4. Sampling and Measurement of Concentration

Slides:



Advertisements
Similar presentations
Corrosion Products Sampler (CPS)
Advertisements

Topical Aspects on Monitoring Airborne Radioactive Effluents from NPPs Wan-tae KIM.
Aero-Hydrodynamic Characteristics
3. The Motion of Particles Drag force d particle diameter V flow velocity Spherical particle, Re < 1 Drag coefficient A projected area.
Chapter 8 : Natural Convection
Free Convection: General Considerations and Results for Vertical and Horizontal Plates Chapter 9 Sections 9.1 through 9.6.2, 9.9.
5-9-B Cyclone Separators Cyclone separators are gas cleaning devices that  employ a centrifugal force generated by a spinning gas stream  to separate.
HIAPER Modular Inlets (HIMIL) & Instrument Exhaust System - Dave Rogers - Outline HIMIL description contamination testing re-install HIMIL to different.
Chapter 4.2: Flow Across a Tube Bundle Heat Exchanger (Tube Bank)
Local Exhaust Hoods. 2 Introduction:  Designed to capture and remove harmful emissions from various processes prior to their escape into the workplace.
Chromatography Dr.Tawfeq A. Al-Howiriny Associate Professor
Internal Flow: Heat Transfer Correlations
Cyclones & Electrostatic Precipitators
Fluid Friction. Outline Bernoulli ’ s Equation The Pressure-Drop Experiment Laminar Flow Turbulent Flow The Three Friction Factor Problems Computer Methods.
Fluid Mechanics 08.
CE Fluid Mechanics Diogo Bolster
Industrial Ventilation
A High Elevation Aerosol Inlet Modeling Study and Inter-comparison A. Gannet Hallar 1, Ian McCubbin 1, Igor Novosselov 2, Riley Gorder 2, John Ogren 3.
Choking Pressure Ratio Guidelines for Small Critical Flow Venturis
Unit: IV-Fluid Dynamic
Introduction to Fluid Mechanics
Sedimentation.
Wet Stack Fine Particulate Method/CEMS Development Measurement Technology Workshop January 29, 2013.
Particulate control techniques Gravity settling chamber Mechanical collectors Particulate wet scrubbers Electrostatic precipitators Fabric filters.
© Pritchard Introduction to Fluid Mechanics Chapter 8 Internal Incompressible Viscous Flow.
Formative Assessment. 1. Water flows at m/s down a pipe with an inner diameter of 1.27 cm. If the pipe widens to an inner diameter of 5.08 cm, what.
A proposal of ion and aerosol vertical gradient measurement (as an example of application of the heat transfer equations) H. Tammet Pühajärve 2008.
Heat Transfer Equations. Fouling Layers of dirt, particles, biological growth, etc. effect resistance to heat transfer We cannot predict fouling factors.
Viscosity Contents: How to calculate Whiteboards.
Collisional Processes In chemistry, the rate of 2-body reactions is based on the rate of collisions between the two species times the probability that.
Objectives Airflow in Ducts Fluid dynamic review Duct Design.
Internal Flow: Heat Transfer Correlations. Fully Developed Flow Laminar Flow in a Circular Tube: The local Nusselt number is a constant throughout the.
Prof. Jiakuan Yang Huazhong University of Science and Technology Air Pollution Control Engineering.
Enrico Da Riva (EN/CV/PJ)
Prof. Jiakuan Yang Huazhong University of Science and Technology Air Pollution Control Engineering.
Introduction to Fluid Mechanics
Mi9 Some experimental measurements of the Diffuser flow in a Ducted Wind Turbine assisted by two ejectors Kypros F. Milidonis Department of Mechanical.
Momentum Equation and its Applications
Major loss in Ducts, Tubes and Pipes
Heat Transfer Su Yongkang School of Mechanical Engineering # 1 HEAT TRANSFER CHAPTER 8 Internal flow.
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Internal Flow: Heat Transfer Correlations
Heat and Flow Technology I.
Viscosity Contents: How to calculate Whiteboards.
CURVES IN ENGINEERING.
and the like in the pipe or duct system.
Internal Incompressible
MAE 5380: AIR-BREATHING ENGINE INLETS
Erosion of rock by moving water
SME Associates LLC Providing Innovative Solutions
Topical Aspects on Monitoring Airborne Radioactive Effluents from NPPs
Presented by Harry C. Elinsky, Jr. Filtech, Inc.
Chapter 4 Airflow in the Respiratory System
Air pollution sampling and control
Field Testing ASHRAE Guideline
Session 4: Air Pollution Measurements
Air Volume Flow Rate and Centerline Velocity in a Tube Wind Tunnel
Filter Installation Leak Testing
Chapter 8 : Natural Convection
In-Situ Filter Testing
Clarkson UNIVERSITY defy convention
HW4 Problem (Use TITUS Square Ceiling MCD diffuser
Pneumatic nebulizer 4. Larger particles are smashed against the
Topical Aspects on Monitoring Airborne Radioactive Effluents from NPPs
Sedimentation Text book, Chapter 3 Reading Materials:
Sedimentation Text book, Chapter 3 Reading Materials:
Introduction to Fluid Mechanics
Particle Collection Mechanisms
Objectives Air Distribution Systems Duct design HW4.
Internal Flow: Heat Transfer Correlations Chapter 8 Sections 8.4 through 8.8.
Presentation transcript:

4. Sampling and Measurement of Concentration Isokinetic sampling - Velocity entering the sampling probe is equal to free stream velocity. - No particle loss at inlet. - Does not insure no particle loss elsewhere.

is the sampling flow rate is the flow rate of aerosol is the probe diameter is the duct diameter

Anisokinetic sampling Misalignment Superisokinetic Subisokinetic

Case 1: Miasalignment Maximum error is concentration in the probe is concentration in free stream

Effect of misalignment of the sampling probe

Case 2 & 3: Superisokinetic & subisokinetic Maximum error

Superisokinetic and subisokinetic sampling (q = 0)

Superisokinetic and subisokinetic sampling (q = 0)

Case 4: Velocity mismatch and misalignment Maximum error

Sampling from still air Two sources of error 1. Settling - sampling tube facing upward-> overestimation of concentration. - sampling tube facing downward-> underestimation of concentration. 2. Inertia - Same as superisokinetic case->loss of large particles.

Criteria to avoid settling error Davies’s criteria For standard condition in mm in m3/hr

Criteria to avoid inertia error Davies’s criteria For standard condition in mm in m3/hr

Davies’s criteria for upper and lower limits of probe diameter.

Maximum air velocity that still-air sampling criteria can be used Agarwal & Liu’s criteria: less restrictive with less than 10% error No restrictions for particle smaller than 100 micron.

Maximum ambient air velocity that still-air sampling criteria can be used

Transport losses: in tubing and fittings

1. Settling loss is the tube length is the inclination of the tube in radians

2. Inertia loss at the bend Laminar flow Turbulent flow is the bend angle

3. Other losses - Diffusion: Previous chapter - Interception: small - Electrostatic: will be discussed later - Thermophorsis: sample of hot aerosol stream in a cooler tubing. Will not be discussed.