Cover Page for Lab Report Group Portion. Pump Performance

Size: px
Start display at page:

Download "Cover Page for Lab Report Group Portion. Pump Performance"

Transcription

1 Cover Page for Lab Report Group Portion Pump Performance Prepared by Professor J. M. Cimbala, Penn State University Latest revision: 02 March 2012 Name 1: Name 2: Name 3: [Name 4: ] Date: Section number: ME 325. Group # Score (For instructor or TA use only): Lab experiment and results, plots, tables, etc. - Procedure portion Discussion Neatness & grammar TOTAL / 50 / 10 / 10 / 70 Comments (For instructor or TA use only):

2 Procedure and Presentations of Results A. The Test Rig and Its Operation A continuous pump flow rig is used in this lab experiment, as sketched in Figure 4. It is basically the same rig as the one that is used in the pipe flow experiment except that the pipe specimens are replaced by a centrifugal test pump, connected by flexible hoses. The test pump has two static pressure taps installed so that the head gain produced by the test pump can be measured directly, using a differential pressure transducer. Quick connect pressure line couplings are used to connect the pressure taps to the pressure transducers, so that the pressure lines can be connected quickly and easily. The volume flow rate through the test rig is measured by the Rosemount magnetic flow meter. Magnetic resonance flow meter Quick connects Pressure tap to high port of Head pressure transducer Flow control valves Pressure tap to low port of Head pressure transducer Test pump Water tank Flow pump Pump Figure 4. Schematic diagram of the pump flow test rig. The test pump is powered by a variable DC supply, so that pump speed can be varied. The shaft rotation speed n as well as the shaft torque, T, are measured directly by the Himmelstein torque and RPM meter. The brake horsepower, bhp, supplied to the pump is calculated from these two measurements, as explained in the Introduction. The back pressure (at the pump outlet) is controlled by a valve. If the valve is closed completely, no water flows through the pump (Q = V = 0), and the net head H is near its maximum value, as shown in Figure 3 of the Introduction. As the valve is opened, Q increases, and H begins to decrease, (the column height difference between the two manometer tubes decreases). The largest volume flow rate, Q max, is achieved when the valve is open enough such that there is no net head gain (or loss) across the pump (free delivery). Note that because the flow pump is capable of supplying a larger head and volume flow rate than the test pump, it is possible to generate conditions in which Q is actually larger than Q max, in which case the test pump supplies a negative net head to the flow in other words, the test pump acts like a minor loss in the system. By carefully adjusting either of the two downstream flow control valves, it should be possible to control the volume flow rate through the test pump so that it spans the desired range of interest, namely from Q = 0 to Q = Q max. B. Calibration of the Head Electronic Pressure Transducer To simplify the task of data collection, the net head across the pump is measured electronically by the computer data acquisition system. The Validyne electronic differential pressure transducer marked Head consists of a thin stainless steel diaphragm within a chamber. Each side of the chamber has a port, which will be connected to one of the pressure taps. Specifically, the low pressure side of the diaphragm will be connected to the static pressure tap at the upstream end of the test pump, while the high pressure side will be connected to the static pressure tap at the downstream end. When the flow loop is running, the test pump is on, and the flow control valves are set properly, the test pump provides a head gain across the pump. The larger pressure downstream of the pump causes the diaphragm inside the pressure transducer to deflect slightly. This deflection is measured electronically and is converted into a DC voltage that is displayed by the Validyne display unit. This voltage is also sent to the computer s Analog-to-Digital (A/D) converter for processing. As presently set up, the A/D converter can read voltages in the range from -5 to 5 volts. However, the Validyne display unit output is an analog voltage that ranges from only -2 to 2 volts. The display unit actually displays the voltage times a factor of 100. For example, a reading of 158 on the display unit corresponds to an analog voltage output of 1.58 volts. A reading of 200 units corresponds to the maximum 2.00 volts of the unit. Thus, to avoid clipping of the signal, never exceed 200 units on the Head display unit while acquiring data. Prior to data collection, the differential pressure transducer must be calibrated to measure the proper head, and to set the span such that nearly the full range of the display unit is utilized (for highest accuracy). The maximum head gain expected in this lab is less than 200 inches of water column, and the unit will be calibrated such that 100 inches of water corresponds to 100 display units, or 1.00 volts. There is a calibration stand in the lab, which is set up to provide 48.0 inches 1

3 of water head as a calibration point. In this lab experiment, therefore, the head transducer will be calibrated such that volts (48.0 display units) corresponds to 48.0 inches of water head. (48 inches per 0.48 volts is the same as 100 inches per 1.0 volts.) To calibrate the transducer, follow these steps: 1. Place both stainless steel calibration containers on the top shelf of the calibration stand, side by side. 2. Check that both manometer tubes coming from the calibration tanks are connected to the pressure transducer inputs (high pressure tank to the high pressure port and low pressure tank to the low pressure port). 3. Add water to the calibration containers (if necessary) until they are about 3/4 full (and approximately equal in level). 4. This step is critical! Any trapped air bubbles in any of the lines will lead to severe calibration errors. Bleed water from the manometer tubes into the return tank by opening the two blue thumb bleed valves (located near the bottom of the manometer) to remove any air bubbles trapped in the manometer tubes. Also open the blue thumb valves that are connected to the Head differential pressure transducer. At the same time, open both bleed valves on top of the Head differential pressure transducer to bleed any air bubbles trapped in the lines or in the transducer chamber itself. Note: These valves are open when the switch handle is vertical, and are closed when the handle is horizontal. Bleed all of the air bubbles out of both lines and both manometer tubes. Lightly tap the control panel to dislodge any bubbles trapped inside. If you are unable to get rid of the air bubbles, get help from your instructor or TA before proceeding. When all air bubbles have been removed, you are now ready to calibrate. 5. Add water to (or drain water from) one of the calibration containers if necessary until the water in both containers is at the same level (approximately 68 inches on the manometer scale, which has an arbitrary datum plane). 6. At this point, there is zero pressure difference across the pressure transducer. If necessary, adjust the ZERO potentiometer on the Head Validyne display unit until the reading is zero. 7. Carefully and slowly move the right hand (low pressure) calibration container from the high shelf to the low shelf. If not done slowly, new bubbles may form in the manometer tube take your time here or you will have to start over at Step Add water to (or drain water from) the low pressure calibration container if necessary until the difference in height between the two manometer tubes is exactly 48.0 inches. 9. At this point, the pressure difference across the pressure transducer is 48.0 inches. Adjust the SPAN potentiometer on the pressure transducer display unit until the reading is 48.0 units. As discussed above, this calibrates the transducer to 48.0 inches of water head per 0.48 volts (100 inches of water per 100 units). 10. Now that the span has been set, the zero may have shifted slightly. Slowly return the low pressure calibration container to the upper shelf. The Head Validyne display unit should return to zero. Repeat Steps 5 through 9 if necessary until both the zero setting and the pressurized setting are correct. 11. The differential pressure transducer is now properly calibrated. (A linear transducer response is assumed, and is quite accurate.) Return the low pressure calibration tank to the upper shelf. 12. Close off the blue thumb valves and then disconnect the tubing from the pressure transducer to the calibration tanks. Instead, connect the high pressure port of the pressure transducer to the quick connect leading from the pressure tap at the downstream (outlet) end of the test pump. Connect the low pressure port of the pressure transducer to the quick connect leading from the pressure tap at the upstream (intlet) end of the test pump. C. Data Collection 1. Add water if necessary to the water tank so that the flow pump is fully submerged. Verify that the test pump is properly installed, and that all the flow control valves are partially open. 2. Turn on the flow pump and make sure there are no significant leaks through any of the connections (some dripping is okay). If leaks persist, call your instructor or TA for assistance. The head reading should be negative, indicating that the test pump is acting as a minor loss. This is expected, of course, when the test pump is not turned on. 3. Bleed the flow system of all air bubbles. Note: This is a very critical step! Air bubbles in any of the pressure lines will lead to gross errors in your data. To bleed the air bubbles properly, close the flow control valve about 95% of the way (not fully closed because this will burn out the flow pump). This lowers the flow rate to a trickle, and increases the head in all the tubes, which aids in purging out any trapped air bubbles in the lines. Open both bleed valves above the pressure transducers. Tap on the tubing quick connects to release trapped air bubbles, and watch them until they move all the way through the pressure line, through the control panel, through the pressure transducer, and out the bleed valve. Close both bleed valves. 2

