1 Air Separators. 2 3 AIR IN THE SYSTEM WHAT DOES IT DO Annoying noises Gurgling and falling water Reduced pump head and failure Water/air mixture becomes.

Slides:



Advertisements
Similar presentations
HVAC523 Heat Sources.
Advertisements

Basic Refrigeration Cycle
©2008 Armstrong International, Inc. Basic Steam Trap Operation.
1 Expansion Tanks. 2 3 Expansion Tanks WHY USE THEM TYPES LOCATION SIZING.
Filling, purging and air removal
Drums, Vessels, & Storage Tanks Design Considerations.
Lesson 25 TWO-PHASE FLUID FLOW
Pumps, Compressors, Fans, Ejectors and Expanders
©2005 Armstrong International, Inc. Open and Closed Systems.
Principles of Liquid Flow through Pipelines
FOAM APPLICATION TECHNIQUES
What is going on inside a packed stuffing box?
Fuel Oil Systems Fuel Oil Systems consist of: Storage Tanks Pumps
STEAM HEATING.
Hydronic Mechanical Controls
©2005 Armstrong International, Inc. Proper Piping Practices (Pumps)
Assignment No. 1 [Grup 8] Figure below shows a portion of a hydraulic circuit. The pressure point B must be 200 psig when the volume flow rate is 60 gal/min.
Steam Traps Function and Types.
Natural Draft Cooling Towers
Mounting Direction Water Cooler Best solution OK Risk of air bubbles in the system Heatsink Water channels Inlet Outlet.
Water piping design.
HVAC523 Circulator Pumps.
1 Combustion Oil Fired Equipment. 2 OIL Combustion of oil fired equipment has the same basics of gas. Remember, Oil is a liquid and this must be converted.
Plan 2 – Dead-end Seal Chamber Optional Jacket
HVAC523 Basic Subsystems.
NFPA 31 Standard for the installation of Oil- Burning Equipment
College of Engineering & Petroleum Depatment of Chemical Engineering
Northvale Korting Fluid Jet Theory and Applications of Eductors By Patrick Belcher.
EVAPORATIVE EMISSION CONTROL SYSTEMS
David Garvin Product Manager EarthDirEX Geothermal Copyright © 2015 Nortek Inc. All rights reserved.
MECHANICAL ENGINEERING FOR SYSTEM BALANCE ASHRAE MEETING 2/15/2007 NORTHERN NEVADA CHAPTER 126 MATT BRENNAN, TBE.
Sizing Variable Flow Piping – An Opportunity for Reducing Energy
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.
Jim Hahn Kelly McCormick Jeff Snyder Andrew Taylor Nathan Wagers ME 414: Thermal/Fluid Systems.
Solar Heating/Cooling/Dehumidifier Systems
Introduction to Energy Management
Table of content 1- Heat exchanger design (cooler ) 2- Distillation column design. 3- Valve.
3.1.8 Student Book © 2004 Propane Education & Research CouncilPage Identifying Procedures for Conducting Container Vapor Flaring Operations Before.
Lecture Objectives: Answer question related to Project 1 Finish with thermal storage systems Learn about plumbing systems.
OILGEAR PVV PUMPS PVV 200 Performance Curves.
Production Engineering II
Flammable Liquids Directorate of Training and Education
Purgers and Non-condensables “What are they and why should I care?” Refrigerating Specialties Division Parker Hannifin Corporation July 2004.
Air Dryers The purpose of an air dryer is to remove water vapor from the air. The higher the pressure, the higher the dew point. Dew point is the temperature.
Chapter 5 Part 2 Mass and Energy Analysis of Control Volumes Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 8th edition.
EMERGING TECHNOLOGIES AVAILABLE TO REDUCE COMPRESSED AIR DEMAND Double Acting Air Cylinder Double Acting Air Cylinder Air Operated Diaphragm Pumps Air.
CHE441 Lecture: Tank & Vessel. Introduction of Vessel Applications of Vessels:  (1) as a liquid surge drum for liquid storage  (2) as a vapor/liquid.
ACTIVE SOLAR DESIGN ALTERNATIVE ENEGRY SOURCES.
Domestic Hot Water Recirculation Design
First Law of Thermodynamics applied to Flow processes
Chapter 37: Fluid Containment
Components Pumps.
Unit 37: Fluid containment Dr
R1 Fundamentals of Refrigeration
Natural Gas Processing I Chapter 2 In-feed System
Thermodynamics Units and Properties.
EVAPORATIVE EMISSION CONTROL SYSTEMS
Unit 37: Fluid containment Dr
Effect of gravity on coalescence
R1 Fundamentals of Refrigeration
Tracer Applications.
Heatless Desiccant Dryers
Chapter 6 Cyclones.
Pneumatic System Conditioning
Presentation transcript:

1 Air Separators

2

3 AIR IN THE SYSTEM WHAT DOES IT DO Annoying noises Gurgling and falling water Reduced pump head and failure Water/air mixture becomes compressible Catastrophic pump failure Disturbed water flow Foam in the piping/loss of conductivity Corrosion

4 Air Management

5 50 o 100 o 150 o 200 o 250 o 300 o 5% 20% 15% 10% 25% 5 PSI 10 PSI 150 PSI 25 PSI 0 PSI 50 PSI 75 PSI 100 PSI 125 PSI Nitrogen Soluble in Water Expressed in % of Water 0 PSI & 32 o F Temperature o F

6 Air Management Velocity

7 Example: Full Flow

8 Example: Half Flow

9 Air Elimination

10 Pipe Sizing Velocities high enough to carry air to the point of separation. –Above 2 ft/sec will carry air bubbles with liquid stream –Below 0.5 ft/sec will allow bubbles to rise by buoyancy in spite of the downward flow Need effective air control. –Maximum velocity limits assume that air is not present.

11 Air < 0.5 fps > 2 fps Water Water velocities greater than 2 feet per second will move entrained air downward. Air will rise in downward water flows at velocities of 6 inches per second or less. (Gil Carlson The design influence of air on hydronic systems. ASHRAE TRANSACTIONS 87(1): )

12 Air Separation Initial fill, remove gross air by: –Venting –Purging

13 System purging City Water Drain Hose to drain Open Closed

14 Air Separation Operation, remove entrained air using: –High temperature –Low pressure –Low velocity –Centrifugal action –Coalescence

15 AIR SEPARATION EFFECT of PRESSURE and TEMPERATURE Lowest pressure /highest temperature: this is the Point of lowest solubility Example at 40 psig (ie: right out of faucet) At 60 degrees F = 8% air by volume Now heat the water up...

16 AIR SEPARATION EFFECT of PRESSURE and TEMPERATURE Lowest pressure /highest temperature: this is the Point of lowest solubility Example at 40 psig At 60 degrees F = 8% air by volume RESULT: At 195 degrees F = 4% air by volume....where did the air go?

17 AIR SEPARATION EFFECT of PRESSURE and TEMPERATURE Lowest pressure /highest temperature: this is the Point of lowest solubility Example at 40 psig At 60 degrees F = 8% air by volume RESULT: At 195 degrees F = 4% air by volume....where did the air go? RELEASED INTO THE SYSTEM Means 100 gallons of water yields 4 gallons of air with a 135 degree F rise at start up

18 CHILLED WATER SYSTEMS Lower temperatures so air pockets are less likely to lockup system Corrosion still a concern Air removal device is recommended

19 Enhanced Air Separator Diffuser Straight Through Inlet Coalescing Brush Outlet Angle Pattern Inlet

20 Effective Air Separators Enhanced Air Separator (EAS) Coalescing Air Separator System Outlet Alternate System Inlet System Inlet To vent or tank

21 Enhanced Air Separator Brush filaments collect entrained air Excellent for radiant loop systems

22 In Line Air Separators Outlet System Inlet To Standard Tank or Vent To Pre-Charged Tank

23 Effective Air Separators In-Line Air Separator (IAS)

24 In Line Air Separators In-Line Air Separator (IAS): collects large air pockets; not as effective on entrained air as the EAS. Low Cost. Also known as an Air PURGER

25 Rolairtrol Centrifugal Air Separator System Inlet System Outlet To Standard (compression) Tank or Vent

26 System Inlet System Outlet To Standard Tank or Vent Rolairtrol Centrifugal Air Separator

27 Rolairtrol Centrifugal Air Separators Rolairtrol: For 2” thru 24” pipe; ASME Code construction; spinning water stays to outside of vessel, the lighter air rises through middle. The percent of entrained air removed per pass is published (air elimination efficiency) Choose size based on flow rate, NOT line-size; approx. 1psi pressure drop, or less, for 90%+ air elimination efficiency

28 Buffer Tank / Air Separator Boiler Buffer Tank