IC67 - Pre-Instructional Survey

Similar documents
ACCURACY, PERFORMANCE, AND HANDLING OF OIL-FILLED DIGIQUARTZ PRESSURE INSTRUMENTATION

Pressure Reducing & Desuperheating (PRDS) Station Pressure Reducing (PRS) Station Desuperheating (DSH) Station. Ver. 1.1 (2016)

The Nitrogen Threat. The simple answer to a serious problem. 1. Why nitrogen is a risky threat to our reactors? 2. Current strategies to deal with it.

IAEA SAFETY STANDARDS for protecting people and the environment

COMPAFLOW. Compressed Air. Volumetric flow. Gas. Mass flow. Steam. Net volumetric flow. Liquid

IAEA SAFETY STANDARDS for protecting people and the environment

English. Introduction. Safety Instructions. All Products. Inspection and Maintenance Schedules. Parts Ordering. Specifications WARNING WARNING

RHPS Series RD(H)F40 User Manual. Read the complete manual before installing and using the regulator.

Model 1159 Remote Diaphragm Seals Manual

SINGLE VALVE WITH LOW-FLOW BYPASS

Design DSA Steam-Atomized Desuperheater

Standard Pneumatic Test Procedure Requirements for Piping Systems

How to specify a product. Process Sensors and Mechanical Instruments

Custom-Engineered Solutions for the Nuclear Power Industry from SOR

CVI Valve Line. Exceeds the industry s highest standards for reliability and performance

N2 Blanketing Valve DST100 / DST200 TYPE INSTRUCTION MANUAL CONTENTS K.S.P.C. General Description Operation. Installation Maintenance

PROCEDURES FOR REPAIRS TO ASME NV STAMPED PRESSURE RELIEF DEVICES OF NUCLEAR SAFETY RELATED PRESSURE RELIEF VALVES

Level transmitters and indicators Series LU Ultrasonic level transmitter and indicator for liquids and solids

OPERATING AND MAINTENANCE MANUAL

Per Section I of the ASME

SV60 Safety valves. for use with steam, gas and liquids

Ultrasonic level transmitter and indicator

Level MEASUREMENT 1/2016

ASME and PED Requirements for Drum Level Instrumentation. Presented by: Amir Hedayatnia Clark-Reliance Corp.

Rosemount 3159 Nuclear Qualified Remote Diaphragm Seal

HYDROSTATIC LEAK TEST PROCEDURE

Slug Catchers Engineered Solutions to Separation Problems

REVISIONS. App Thom. App Sud. App PC IG 2014/09/19

HTR Systems and Components

Fisher DVI Desuperheater Venturi Inline

Installation and Operation Manual

Safety Classification of Structures, Systems and Components in Nuclear Power Plants

Pressure and/or Temperature Pilot Operated Steam Regulators Series 2000

MDEP Common Position No AP

RULES OF THE OIL AND GAS PROGRAM DIVISION OF WATER RESOURCES CHAPTER DRILLING WELLS TABLE OF CONTENTS

FUNDAMENTAL SAFETY OVERVIEW VOLUME 2: DESIGN AND SAFETY CHAPTER F: CONTAINMENT AND SAFEGUARD SYSTEMS 7. CONTAINMENT HEAT REMOVAL SYSTEM (EVU [CHRS])

Type ACE97. Introduction. Installation. P.E.D. Categories. Specifications. Overpressure Protection. Installation Guide English May 2002

Mounting and operating instructions EB 2530 EN. Self-operated Pressure Regulator. Pressure Reducing Valve Type M 44-2

DESIGN OF REACTOR CONTAINMENT STRUCTURE AND SYSTEMS FOR NUCLEAR POWER PLANTS

Pressure measurement Applying remote seal, isolation diaphragms between process fluids and transmitters

Buying more than 11 gauges? Call Lesman for additional discounts.