4 4. Start program PumpLabMeasure from the computer s desktop. In the User Control window, Enter Parameters. In the User Entries window that pops up, Save Results File, and enter a file name for your data set. For uniqueness of your data file, name your file something indicative of your group and of the test specimen, such as Smith_groupC_pump_1000.txt, where Smith is the name of one of the group members, and the 1000 represents the rpm of the first data set. Unless calibrated otherwise, the calibration constant should default to 1.0 V = inches of water head, since the Head transducer is calibrated at 48.0 units (0.480 V) per 48.0 inches of water head. OK. 5. Turn on the test pump, and adjust the speed of the test pump until the rpm is as close as possible to 1000 rpm. Check for any additional air bubbles in the pressure lines, and bleed if necessary. (5) 6. Adjust the valves if necessary so that the Head display is positive (the pump is operating somewhere within its designed operating range). Record the following values from the instruments (manual readings): Manual readings at 1000 rpm: Torque, T: ounce-inches (oz-in) Rotation rate, n : rotations per minute (rpm) Volume flow rate, Q or V : liters per minute (L/min) Motor supply voltage, E: volts (V) Motor supply current, I: amperes (A) (5) 7. Convert the volume flow rate to cubic meters per second, showing your calculations below, including all unit conversions: Calculated Q or V : m 3 /s Calculate the electrical power delivered to the motor, Welectric EI in watts, showing your calculations below: Calculated W electric : W (5) 8. Compare the manual reading of the pump s net head, torque, and rotation rate to those measured and calculated by the computer (take a data point using the data acquisition system be sure to also enter into the computer the volume flow rate displayed on the Rosemount flow meter before starting the data acquisition process. Note that the manual readings fluctuate and are difficult to read the computer averages the voltages for several seconds so that the averaged outputs are much more stable, easier to read, and therefore more accurate. Manual net head calculation: Validyne Head display: units Validyne Head voltage: Volts (V) Calculated net head, H: inches of water (in H 2O) Computer-acquired values: Net head, H: inches of water (in H 2O) Torque, T: ounce-inches (oz-in) Rotation rate, n : rotations per minute (rpm) Make sure that the computer s values agree reasonably well with those recorded manually. If they don t, something is not set correctly ask your instructor or TA for assistance if needed. It is a good idea to take a few data points with the computer to verify that the flow rate and the readings are stable and repeatable. 9. Open an Excel spreadsheet, and list your group members names and date at the top. Type the following column titles near the top of the spreadsheet: Motor voltage (V), Motor current (A), RPM (rot/min), Torque (oz-in), Volume flow rate (L/min), and Net head (in H 2O). Enter the values recorded above as your first data point. 3

5 10. Sample many more data points at various flow rates, but at a constant test pump rotational speed of 1000 rpm. Start with the flow control valve open enough to get nearly zero net head, and then slowly close the valve. At each valve setting, use the computer to measure net head H, torque T, and rotation rate n. Other parameters, such as the volume flow rate of water, motor voltage, and motor current must be read from the instruments and entered manually into the spreadsheet. Note: As H changes, the load on the test pump is changed, and its rpm may drift. Adjust the pump speed as required (with the potentiometer) in order to maintain a constant rpm throughout the test, as best as possible (it is somewhat sensitive and difficult to control precisely). The manometer tubes may need to be bled occasionally to free trapped air bubbles. Be sure to take enough data points for meaningful results; take data from Q = Q max to Q = 0. Never close the control valve completely for more than a few seconds, as this can cause pump burnout! It is OK to cycle the flow rate up and down, taking data along the way. Note: Monitor the Head Validyne display unit to ensure that the reading never drops below zero units or rises above 200 units. Repeat some of your data points more than once to check for repeatability of the measurements. 11. Increase the rotational speed to about 2000 rpm. Repeat the data collection for the full range of valve settings. Make sure to begin at Q = Q max, which corresponds to zero head loss over the pump, and continue until Q = 0. You will need to open the valves around the pump to achieve Q max. 12. When finished, turn both pumps off. Do not turn off the computer or the Himmelstein unit or the magnetic flow meter, and do not drain the water from the lower tank unless told to do so by your instructor or TA. You may exit the data acquisition program (Quit). E. Presentation of the Data (5) 1. Being careful with unit conversions, add columns to your spreadsheet and calculate angular velocity (rad/s), net head H (m), volume flow rate V (m 3 /s), supplied motor power W electric (W), water horsepower delivered by the pump W water horsepower (W), pump efficiency pump (dimensionless), and pump-motor efficiency pump-motor (dimensionless). Show sample calculations for all parameters here: Sample Calculations: (5) 2. Generate a plot of net head as a function of volume flow rate. Include both sets of data (at both rpm settings) on the same plot (use a different symbol for each rpm, and be sure to include a figure caption, figure number, and legend on your plot). 4

