The most common terms rating air flow capacity are ICFM, FAD, ANR, SCFM or nl/min

Similar documents
ACFM vs. SCFM vs. ICFM Series of Technical White Papers from Squire-Cogswell

Fundamentals of Compressed Air Systems. Pre-Workshop Assignment

Advanced Management of Compressed Air Systems Pre-Workshop Assignment

CHAPTER 3 : AIR COMPRESSOR

Quick Reference Technical Data

GLOSSARY OF TERMS. Adiabatic Compression Compression process when all heat of compression is retained in the gas being compressed.

Reliability: Piping Distribution & Storage Matter. Instructor: Kurt Thielemann Principal

Best Practices Pneumatics Machine & Design. Written by Richard F. Bullers, CFPPS as published in Fluid Power Journal, July/August 2016

Technical Committee on LP-Gas at Utility Gas Plants

Getting the Most for Your Money

Application Worksheet

RELIEF CAPACITY CURVES

Gas Turbine Performance Analysis

Compressed Air - Food/Bev. Presented By: Adam Zimmerman

The Hoffman Specialty Series 2000 consists of main

Pressure Control. where: p is the pressure F is the normal component of the force A is the area

Lowering Compressed Air Pressure: What Works in the Plas9cs Industry? Introduc)on by Rod Smith, Publisher, Compressed Air Best Prac)ces Magazine

Sullair Air Systems. *Assessment of the market for compressed air efficiency services. Technical report, U.S. Department of Energy, June 2001

Case 12 Multistage Centrifugal Refrigeration System Halocarbon Refrigerant

Methods of Rating Flow

/ /

1 Exam Prep NFPA 99 Health Care Facilities Questions and Answers (Plumbing Contractor)

The Discussion of this exercise covers the following points: Pumps Basic operation of a liquid pump Types of liquid pumps The centrifugal pump.

(AS AT 31 st MARCH, 2002)

Device Description. Operating Information. CP Q (eq. 1) GT. Technical Bulletin TB-0607-CFP Hawkeye Industries Critical Flow Prover

pumping gases JET PUMP TECHNICAL DATA

DESIGN DATA. Dry 105a. September 5, 2008

4-7 kw/ hp. Dual Output Compressors (Air/Nitrogen) Driving Nitrogen Forward

Natural Gas Gathering

Quiz #1 Thermodynamics Spring, 2018 Closed Book, Open Appendices, Closed Notes, CLOSED CALCULATORS

1800CPB2 Service Regulators Maximum Inlet Pressure 125 PSIG

V248 Series 3-Way Pressure-Actuated Water-Regulating Valves for High-Pressure Refrigerants

SIZING THE WELL-X-TROL

SIZING OF WATER PIPING SYSTEM

Applied Fluid Mechanics

The Application of Temperature and/or Pressure Correction Factors in Gas Measurement

1800CPB2 Service Regulators

Practical Guide. By Steven T. Taylor, P.E., Member ASHRAE

TECHNICAL INFORMATION

09 - Choosing /sizing a cylinder and valve

SIZING OF WATER PIPING SYSTEM

CASH VALVE TYPE KP BACK PRESSURE VALVES

Troubleshooting Guide. Pg. 1

SIZING AND CAPACITIES OF GAS PIPING

Operating Guidelines for PermSelect Modules Liquid Contacting

SIZING THE EXTROL DIAPHRAGM-TYPE HYDRO-PNEUMATIC TANK

Pneumatic Conveying Systems Theory and Principles Session 100

TUTORIAL. NPSHA for those who hate that stuffy word. by Jacques Chaurette p. eng. copyright 2006

A centrifugal pump consists of an impeller attached to and rotating with the shaft and a casing that encloses the impeller.

Technical Information

Model 10. Low-Medium Pressure Reducing Regulator

SIZING AND CAPACITIES OF GAS PIPING

CNG FILLING STATIONS

Compiled by: B Beard. Approved by: SH Carstens. Description of requirements and procedures for compact provers to be used as verification standards.