SERIES 500 VARIABLE RANGE PNEUMATIC DIFFERENTIAL PRESSURE TRANSMITTER

V46 Series 2-Way Pressure-Actuated Water-Regulating Valves With Union Fittings

Stormy Phillips BASICS OF LEASE AUTOMATIC CUSTODY TRANSFER (LACT) SYSTEMS

L3 Pressure and Level transmitter

Beyond Switches for Pump Monitoring:

Improving distillation tower operation

FUNDAMENTAL SAFETY OVERVIEW VOLUME 2: DESIGN AND SAFETY CHAPTER I: AUXILIARY SYSTEMS. A high-capacity EBA system [CSVS] [main purge]

Fisher DSA Steam-Atomized Desuperheater

DESIGN OF REACTOR CONTAINMENT STRUCTURE AND SYSTEMS FOR NUCLEAR POWER PLANTS

Botlek Studiegroep Badotherm. Solving measurements issues with Diaphragm seals 3 Case Studies

Design of Relief Valves/Devices/Systems for Cryogenic Apparatuses and Installations

Mounting and Operating Instructions EB 3007 EN. Self-operated Pressure Regulators. Differential Pressure Regulators (opening) Type Type 42-25

ASVAD THE SIMPLE ANSWER TO A SERIOUS PROBLEM. Automatic Safety Valve for Accumulator Depressurization. (p.p.)

innova-ve entrepreneurial global 1

L 100. Bubble-Tube Level System. Installation, Operation and Maintenance Instructions

Smooth Vent Valve. Series XVD XL XL Q D- XVD XGT CYV

Torque Tube TB300 Digital Transmitters

Installation, operating and maintenance Instructions for Seemag bypass level indicator

Standard: NFPA 86 Process Ovens and Furnaces. NFPA 85 Boiler and Combustion Systems Hazards Code

DeZURIK. KSV Knife Gate Valve. Safety Manual

TA10A and TA10P Steam Tracing Temperature Control Valves Installation and Maintenance Instructions

V48 Series 3-Way Pressure-Actuated Water-Regulating Valves With Union Fittings

Review and Assessment of Engineering Factors

Liquid Level Measurement

Engineered solutions for complex pressure situations

PROCESS MONITORING AND CONTROL

Rosemount 1195 Integral Orifice Primary Element

Mounting and Operating Instructions EB 3017 EN. Self-operated Regulators

BUTTERFLY VALVES Series 800

EASTERN ENERGY SERVICES PTE LTD. 60 Kaki Bukit Place #02-19 Eunos Tech Park Singapore, SG Singapore Telephone: Fax:

PROCEDURE TWO-PLY TESTABLE BELLOWS D 1 OF 5 TWO PLY BELLOWS TEST PROCEDURE

Restriction Orifice. Single or Multi Stage Orifice to. Reduce Pressure or. Limit the Flow Rate

RD(H)20/25 Pressure-Reducing Regulator User Manual

Pro-V Multivariable Flowmeter Model M22 In-line Vortex

Smart Water Application Technologies (SWAT) TM

TRI LOK SAFETY MANUAL TRI LOK TRIPLE OFFSET BUTTERFLY VALVE. The High Performance Company

A review of best practices for Selection, Installation, Operation and Maintenance of Gas meters for Flare Applications used for Managing facility

Vortex Flow Meter Wafer or Flange Connection. - Steam - Liquid - Gas

INSTRUMENTATION EQUIPMENT

2600T Series Pressure Transmitter Models 264DC Differential and 264HC Gage Level Transmitters. Kent-Taylor

Solenoid Valves used in Safety Instrumented Systems

ACCURATE PRESSURE MEASUREMENT FOR STEAM TURBINE PERFORMANCE TESTING

Smooth Vent Valve XVD. Series

Mechanical Seal Piping Plans

For use with select HPC Fire Pits ONLY- refer to product catalog or website. 100K BTU Maximum WARNING: FOR OUTDOOR USE ONLY

Mechanical Seal Piping Plans

DESIGN DATA A WET PIPE BLADDER TANK FOAM/WATER SYSTEM WITH HYDRAULICALLY ACTUATED DELUGE CONCENTRATE CONTROL VALVE

TechTalk. Purging for Delayed Coking. Understanding purging system design in heavy-fouling applications. Outline

Un-Pressurized Orefice Fittings FIO EZ. Parts List and Operation Instructions TECHNICAL MANUAL. Dn 2-6 Class Lbs

Every things under control High-Integrity Pressure Protection System (HIPPS)

HCMTCB MATERIALS SAMPLING & TESTING PERFORMANCE CHECKLIST

PX3005. Rangeable Industrial Pressure Transmitter M-5721/1018

Kube Engineering Quinn E. Eddins, B.S.E.E Phone

Requirements for the Ethylene MACT

Efficient Pigging of Gathering Lines. Energy Management Workshop for Upstream and Midstream Operations