6 (5) 3. Generate a plot of pump and pump-motor efficiency as a function of Q for both sets of data on the same plot. (5) 4. Add additional columns, as needed, to your Excel spreadsheets in order to calculate the nondimensional pump parameters C Q and C H for each data point, and for each rpm case. Note: For the pump used in this experiment, the impeller diameter D = 3.5 in. Show sample calculations of C Q and C H in the space below, showing all units, unit conversions, etc. Make sure all your units cancel, as they must since these are dimensionless parameters. Sample Calculations: (5) 5. Make printouts of both of your Excel data files. Attach these tables, along with a title and table number for each, to this report. Record the table numbers here as well. See Tables. (5) 6. Generate a plot of C H, with all the data from both rpm settings on the same plot. Use different symbols for each case so that the data are distinguishable. Number, label, and attach your plot to your report and record the number here. (5) 7. In a similar manner, generate a plot of pump and pump-motor for all cases. Number, label, and attach your plot to your report and record the number here. 5

7 Discussion (5) 1. Explain how this lab has helped you to understand the performance characteristics of centrifugal pumps. Specifically, discuss the trade-offs between high volume flow rate and large pump head. (5) 2. Do the predictions of dimensional analysis really work? Specifically, do the data for C H from different pump speeds collapse onto the same curve when plotted nondimensionally? Why or why not? What about the data for pump and pump-motor? Compare and discuss. 6

Cover Page for Lab Report Group Portion. Head Losses in Pipes

Cover Page for Lab Report Group Portion. Head Losses in Pipes Cover Page for Lab Report Group Portion Head Losses in Pipes Prepared by Professor J. M. Cimbala, Penn State University Latest revision: 02 February 2012 Name 1: Name 2: Name 3: [Name 4: ] Date: Section

More information

Cover Page for Lab Report Group Portion. Drag on Spheres

Cover Page for Lab Report Group Portion. Drag on Spheres Cover Page for Lab Report Group Portion Drag on Spheres Prepared by Professor J. M. Cimbala, Penn State University Latest revision: 29 September 2017 Name 1: Name 2: Name 3: [Name 4: ] Date: Section number:

More information

Cover Page for Lab Report Group Portion. Lift on a Wing

Cover Page for Lab Report Group Portion. Lift on a Wing Cover Page for Lab Report Group Portion Lift on a Wing Prepared by Professor J. M. Cimbala, Penn State University Latest revision: 17 January 2017 Name 1: Name 2: Name 3: [Name 4: ] Date: Section number:

More information

Lab #1 Pressure: Bubblers and Water Balloons CEE 331 Fall 2003

Lab #1 Pressure: Bubblers and Water Balloons CEE 331 Fall 2003 CEE 331 Lab 1 Page 1 of 9 SAFETY Lab #1 Pressure: Bubblers and Water Balloons CEE 331 Fall 2003 Laboratory exercise based on an exercise developed by Dr. Monroe Weber-Shirk The major safety hazard in this

More information

Cover Page for Lab Report Group Portion. Boundary Layer Measurements

Cover Page for Lab Report Group Portion. Boundary Layer Measurements Cover Page for Lab Report Group Portion Boundary Layer Measurements Prepared by Professor J. M. Cimbala, Penn State University Latest revision: 30 March 2012 Name 1: Name 2: Name 3: [Name 4: ] Date: Section

More information

Cover Page for Lab Report Group Portion. Compressible Flow in a Converging-Diverging Nozzle

Cover Page for Lab Report Group Portion. Compressible Flow in a Converging-Diverging Nozzle Cover Page for Lab Report Group Portion Compressible Flow in a Converging-Diverging Nozzle Prepared by Professor J. M. Cimbala, Penn State University Latest revision: Prof. Steve Lynch, 14 February 2017

More information

The Discussion of this exercise covers the following points:

The Discussion of this exercise covers the following points: Exercise 5-3 Wet Reference Leg EXERCISE OBJECTIVE Learn to measure the level in a vessel using a wet reference leg. DISCUSSION OUTLINE The Discussion of this exercise covers the following points: Measuring

More information

Lab 1: Pressure and surface tension. Bubblers, gravity and the mighty paper clip.

Lab 1: Pressure and surface tension. Bubblers, gravity and the mighty paper clip. Lab 1: Pressure and surface tension. Bubblers, gravity and the mighty paper clip. CEE 3310 - Summer 2012 SAFETY The major safety hazard in this laboratory is a shock hazard. Given that you will be working

More information

Cover Page for Lab Report Group Portion. Compressible Flow in a Converging-Diverging Nozzle

Cover Page for Lab Report Group Portion. Compressible Flow in a Converging-Diverging Nozzle Cover Page for Lab Report Group Portion Compressible Flow in a Converging-Diverging Nozzle Prepared by Professor J. M. Cimbala, Penn State University Latest revision: 13 January 2012 Name 1: Name 2: Name

More information

1. Study the performance of a binary distillation column operated in batch mode.

1. Study the performance of a binary distillation column operated in batch mode. Goals for batch distillation using the East distillation column: 1. Study the performance of a binary distillation column operated in batch mode. 2. Determine the overall and local efficiency of the column

More information

Exercise 8. Closed-Loop Pressure Control, Proportional-Plus-Integral Mode EXERCISE OBJECTIVE

Exercise 8. Closed-Loop Pressure Control, Proportional-Plus-Integral Mode EXERCISE OBJECTIVE Exercise 8 Closed-Loop Pressure Control, EXERCISE OBJECTIVE To understand open and closed-loop pressure control; To learn how to sense the pressure in a pneumatic circuit; To control the pressure in a

More information

Pump Performance Testing

Pump Performance Testing Pump Performance Testing SAFETY Keep water away from all electrical equipment except the pump, and do your best to keep the pump motor dry. Don t handle the power supply or multimeter(s) with wet hands

More information

Lab #4 Pipe Flow, Minor and Major Losses, and Walking in Osborne Reynolds Shoes CEE 331 Fall 2006

Lab #4 Pipe Flow, Minor and Major Losses, and Walking in Osborne Reynolds Shoes CEE 331 Fall 2006 CEE 331 Lab 4 Page 1 of 5 Lab #4 Pipe Flow, Minor and Major Losses, and Walking in Osborne Reynolds Shoes CEE 331 Fall 2006 Safety The major safety hazard in this laboratory is a shock hazard. Given that