Chapter 1: Basic Concepts of Pneumatics

Workhorse-15 Oxygen Generator

Gerald D. Anderson. Education Technical Specialist

SIZING AND CAPACITIES OF GAS PIPING

SG TF. Q = 963 Cv (P1 - P2)(P1 + P2) TECHNICAL INFORMATION. Flow Q (GPM)

SRL Series. Oil-less Scroll Air Compressors. Pharmaceutical. Research & Development. Food & Beverage. Chemical. Electronic

Air Cylinders Drive System Full Stroke Time & Stroke End Velocity

Air Amplifiers & SYSTEMS

Oil-injected rotary screw compressors GA (VSD + )

MULTI-STAGE VACUUM GENERATORS PVP M

Pressure on Demand. Air Pressure Amplifiers

S.A. Klein and G.F. Nellis Cambridge University Press, 2011

Cash Valve TYPE KP PILOT OPERATED BACK PRESSURE VALVE. ISSUED - DECEMBER 2000 CAVMC-0518-US-0208 ISO 9001 Certified

ENSURING AN ACCURATE RESULT IN AN ANALYTICAL INSTRUMENTATION SYSTEM PART 1: UNDERSTANDING AND MEASURING TIME DELAY

Installation and User Manual

TECHNICAL BULLETIN DESIGNING A FUNCTIONAL COMPRESSED AIR SYSTEM

Discontinued. Powers Controls. Technical Instructions Document No P25 RV Rev. 1, May, RV 201 Pressure Reducing Valves.

POP Safety Valve. POP Safety Valve INTRODUCTION DEFINITIONS

1800CPB2 Pilot-Loaded Service Regulators

Understanding Lobe Blowers Roots Blowers. Article written by Technical Team of EVEREST GROUP

Air Eliminators and Combination Air Eliminators Strainers

Multiple Pressure Booster Systems With Variable Speed Controller Type BL

2 are both ways of saying a ratio of 2 to 5

TOPIC: KNOWLEDGE: K1.01 [2.5/2.7] An atmospheric pressure of 15.0 psia is equivalent to... A psig. B psig. C psig.

PENBERTHY SERIES LM, ELL, FL, GL, GH, U, L AND 2NC FOR PUMPING GASES

Let s examine the evolution and application of some of the more popular types. Cascading Pressure Type

C 10 Pressure Reducing Valve

3M TM Versaflo TM AP-600 Series Air Filtration Panels For use with 3M TM Versaflo TM Supplied Air Respirator Systems. Work. in a World of.

PTF4 Pivotrol Pump (patented) version Dual Mechanism - Pressure Powered Pump

OVERVIEW. Flow Coefficient C v. Operating Conditions. Specific Gravity

Medical Oxygen Concentrator Systems. Generate gases on site generate savings

Nitrogen Advantage. Better Tire Pressure Retention. Improved Fuel Economy. Extended Tread Life. Elimination of Oxidation. Reduction in Tire Failures

Guideline No.M-05(201510) M-05 AIR COMPRESSOR. Issued date: 20 October China Classification Society

SIZING AND CAPACITIES OF GAS PIPING Reserved

How Inlet Conditions Impact Centrifugal Air Compressors

Exercise 4-2. Centrifugal Pumps EXERCISE OBJECTIVE DISCUSSION OUTLINE DISCUSSION. Pumps

IRC 2011 All Rights Reserved

Oxygen Generating Systems Ozone Medical Welding Glassblowing Aquaculture Pulp & Paper Wastewater

Installation, Operation, and Maintenance Manual Parker Balston Model N2-04 Nitrogen Generator

Air Operated Hydraulic Pumping Systems to 50,000 psi

Screw Compressors 11-22kW

COMPRESSED AIR SYSTEMS AND ENERGY SAVINGS

Plant, components and devices for very high and high pressures (7000 bar and over)

VBS-9263 Series. Application. Features. Applicable Literature

Exercise 2-3. Flow Rate and Velocity EXERCISE OBJECTIVE C C C

THE IMPACT ON ENERGY CONSUMPTION CAUSED BY PRESSURE DROP IN A COMPRESSED AIR SYSTEM

Transcription:

Rating of Air Compressors and Air Equipment The most common terms rating air flow capacity are ICFM, FAD, ANR, SCFM or nl/min There is no universal standard for rating air compressors, air equipment and tools. Common terms are: CFM ICFM ACFM FAD ANR SCFM nl/min CFM CFM (Cubic Feet per Minute) is the imperial method of describing the volume flow rate of compressed air. It must be defined further to take account of pressure, temperature and relative humidity - see below. ICFM ICFM (Inlet CFM) rating is used to measure air flow in CFM (ft 3 /min) as it enters the air compressor intake. ACFM ACFM (Actual CFM) rating is used to measure air flow in CFM at some reference point at local conditions. This is the actual volume flow rate in the pipework after the compressor. FAD FAD (Free Air Delivery) (f.a.d) is the actual quantity of compressed air converted back to the inlet conditions of the compressor. The units for FAD are CFM in the imperial system and l/min in the SI system. The units are in general measured according the ambient inlet standard conditions ISO 1217: Ambient temperature = 20 o C, Ambient pressure = 1 bar abs, Relative humidity = 0%, Cooling water/air = 20 o C and Effective working pressure at discharge valve = 7 bar abs. 1 m 3 /min (f.a.d) = 1000 liter/min (f.a.d) = 1000 dm 3 /min (f.a.d) = 16.7 l/s (f.a.d) = 16.7 dm 3 /s (f.a.d) = 35.26 ft 3 /min (f.a.d)

ANR ANR (Atmosphere Normale de Reference) is quantity of air at conditions 1.01325 bar absolute, 20 o C and 65% RH (Relative Humidity). SCFM SCFM (Standard CFM) is the flow in CFM measured at some reference point but converted back to standard air conditions (Standard Reference Atmosphere) 14.4 psia, 60 o F. nl/min nl/min is the flow in l/min measured at some reference point but converted to standard air conditions 1.01325 bar absolute, 0 o C and 0% RH (Relative Humidity). ISO 1217 standard reference ambient conditions - temperature 20 o C, pressure 1 bar abs, relative humidity 0%, cooling air/water 20 o C, and working pressure at outlet 7 bar absolute. Example - Rating a Compressor A typical rating of a compressor may look like this FAD (CFM) 11.1 cfm @ 7.5 Bar 8.2 cfm @ 10 Bar Description The Free Air Delivery from the compressor is 11.1 CFM at 7.5 Bar The Free Air Delivery from the compressor is 8.2 CFM at 10 Bar Calculating receivers in compressed air systems An air receiver is essential to every compressed air system to act as a buffer and a storage medium between the compressor and the consumption system. There are in principal two different air receivers in a compressed air system: PRIMARY receiver - located near the compressor, after the after-cooler but before filtration and drying equipment SECONDARY receivers - located close to points of larger intermittent air consumptions

The maximum capacity of the compressor in a well designed systems always exceed the maximum mean air consumption of the system (maximum mean air consumption is the mean air consumption over some reasonable time). Since the maximum capacity of an air compressor also always exceed the minimum air consumption in the system - the compressor must modulate its capacity during normal work, often by using primitive strategies as on/off modulating or more advanced strategies as frequency drives and inverters. Primitive modulating strategies cause more pressure variations in compressed air systems than more advanced strategies. In addition, the air consumption vary due to the process supported. In shorter periods the demand for compressed air may even exceed the maximum capacity of the compressor. In fact, it is common in well designed systems not to design the compressor for the maximum peek loads. Air receivers in compressed air systems serves the important purposes of equalizing the pressure variation from the start/stop and modulating sequence of the compressor storage of air volume equalizing the variation in consumption and demand from the system In addition the receiver serve the purpose of collecting condensate and water in the air after the compressor Sizing the Air Receiver The air receiver must in general be sized according the variation in the consumption demand the compressor size and the modulation strategy In general it is possible to calculate the maximum consumption in the system by summarizing the demand of each consumer. The summarized consumption must be multiplied with a usage factor ranging 0.1-1

depending on the system. In practice it is common that the manufacturer use standardized receivers for specific compressor models based on their know-how. For calculating the receiver, note that it is necessary with a pressure band for the receiver to be effective. If the consumption process requires 100 psig and the compressor is set to 100 psig, there is no storage and no buffer. Any increased demand makes a pressure drop below 100 psig until the compressor controls respond by increasing the volume compressed. If the compressors operates at 110 psig the difference between 110 psig and 100 psig accounts for the air stored in the receiver. If the demand increase, the pressure can drop 10 psig before the minimum requirement is met. Pressure and flow controllers can be used after the receiver for stabilizing downstream pressure to 100 psig and flattening demand peaks. Note that in a compressed air system the pipe work also makes the purpose of a buffered volume. The receiver volume may be calculated with the formula t = V (p 1 - p 2 ) / C p a (1) where V = volume of the receiver tank (cu ft) t = time for the receiver to go from upper to lower pressure limits (min) C = free air needed (scfm) p a = atmosphere pressure (14.7 psia) p 1 = maximum tank pressure (psia) p 2 = minimum tank pressure (psia) It is also common to size receivers to 1 gallon for each ACFM (Actual Cubic Feet per Minute), or 4 gallons per compressor hp (horse power)

Note! Receivers of unsound or questionable constructions may be very dangerous.