3.0 Pressure Transmitter Selection

DeZURIK Double Block & Bleed (DBB) Knife Gate Valve Safety Manual

Genie Supreme TM Model 123HP Installation & Operation Instructions

Flange Bolt Torquing. for Resistoflex Plastic-Lined Piping Products. Torquing. Retorquing. Hydrotesting. Annual retorquing

Transcription:

IC67 - Pre-Instructional Survey 1. What does the term code refer to in the installation of power plant piping? a. National welders code b. Fire protection code c. ASME Boiler and Pressure Vessel Code Section III 2. Nuclear Safety-Related systems are essential to? a. Protect plant personnel from injury b. Prevention or mitigation of significant release of radioactive material to the environment c. Productive supply of electrical power 3. What does the term pressure boundary integrity mean? a. The capability to retain the process fluid b. Maintains system pressure during operation c. Controls process pressure within specific limits 4. In the context of this standard what does qualified mean? a. Able to install transducers for the plant staff b. Demonstrated to be acceptable for the design requirements c. Successful class completion 5. Where the only code function for a device is mounting, what evaluations are necessary? a. Instrument and supports will not fall and damage other equipment b. Tubing and supports will not fall and damage other equipment 6. How are seismically qualified transducers mounted? a. In the same configuration as the qualified configuration b. Best orientation for plant location c. Around other seismically qualified transducers 7. Impingement barriers are used for: a. Preventing postulated missiles from striking instruments b. Stopping leakage c. All the above 1

8. Unless otherwise justified, auxiliary equipment shall be mounted. a. Follow the requirements of off-line transducers b. Independent of other mounts 9. Transducers shall not be installed in locations with environments that may exceed the qualified capabilities of the transducer, except. a. There is no other device b. The transmitter will probably survive to environment c. The potential adverse environment will only exist after the transmitter function is no longer required. 10. What ambient operating conditions, as a minimum must be considered? a. Temperature, pressure sun angle, radiation b. Radiation, humidity, pressure, temperature c. Radiation, electromagnetic effect, temperature 11 What pipe or tubing sizes are covered by the standard? a. 2.54 cm or less outside diameter and pipe 1.9 cm or less outside diameter b. All small pipe and tubing c. Piping smaller than 25.4 cm outside diameter 12. What is the difference between a sensing line and a sample line? 13. Primary Containment wall penetration is ASME Section III Class 2 Seismic Category 1, what is the classification of the sensing line past the containment isolation valve? a. ASME Section III Class 2 Seismic Category 1 b. ANSI B31.1 Seismic Category 1 c. No classification required 14. Why are capillary lines with diaphragm seals used? a. Long tubing runs through high temperature rooms b. Isolation of potentially highly contaminated fluids c. Easier than a tubing installation 2

15. For remote seals what is the largest effect on system performance? a. Pressure of the process b. Process fluid c. Temperature of the environment where the capillarity is routed. 16. What is an isokinetic sample? a. Sample where the kinetic energy of the particles are identical in the sample line as in the process line being sampled. b. Sample stream is representative of the process stream in particle size and composition 17. When should restriction orifices not be used? a. Where constituents of the fluid may be trapped b. Where flow would be restricted c. Where a tubing break could result in excess flow from the system 18. What is the proper tap location for pressure measurement on a gas system? a. Side b. Top c. Bottom 19. What does the term single failure proof mean in sensing line installation? a. No active or passive failure will prevent the safety function b. No passive failure will prevent the safety function c. No failure will cause the failure of more than one redundant sensing line unless the function will still be accomplished. 20. A detailed seismic analysis must be performed for each tubing installation. 21. Instrument line slope is necessary because: a. Smooth transition from process connection to instrument connection b. Prevents entrapment of liquid in gas lines c. Prevents the tubing being used as a ladder 3

22. Once the tubing is routed the installation is complete. 23. Loops in the tubing are used to make the drawing interesting. 24. It is best to use a single tap and tube installation for all redundant sensors. 25. Potential inaccuracies in water level indication during and after repid depressurization events have been identified as industry concerns and shall be considered in routing? 4

IC67 - Pre-Instructional Survey Answer Sheet 1. c 2. b 3. a 4. b 5. c 6. a 7. a 8. a 9. c 10. b 11. a 12. Sample lines have the expectation of flow. 13. b 14. b 15. c 16. c 17. a 18. b 19. c 20. b 21. b 22. b 23. b 24. b 25. a 1