More information

Exercise 2-2. Second-Order Interacting Processes EXERCISE OBJECTIVE DISCUSSION OUTLINE. The actual setup DISCUSSION

Exercise 2-2. Second-Order Interacting Processes EXERCISE OBJECTIVE DISCUSSION OUTLINE. The actual setup DISCUSSION Exercise 2-2 Second-Order Interacting Processes EXERCISE OBJECTIVE Familiarize yourself with second-order interacting processes and experiment with the finer points of controller tuning to gain a deeper

More information

The Discussion of this exercise covers the following points:

The Discussion of this exercise covers the following points: Exercise 3-2 Orifice Plates EXERCISE OBJECTIVE In this exercise, you will study how differential pressure flowmeters operate. You will describe the relationship between the flow rate and the pressure drop

More information

Lab 1c Isentropic Blow-down Process and Discharge Coefficient

Lab 1c Isentropic Blow-down Process and Discharge Coefficient 058:080 Experimental Engineering Lab 1c Isentropic Blow-down Process and Discharge Coefficient OBJECTIVES - To study the transient discharge of a rigid pressurized tank; To determine the discharge coefficients

More information

Exercise 5-2. Bubblers EXERCISE OBJECTIVE DISCUSSION OUTLINE. Bubblers DISCUSSION. Learn to measure the level in a vessel using a bubbler.

Exercise 5-2. Bubblers EXERCISE OBJECTIVE DISCUSSION OUTLINE. Bubblers DISCUSSION. Learn to measure the level in a vessel using a bubbler. Exercise 5-2 Bubblers EXERCISE OBJECTIVE Learn to measure the level in a vessel using a bubbler. DISCUSSION OUTLINE The Discussion of this exercise covers the following points: Bubblers How to measure

More information

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

Exercise 4-2. Centrifugal Pumps EXERCISE OBJECTIVE DISCUSSION OUTLINE DISCUSSION. Pumps Exercise 4-2 Centrifugal Pumps EXERCISE OBJECTIVE Familiarize yourself with the basics of liquid pumps, specifically with the basics of centrifugal pumps. DISCUSSION OUTLINE The Discussion of this exercise

More information

Instruction Manual. Pipe Friction Training Panel

Instruction Manual. Pipe Friction Training Panel Instruction Manual HL 102 Pipe Friction Training Panel 100 90 80 70 60 50 40 30 20 10 HL 102 Instruction Manual This manual must be kept by the unit. Before operating the unit: - Read this manual. - All

More information

INSTRUCTION MANUAL. process. Ultrasonic Flowmeter Range

INSTRUCTION MANUAL. process. Ultrasonic Flowmeter Range INSTRUCTION MANUAL process TM Ultrasonic Flowmeter Range process TM CONTENTS Page No 1 General 4 2 Order Codes 4 3 Installation 5 & 6 4 Specifications 7 & 8 1 General 3 Installation The Process Atrato

More information

The Discussion of this exercise covers the following points: Range with an elevated or suppressed zero Suppressed-zero range Elevated-zero range

The Discussion of this exercise covers the following points: Range with an elevated or suppressed zero Suppressed-zero range Elevated-zero range Exercise 4-3 Zero Suppression and Zero Elevation EXERCISE OBJECTIVE In this exercise, you will learn the effect that mounting a pressure transmitter above or below the reference level has on the hydrostatic

More information

(AS AT 31 st MARCH, 2002)

(AS AT 31 st MARCH, 2002) ACACA PROTOCOL 2000 (AS AT 31 st MARCH, 2002) ACACA PROTOCOL 2000 INCLUDES (A) CODE OF PRACTICE FOR MANUFACTURERS AND/OR SUPPLIERS OF COMMERCIAL AIR COMPRESSORS AND METHOD FOR DETERMINING (B) RECIPROCATING

More information

Armfield Distillation Column Operation Guidelines

Armfield Distillation Column Operation Guidelines Armfield Distillation Column Operation Guidelines 11-2016 R.Cox Safety SAFETY GLASSES ARE REQUIRED WHEN OPERATING THE DISTILLATION COLUMN Wear gloves when mixing alcohol feedstock The column will become

More information

Manual for continuous distillation

Manual for continuous distillation Manual for continuous distillation 1. Week 1: Objectives: Run the column at total reflux. When steady state is reached, take the sample from the top and bottom of the column in order to determine the overall

More information

XDF BURNERS DUAL FUEL EXCESS AIR BURNER FEATURES DESCRIPTION EXCESS AIR OPERATION

XDF BURNERS DUAL FUEL EXCESS AIR BURNER FEATURES DESCRIPTION EXCESS AIR OPERATION DUAL FUEL EXCESS AIR BURNER MODEL: 3610, 3651 Revision: 0 FEATURES Burns all fuel gases or light oils Nozzle mix design for on ratio control or excess air 350% excess air all sizes on gas or oil Turndown

More information

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

A centrifugal pump consists of an impeller attached to and rotating with the shaft and a casing that encloses the impeller. Centrifugal pump How centrifugal pumps work A centrifugal pump consists of an impeller attached to and rotating with the shaft and a casing that encloses the impeller. In centrifugal pump, liquid is forced

More information

User Manual for the Mars Calibration Bench

User Manual for the Mars Calibration Bench User Manual for the Mars Calibration Bench Fall 2013 Table of Contents Table of Contents Table of Contents... iii Introduction... v Chapter 1: The Mars Calibration Bench... 1 What Is the Mars Calibration

More information

Operating Instructions

Operating Instructions Operating Instructions Note: 1. Never let the centrifugal pump run dry. 2. Make sure that there is at least one open path for water flow in the pipe network before turning the pump on. Never run the pump

More information

BAPI Pressure Line of Products - FAQs

BAPI Pressure Line of Products - FAQs Table of Contents 1. Several manufacturers produce pressure transmitters, why should I purchase from BAPI?... p. 2 2. BAPI makes several styles of pressure transmitters. What are the features of each?...

