obtain fully reliable measurements, it is also desirable to provide battery backup and wireless output for all the transmitters, so that if either the regular power supply fails, or the regular output signal wires are damaged, the level information will still be available and can be read not only in the control room, but also outside the building.

Preventing Hydrogen Explosions

 

Once the „window of opportunity” to keep the fuel rods covered was missed (Figure 1) and the melting of the fuel rods started, the safety goal should have been to prevent the explosion of the hydrogen generated. During an emergency shut down, if cooling is lost, the fuel rod temperatures will rise, the zirconium cladding (the material that covers the fuel rod) melts (at around 1200 °C) and reacts with the water in the reactor, generating hydrogen:

 Zr + 2H2O = ZrO2 + 2H2

If the generated hydrogen comes in contact with an ignition source (such as a melting fuel rod or any other) and if oxygen is present, it can explode. This is what occurred in theFukushimaplant. The hydrogen accumulated in the primary and later in the secondary containments and because they contained air (not inert gas), it exploded (Figure 5).

 

Figure 5: At Fukushima, as the pressure increased, the radioactive steam containing hydrogen, was relieved by the PSV into the wet well, but due to loss of cooling, the steam did not condense. Therefore the pressure built up until (7 hours later) the operators finally relieved it by manually opening the vent valve (SS). The hydrogen accumulated inside the building, mixed with oxygen in the air and exploded.

As an explosion requires a fuel, ignition source and oxygen, relieving the hydrogen inside the building made the explosion unavoidable. Yet, a properly designed automatic safety control system would have prevented the explosion, because:

As soon as hydrogen was detected in the torus, the backup cooling system would have been automatically actuated and if pressure continued to rise a pressure relief system (Figure 6) would have automatically opened to relieve the steam-hydrogen mixture outside the building (after it has been filtered to remove any radioactive solids). In addition, nitrogen purging of the primary containment would have started automatically and immediately. (Fukushima operators did not inert the primary containment until two months later in May, 2011)

 

Figure 6: A properly designed pressure relief system would have automatically relieved the steam and hydrogen to outside the building, where it would have quickly risen.

 

Because hydrogen was allowed to accumulate inside the building, its explosion destroyed the building and radioactive particles were discharged with it, because it was not filtered as in Figure 6. Another important feature in the design in Figure 6 is that as soon as the excess pressure is released, the pressure safety valve recloses. In case of the Fukushima(or any other plant where the vent valve is manually opened), the operator can forget to reclose the valve and thereby unnecessarily release additional radioactive gases and solids. It is also important that full backup be provided for the automatic pressure relief system so that the burst rupture disk can be replaced while the backup relief valve protects the building. The main reason why the design in Figure 6 is safe is because it is automatic. Therefore, there is no operator’s judgment involved (there is no hesitation for seven hours) but whenever the pressure reaches about 75% of the design pressure, it relieves it automatically.

Conclusion

If automatic, state-of-the-art safety controls were used atFukushima, both the meltdown and the hydrogen explosions could have been prevented.

Béla Lipták, PE
President of Béla Lipták Associates, PC
Automation and Safwty Consultants
84 Old N. Stamford Rd, Stamford CT. 06905
T/F: 203-357-7614, E: liptakbela@aol.com
www.BelaLiptakPE.com

 

 

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Letter on St. Emery Church

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