Air Receivers Capacities Air Receiver Capacities (cubic feet) Tank Size Tank Size Gauge Pressure on Tank (psig) (inches) (gallons) 0 100 150 200 12 x 24 10 1.3 11 15 19 14 x 36 20 2.7 21 30 39 16 x 36 30 4.0 31 45 59 20 x 48 60 8.0 62 90 117 20 x 63 80 11 83 120 156 24 x 68 120 16 125 180 234 30 x 84 240 32 250 360 467 1 ft 3 = 0.02832 m 3 1 inch = 25.4 mm 1 psig = 6.9 kpa = 0.069 bar 1 Gallon (U.S.) = 3.785x10-3 m 3 = 3.785 dm 3 (liter) = 231 in 3 Actual air compressor capacity (ACFM) versus standard air capacity (SCFM) and inlet air capacity (ICFM) SCFM - Standard Cubic Feet per Minute It is common to rate the compressed air consumption in Standard Cubic Feet per Minute - SCFM. The SCFM - Standard Cubic Feet per Minute - determines the weight of air to fixed or "Standard" conditions. There are several definitions of SCFM. The most common used in the United States is with "sea-level" properties:

14.696 Pounds per Square Inch (psia) 60 Degrees Fahrenheit ( o F) (520 o R) 0% Relative Humidity (RH) Europeans normally use one ata and 0 o C as SCFM. ACFM - Actual Cubic Feet per Minute Unfortunately, real life "actual conditions" are seldom "standard conditions". When pressure is applied a volume of air - it gets smaller vacuum is applied to a volume of air - it expand Actual air volume flow is often termed ACFM - Actual Cubic Feet per Minute. Actual Cubic Feet per Minute - ACFM, depends on the pressure temperature humidity of the actual air. The conversion from SCFM to ACFM can be expressed as ACFM = SCFM [P std / (P act - P sat Φ)](T act / T std ) (1)

where ACFM = Actual Cubic Feet per Minute SCFM = Standard Cubic Feet per Minute P std = Standard absolute air pressure (psia) P act = absolute pressure at the actual level (psia) P sat = Saturation pressure at the actual temperature (psi) Φ = Actual relative humidity T act = Actual ambient air temperature ( o R) T std = Standard temperature ( o R) Related Mobile Apps from The Engineering ToolBox SCFM - ACFM App - free apps for offline use on mobile devices. Online SCFM - ACFM Calculator The calculator below can used to calculate ACFM: 100 SCFM 14.7 Standard absolute air pressure (psia) 12.23 Actual absolute air pressure (psia) 0.5069 Saturation pressure at the actual temperature (psia) 0.80 Actual relative humidity 540 Actual ambient air temperature ( o R) 520 Standard air temperature ( o R)

temperature converter pressure converter Example - SCFM to ACFM The actual CFM of a compressor operating at "non-standard" conditions like elevation 5000 feet (1500 m) - atmospheric pressure P act = 12.23 psia temperature 80 o F - absolute temperature T act = 540 o R saturation pressure P sat = 0.5069 psia relative humidity Φ = 80% demand 100 SCFM can be calculated as ACFM = (100 SCFM) [(14.7 psia) / ((12.23 psia) - (0.5069 psia) (80 / 100))]((540 o R ) / (520 o R)) = 129.1 ICFM - Inlet Cubic Feet per Minute Inlet Cubic Feet per Minute - ICFM - is used by compressor vendors to establish conditions in front of additional equipment like inlet filter, blower or booster. When air passes through the filter there will be a pressure drop. The conversion from ICFM to ACFM can be expressed as ACFM = ICFM (P act / P f ) (T f / T act ) (2) where ICFM = Inlet Cubic Feet per Minute P f = Pressure after filter or inlet equipment (psia) T f = Temperature after filter or inlet equipment ( o R) Note! The Ideal Gas Law is accurate only at relatively low pressures and high temperatures. To account for the deviation from the ideal situation, another factor is included. It is called the Gas Compressibility Factor, or Z-factor. This correction factor is dependent on pressure and temperature for each gas considered. The True Gas Law, or the Non-Ideal Gas Law, becomes:

P V = Z n R T (3) where Z = Gas Compressibility Factor n = number of moles of gas present