More information

Model 106 DPI "Micro-switch" Installation and Operating Instructions

Model 106 DPI Micro-switch Installation and Operating Instructions Mid-West Instrument Model 106 DPI "Micro-switch" Installation and Operating Instructions BULLETIN NO. IM116DPImicro/09A Replaces --- INSPECTION Before installation carefully check the Model Number on each

More information

AC : A LABORATORY EXERCISE TO DEMONSTRATE HOW TO EXPERIMENTALLY DETERMINE THE OPERATING POINT FOR A FAN

AC : A LABORATORY EXERCISE TO DEMONSTRATE HOW TO EXPERIMENTALLY DETERMINE THE OPERATING POINT FOR A FAN AC 2007-206: A LABORATORY EXERCISE TO DEMONSTRATE HOW TO EXPERIMENTALLY DETERMINE THE OPERATING POINT FOR A FAN Robert Edwards, Pennsylvania State University-Erie Robert Edwards is currently a Lecturer

More information

Cover Page for Lab Report Group Portion. Flow Visualization in a Water Channel

Cover Page for Lab Report Group Portion. Flow Visualization in a Water Channel Cover Page for Lab Report Group Portion Flow Visualization in a Water Channel Prepared by Professor J. M. Cimbala, Penn State University Latest revision: 08 September 2017 Name 1: Name 2: Name 3: [Name

More information

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

L 100. Bubble-Tube Level System. Installation, Operation and Maintenance Instructions L 100 Bubble-Tube Level System Installation, Operation and Maintenance Instructions Figure 1 Contents Section Description Page 1.0 Introduction 2 2.0 Specifications 3 3.0 Installation 3 4.0 Warranty 6

More information

AC : MEASUREMENT OF HYDROGEN IN HELIUM FLOW

AC : MEASUREMENT OF HYDROGEN IN HELIUM FLOW AC 2010-2145: MEASUREMENT OF HYDROGEN IN HELIUM FLOW Randy Buchanan, University of Southern Mississippi Christopher Winstead, University of Southern Mississippi Anton Netchaev, University of Southern Mississippi

More information

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

The Discussion of this exercise covers the following points: Pumps Basic operation of a liquid pump Types of liquid pumps The centrifugal pump. Exercise 2-3 Centrifugal Pumps EXERCISE OBJECTIVE In this exercise, you will become familiar with the operation of a centrifugal pump and read its performance chart. You will also observe the effect that

More information

Pegas 4000 MF Gas Mixer InstructionManual Columbus Instruments

Pegas 4000 MF Gas Mixer InstructionManual Columbus Instruments Pegas 4000 MF Gas Mixer InstructionManual Contents I Table of Contents Foreword Part I Introduction 1 2 1 System overview... 2 2 Specifications... 3 Part II Installation 4 1 Rear panel connections...

More information

ONSITE PROVING OF GAS METERS. Daniel J. Rudroff WFMS Inc West Bellfort Sugar Land, Texas. Introduction

ONSITE PROVING OF GAS METERS. Daniel J. Rudroff WFMS Inc West Bellfort Sugar Land, Texas. Introduction ONSITE PROVING OF GAS METERS Daniel J. Rudroff WFMS Inc. 13901 West Bellfort Sugar Land, Texas Introduction With the increased use of Natural Gas as a fuel, and higher natural gas prices buyers and sellers

More information

Experiment 8: Minor Losses

Experiment 8: Minor Losses Experiment 8: Minor Losses Purpose: To determine the loss factors for flow through a range of pipe fittings including bends, a contraction, an enlargement and a gate-valve. Introduction: Energy losses

More information

Constant Pressure Inlet (CCN) Operator Manual

Constant Pressure Inlet (CCN) Operator Manual Constant Pressure Inlet (CCN) Operator Manual DOC-0125 Revision J 2545 Central Avenue Boulder, CO 80301-5727 USA C O P Y R I G H T 2 0 1 1 D R O P L E T M E A S U R E M E N T T E C H N O L O G I E S, I

More information

(Refer Slide Time: 2:16)

(Refer Slide Time: 2:16) Fluid Machines. Professor Sankar Kumar Som. Department Of Mechanical Engineering. Indian Institute Of Technology Kharagpur. Lecture-23. Diffuser and Cavitation. Good morning and welcome you all to this

More information

This portion of the piping tutorial covers control valve sizing, control valves, and the use of nodes.

This portion of the piping tutorial covers control valve sizing, control valves, and the use of nodes. Piping Tutorial A piping network represents the flow of fluids through several pieces of equipment. If sufficient variables (flow rate and pressure) are specified on the piping network, CHEMCAD calculates

More information

Installation and Operation Manual

Installation and Operation Manual Manual Static pressure transducer with controller Differential static pressure transducer with analog output and optional PI control mode Large diaphragm element with differential transformer Transducer

More information

256 Pneumatic Pressure Indicator

256 Pneumatic Pressure Indicator 256 Pneumatic Pressure Indicator 51425699 Copyright 2002 Slope Indicator Company. All Rights Reserved. This equipment should be installed, maintained, and operated by technically qualified personnel. Any

More information

ACCESSORY KIT INSTALLATION INSTRUCTIONS

ACCESSORY KIT INSTALLATION INSTRUCTIONS ACCESSORY KIT INSTALLATION INSTRUCTIONS 1NP0680 - PROPANE CONVERSION FOR USE WITH MODELS: PM8, PC8, PM9, PC9, FL9M, FL9C, FC9M, FC9C This conversion kit is to be installed by a qualified service agency

More information

P-5215 Differential Pressure Transmitter

P-5215 Differential Pressure Transmitter P-5215 Differential Pressure Transmitter Pneumatic Control Manual 717.1 Pressure Section Product Bulletin P-5215 Issue Date 0891 Features and Benefits Ultra Sensitive Feedback Circuit - Enhances System

More information

AerE 343L: Aerodynamics Laboratory II. Lab Instructions

AerE 343L: Aerodynamics Laboratory II. Lab Instructions AerE 343L: Aerodynamics Laboratory II Lab Instructions Lab #2: Airfoil Pressure Distribution Measurements and Calibration of a Small Wind Tunnel Instructor: Dr. Hui Hu Department of Aerospace Engineering

More information

UBEC 1AT. AUTO TANK Fill System Installation, Operation, & Setup Instructions

UBEC 1AT. AUTO TANK Fill System Installation, Operation, & Setup Instructions Document Number: XE-ATA5PM-R1A UBEC 1AT AUTO TANK Fill System 08899155 Installation, Operation, & Setup Instructions Rev170906-EB-FRC PHYSICAL: 1302 WEST BEARDSLEY AVE ELKHART, IN 46514 WWW.ELKHARTBRASS.COM

More information

PEAPOD. Pneumatically Energized Auto-throttled Pump Operated for a Developmental Upperstage. Test Readiness Review

PEAPOD. Pneumatically Energized Auto-throttled Pump Operated for a Developmental Upperstage. Test Readiness Review PEAPOD Pneumatically Energized Auto-throttled Pump Operated for a Developmental Upperstage Test Readiness Review Customer: Special Aerospace Services Chris Webber and Tim Bulk 1 Overview Project Overview

More information

MEMORIAL UNIVERSITY OF NEWFOUNDLAND Faculty of Engineering and Applied Science FLUID MECHANICS LABORATORY PIPE FRICTION

MEMORIAL UNIVERSITY OF NEWFOUNDLAND Faculty of Engineering and Applied Science FLUID MECHANICS LABORATORY PIPE FRICTION MEMORIAL UNIVERSITY OF NEWFOUNDLAND Faculty of Engineering and Applied Science FLUID MECHANICS LABORATORY PIPE FRICTION Objective To estimate the fluid pressure drops and roughness specifications for copper

More information

Sizing Pulsation Dampeners Is Critical to Effectiveness

Sizing Pulsation Dampeners Is Critical to Effectiveness Sizing Pulsation Dampeners Is Critical to Effectiveness Pressure variation is an important consideration when determining the appropriate size pulsation dampener needed for an application. by David McComb,

More information

Water Weir Flow Controller. Introduction. Safety Precautions. Mounting the Hardware

Water Weir Flow Controller. Introduction. Safety Precautions. Mounting the Hardware 57007-88 Introduction Safety Precautions This instruction sheet describes how to set up and use the Hach (Figure 1). A water weir is a device that raises or diverts water to regulate the flow. Hach s water

More information

CONTENT. General Requirement. 2 Lab Format Lab Reports Self-evaluation Grading of Lab Reports Reference

CONTENT. General Requirement. 2 Lab Format Lab Reports Self-evaluation Grading of Lab Reports Reference CE322 Hydraulic Laboratory Component General Information, Requirements, and Instructions (Prepared by Dr. Jim Liou, Department of Civil Engineering, Univ. of Idaho) CONTENT General Requirement. 2 Lab Format

More information

Title: Standard Operating Procedure for Dasibi Model 5008 Gas Dilution Calibrator

Title: Standard Operating Procedure for Dasibi Model 5008 Gas Dilution Calibrator Procedure No: SOP-034 Revision No: 1.0 Revised Dec. 29, 2010 Page No.: 1 of 10 1. INTRODUCTION AND SCOPE This procedure is intended to describe the operations of the Dasibi model 5008 calibrator. The Dasibi

More information

KC Series Gas Components and Supply Design Guide

KC Series Gas Components and Supply Design Guide Technical Bulletin KC Series Gas Components and Supply Design Guide GF-1030 General AERCO KC Series gas fired potable water heaters and boilers are modulating input devices that require an adequate volume

More information

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

Exercise 2-3. Flow Rate and Velocity EXERCISE OBJECTIVE C C C Exercise 2-3 EXERCISE OBJECTIVE C C C To describe the operation of a flow control valve; To establish the relationship between flow rate and velocity; To operate meter-in, meter-out, and bypass flow control

More information

Radar, Ultrasonic and RF Level Transmitters

Radar, Ultrasonic and RF Level Transmitters Radar, Ultrasonic and RF Level Transmitters Both measures the time it takes the wave to travel between the transmitter and that reflected wave off the surface of the material to reach the transmitter again.

More information

SINGLE VALVE WITH LOW-FLOW BYPASS

SINGLE VALVE WITH LOW-FLOW BYPASS CONTROL VALVES Pressure Reducing Valve Sizing Guide Sizing pilot operated reducing valves is not a complicated process. It starts with determining requirements and following these guidelines in valve size

More information

OIL SUPPLY SYSTEMS ABOVE 45kW OUTPUT 4.1 Oil Supply

OIL SUPPLY SYSTEMS ABOVE 45kW OUTPUT 4.1 Oil Supply OIL SUPPLY SYSTEMS ABOVE 45kW OUTPUT 4.1 Oil Supply 4.1.1 General The primary function of a system for handling fuel oil is to transfer oil from the storage tank to the oil burner at specified conditions

More information

Modulating Valves for Atmospheric, Infrared, and Direct Fired Burners

Modulating Valves for Atmospheric, Infrared, and Direct Fired Burners BULLETIN MT2035-07/05 Modulating Valves for Atmospheric, Infrared, and Direct Fired Burners M/MR Series M411, M511, M611 M420, M520, M620, MR410, MR510, MR610 MR212D, MR212E, MR212G and MR212J (Flanged),

More information

Experiment Instructions. Circulating Pumps Training Panel

Experiment Instructions. Circulating Pumps Training Panel Experiment Instructions Circulating Pumps Training Panel Experiment Instructions This manual must be kept by the unit. Before operating the unit: - Read this manual. - All participants must be instructed

More information

Refiner Trial Working Manual Rev 3 updated July 26, 2012 by Nici Darychuk

Refiner Trial Working Manual Rev 3 updated July 26, 2012 by Nici Darychuk Refiner Trial Working Manual Rev 3 updated July 26, 2012 by Nici Darychuk Steps for Preparing Refiner Loop and Running Trial Before the trial 1. Minimum 2 hours before trial, switch on all electrical power

More information

ONSITE PROVING OF GAS TURBINE METERS Daniel J. Rudroff Invensys Metering Systems

ONSITE PROVING OF GAS TURBINE METERS Daniel J. Rudroff Invensys Metering Systems ONSITE PROVING OF GAS TURBINE METERS Daniel J. Rudroff Invensys Metering Systems 1322 Foxwood, Houston, Texas 77008 INTRODUCTION With the increased use of Natural Gas as a fuel, higher natural gas prices,

More information

CHEMICAL ENGINEERING LABORATORY CHEG 239W. Control of a Steam-Heated Mixing Tank with a Pneumatic Process Controller

CHEMICAL ENGINEERING LABORATORY CHEG 239W. Control of a Steam-Heated Mixing Tank with a Pneumatic Process Controller CHEMICAL ENGINEERING LABORATORY CHEG 239W Control of a Steam-Heated Mixing Tank with a Pneumatic Process Controller Objective The experiment involves tuning a commercial process controller for temperature

More information

Pump Selection and Sizing (ENGINEERING DESIGN GUIDELINE)

Pump Selection and Sizing (ENGINEERING DESIGN GUIDELINE) Guidelines for Processing Plant Page : 1 of 64 Feb 2007 (ENGINEERING DESIGN GUIDELINE) Author: A L Ling Checked by: Karl Kolmetz TABLE OF CONTENT INTRODUCTION Scope 5 General Design Consideration Type

More information

Test Report # Rev 0. Adiabatic Compression With Constant Bleed Valve

Test Report # Rev 0. Adiabatic Compression With Constant Bleed Valve Test Report # 30016558 Rev 0 Adiabatic Compression With Constant Bleed Valve Scope: This test report contains test data on the effects of adiabatic compression in nitrogen service on AP3600 diaphragm valves,

More information

Multiple Pressure Booster Systems With Variable Speed Controller Type BL

Multiple Pressure Booster Systems With Variable Speed Controller Type BL Multiple Pressure Booster Systems With Variable Speed Controller Type BL General Characteristics - Single or multistage pumps - Horizontal or vertical mounting - Total head 30m ~ 250m - Material construction:

More information

INSTRUCTION MANUAL STATION CONTROLLER SC100 MOTOR PROTECTION ELECTRONICS, INC.

INSTRUCTION MANUAL STATION CONTROLLER SC100 MOTOR PROTECTION ELECTRONICS, INC. INSTRUCTION MANUAL STATION CONTROLLER SC100 MOTOR PROTECTION ELECTRONICS, INC. 2464 Vulcan Road, Apopka, Florida 32703 Phone: (407) 299-3825 Fax: (407) 294-9435 Revision Date: 2-12-07 STATION CONTROLLER

More information

Master Meter Maintenance Manual

Master Meter Maintenance Manual Eastern Petroleum Supplies Ltd, New House Farm, Maldon Road, Steeple, Essex, CM0 7RR, UK Master Meter Maintenance Manual Tel + 44 (0) 1621 773292 Fax + 44 (0) 1621 772353 E-Mail sales@easternsupplies.co.uk

More information

Digital Vacuum Regulator

Digital Vacuum Regulator Temperature Control for Research and Industry Digital Vacuum Regulator User s Manual Model 300 INDEX SECTION PAGE 1. QUICK OPERATING INSTRUCTIONS........................... 3 Safety Notices.................................................

More information

Introductory Lab: Vacuum Methods

Introductory Lab: Vacuum Methods Introductory Lab: Vacuum Methods Experiments in Modern Physics (P451) In this lab you will become familiar with the various components of the lab vacuum system. There are many books on this topic one of

More information

Improving distillation tower operation

Improving distillation tower operation Improving distillation tower operation Measuring differential pressure across long sections of distillation columns has always been challenging, but purpose-built sensor systems provide a solution Fast

More information

Blue River Technologies Port-A-Poly Mixer w/2.5 GPH LMI Pump And Secondary Water Dilution Line INSTALLATION AND OPERATION

Blue River Technologies Port-A-Poly Mixer w/2.5 GPH LMI Pump And Secondary Water Dilution Line INSTALLATION AND OPERATION Blue River Technologies Port-A-Poly Mixer w/2.5 GPH LMI Pump And Secondary Water Dilution Line INSTALLATION AND OPERATION Install your Blue River Technologies Port-A-Poly mixing system in a clean dry area.

More information

Introduction. Part one: Identify the Hydraulic Trainer Components

Introduction. Part one: Identify the Hydraulic Trainer Components The University Of Jordan School of Engineering Mechatronics Engineering Department Fluid Power Engineering Lab Experiments No.4 Introduction to Hydraulic Trainer Objective: Students will be able to identify

More information

Exhibit 4. Determination of Static Pressure Performance of the Healy Clean Air Separator (Executive Orders VR-201-N and VR-202-N)

Exhibit 4. Determination of Static Pressure Performance of the Healy Clean Air Separator (Executive Orders VR-201-N and VR-202-N) 1 APPLICABILITY Exhibit 4 Determination of Static Pressure Performance of the Healy Clean Air Separator (Executive Orders VR-201-N and VR-202-N) Definitions common to all certification and test procedures

More information

Glove Box Installation Manual

Glove Box Installation Manual Glove Box Installation Manual 1998 by M. Braun Company File: GB-UNI-INS.DOC! Edition 08-00 by M. Boutin! Subject to be changed without notice Glovebox Installation Your Glove box has been fully assembled,

More information

IT STARTS AT THE SOURCE - RE-CALIBRATING YOUR PLANT METERS

IT STARTS AT THE SOURCE - RE-CALIBRATING YOUR PLANT METERS IT STARTS AT THE SOURCE - RE-CALIBRATING YOUR PLANT METERS NYS AWWA Spring Conference Saratoga Springs, New York April 25, 2017 Robert Lucas, P.E. WHAT ARE WE TALKING ABOUT? Types of Flow Measuring Devices

More information

Digital Level Control One and Two Loops Proportional and Integral Control Single-Loop and Cascade Control

Digital Level Control One and Two Loops Proportional and Integral Control Single-Loop and Cascade Control Digital Level Control One and Two Loops Proportional and Integral Control Single-Loop and Cascade Control Introduction This experiment offers a look into the broad field of process control. This area of

More information

GAS SUPPLY DESIGN GUIDE

GAS SUPPLY DESIGN GUIDE GAS SUPPLY DESIGN GUIDE Natural Gas, Propane Gas, or Dual Fuel Fired Modulating, Condensing Boilers BENCHMARK Series Gas-Fired Boilers For models: BMK750 to BMK6000 Last Update: 06/20/2014 PR1 06/20/14

More information

2. Determine how the mass transfer rate is affected by gas flow rate and liquid flow rate.

2. Determine how the mass transfer rate is affected by gas flow rate and liquid flow rate. Goals for Gas Absorption Experiment: 1. Evaluate the performance of packed gas-liquid absorption tower. 2. Determine how the mass transfer rate is affected by gas flow rate and liquid flow rate. 3. Consider

More information

Title: Standard Operating Procedure for R&R Environmental Devices Model MFC201 Gas Dilution Calibrator

Title: Standard Operating Procedure for R&R Environmental Devices Model MFC201 Gas Dilution Calibrator Procedure No: SOP-029 Revision No: 1.1 (December 29, 2010) Page No.: 1 of 7 1. INTRODUCTION AND SCOPE To obtain timely data for the purpose of air quality assessment, air quality trend reporting, air quality

More information

The Experts in Vacuum Solutions

The Experts in Vacuum Solutions By Woodrow Farrow - Reprinted with permission from Specialty Gas Report Vacuum: a space that is relatively empty of matter, especially when that void has been created through artificial means. The earth

More information

TECHNICAL DATA. than the water inlet pressure to the concentrate

TECHNICAL DATA. than the water inlet pressure to the concentrate Foam102a 1. DESCRIPTION The Viking Low Flow Foam/Water proportioning system, is a UL Listed and FM Approved system, for use with 3M foam concentrates. This system consists of a standard wet pipe sprinkler

More information

In Response to a Planned Power Outage: PPMS EverCool II Shut Down and Re-start Procedure

In Response to a Planned Power Outage: PPMS EverCool II Shut Down and Re-start Procedure PPMS Service Note 1099-412 In Response to a Planned Power Outage: PPMS EverCool II Shut Down and Re-start Procedure Introduction: Loss of electricity to the PPMS EverCool II should not cause damage to

More information

Title: Standard Operating Procedure for Elemental and Organic Carbon (EC and OC) using Non-Dispersive Infrared Detection (NDIR)

Title: Standard Operating Procedure for Elemental and Organic Carbon (EC and OC) using Non-Dispersive Infrared Detection (NDIR) Procedure No: SOP-025 Revision No: 1.0 (January 21, 2011) Page No.: 1 of 8 1. INTRODUCTION AND SCOPE To obtain timely data for the purpose of air quality assessment, air quality trend reporting and to

More information

GAS SUPPLY APPLICATION GUIDE

GAS SUPPLY APPLICATION GUIDE GAS SUPPLY APPLICATION GUIDE Natural Gas or Propane Modulating & Condensing Boilers and Water Heaters This document applies to the following models: Boilers AM 399B AM 500B AM 750B AM 1000B Gas-Fired Boilers

More information

product manual HM-4140, HM-4150, HM-4160 HM-4160A HM-4150 Humboldt FlexPanels

product manual HM-4140, HM-4150, HM-4160 HM-4160A HM-4150 Humboldt FlexPanels 12.09 product manual HM-4140, HM-4150, HM-4160 HM-4160A HM-4150 Humboldt FlexPanels Introduction: This manual covers the installation and operation of Humboldt FlexPanels for Triaxial and Permeability

More information

Fluid Machinery Introduction to the laboratory measurements

Fluid Machinery Introduction to the laboratory measurements Fluid Machinery Introduction to the laboratory measurements Csaba H s (csaba.hos@hds.bme.hu) Ferenc Hegedus (hegedusf@hds.bme.hu) February 21, 2014 1 Requirements related to the measurement part of the

More information

Model 130M Pneumatic Controller

Model 130M Pneumatic Controller Instruction MI 017-450 May 1978 Model 130M Pneumatic Controller Installation and Operation Manual Control Unit Controller Model 130M Controller is a pneumatic, shelf-mounted instrument with a separate

More information

Quick Installation Guide Doc nr.: C Date:

Quick Installation Guide Doc nr.: C Date: Quick Installation Guide Doc nr.: 9.17.093C Date: 13-05-2016 SCOPE OF THIS GUIDE mini CORI-FLOW instruments are highly accurate instruments for measuring and controlling the mass flow rate of liquids and/or

More information

Third measurement MEASUREMENT OF PRESSURE

Third measurement MEASUREMENT OF PRESSURE 1. Pressure gauges using liquids Third measurement MEASUREMENT OF PRESSURE U tube manometers are the simplest instruments to measure pressure with. In Fig.22 there can be seen three kinds of U tube manometers

More information

Installation, operating and maintenance Instructions for Seemag bypass level indicator

Installation, operating and maintenance Instructions for Seemag bypass level indicator Issue: S Date: 05-09-14 Type G35 General information The Seetru bypass magnetic level indicator, abbreviate SEEMAG, serves to show the filling level of fluids in tanks, basins, tubes etc. The Seemag operates

More information

Model PDT Dewpoint Transmitter

Model PDT Dewpoint Transmitter Model PDT Dewpoint Transmitter Instruction Manual Alpha Moisture Systems Alpha House 96 City Road Bradford BD8 8ES England Tel: +44 1274 733100 Fax: +44 1274 733200 email: mail@amsytems.co.uk web: www.amsystems.co.uk

More information

Copyright, 2005 GPM Hydraulic Consulting, Inc.

Copyright, 2005 GPM Hydraulic Consulting, Inc. Troubleshooting and Preventive Maintenance of Hydraulic Systems Learning to Read the Signs of Future System Failures Instructed by: Al Smiley & Alan Dellinger Copyright, 2005 GPM Hydraulic Consulting,

More information

icon i150 / i350 Installation / Operation Manual

icon i150 / i350 Installation / Operation Manual i150 Concentrator i350 Concentrator icon i150 / i350 Installation / Operation Manual www.iconcentrator.com What You Will Need to Install Your icon In order to install your icon you will have to consider

More information

1.2 Example 1: A simple hydraulic system

1.2 Example 1: A simple hydraulic system Note: It is possible to use more than one fluid in the Hydraulic library. This is important because you can model combined cooling and lubrication systems of a library. The hydraulic library assumes a

More information

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

DESIGN DATA A WET PIPE BLADDER TANK FOAM/WATER SYSTEM WITH HYDRAULICALLY ACTUATED DELUGE CONCENTRATE CONTROL VALVE February 9, 1998 Foam 101a A BLADDER TANK WITH 1. DESCRIPTION A Wet Pipe Bladder Tank Foam/Water System is a standard wet pipe automatic sprinkler system capable of discharging a foam/water solution automatically

More information

PNEUMATIC PRESSURE CONTROLLERS

PNEUMATIC PRESSURE CONTROLLERS PNEUMATIC PRESSURE CONTROLLERS VARIABLE VOLUME PRESSURE CONTROLLER MODELS: V-1 R AND V-2R The 3D Variable Volume Pressure Controller is available for requirements of 0-1,000 psi and 0-6,000 psi in absolute

More information

Technical Data Sheet MF010-O-LC

Technical Data Sheet MF010-O-LC Technical Data Sheet MF010-O-LC - 1 - 1. Properties The oxygen measuring system MF010-O-LC determines the oxygen content in gas mixtures up to a temperature of 250 C. It is particularly suitable for the

More information

ACCURATE PRESSURE MEASUREMENT FOR STEAM TURBINE PERFORMANCE TESTING

ACCURATE PRESSURE MEASUREMENT FOR STEAM TURBINE PERFORMANCE TESTING ACCURATE PRESSURE MEASUREMENT FOR STEAM TURBINE PERFORMANCE TESTING Blair Chalpin Charles A. Matthews Mechanical Design Engineer Product Support Manager Scanivalve Corp Scanivalve Corp Liberty Lake, WA

More information

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

Compiled by: B Beard. Approved by: SH Carstens. Description of requirements and procedures for compact provers to be used as verification standards. 1. Scope Description of requirements and procedures for compact provers to be used as verification standards. 2. Reference documents Trade Metrology Act SANS1698 3. Policy A. BASIC REQUIREMENTS Compact

More information