ANSI - CURVE BOOK CHEMICAL PROCESS PUMPS
|
|
|
- Cecil Knight
- 5 years ago
- Views:
Transcription
1 - CURVE BOOK CHEMICAL PROCESS PUMPS
2 WE HAVE ALL THE TICKS Version 1 - ANSI Curve Book: Rapid Allweiler Pumps Whilst all care has been taken to ensure the accuracy of the information contained in this Brochure was correct at the time of printing, please be advised we cannot be held responsible for any errors contained within and or changes that may have taken place. Dimensions contained within are for reference purpose only and should not be used for construction; certified drawings are available upon request. For confirmation of any information contained herewith please contact a member of our technical sales team.
3 TOMBSTONE CURVES 1 rpm Size* Pg. no. HEAD [m] x -1 1x 1-1/ 1 x 1-6 1/ 1 x / x 3-1 x 3-1/ 11/ x 3-6 x x -1 3 x -13 x x - 1 x 3-1 1/ x x - G 6 x -1 x 6-13 x FLOW RATE [m 3 /h] 6 x -13 x 1-1 G x 1-13 x rpm 1x1½-6 1x1½- 3 1½x ½x3-7 1½x ½x x-1 3 x x3-1 3 x x x-G x x x x x x x-1 x x1-1g x1-1 3 HEAD [m] / x 3-13 x x -1 1 x 1 1 /- 1 x 1 1 / / x / x 3-1 x / x 3- x x -1 3 x -G 3 x -7 x x x - BEST EFFICIENCY POINT SHOWN FLOW RATE [m 3 /h] 1
4 1 OCTOBER 1 ½ 1 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 33 1 x 1½ rpm % % % 6% % 9% 9.3% 9% % 6% % %
5 1 OCTOBER 1 ½ 1 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 33 1 x 1½ - 1 rpm % % % % 3%.6% 1 1 3% % %
6 1 OCTOBER 3 1½ Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 33 1½ x rpm 6. 6 % % % % % 6% 6.6% 6% % % %
7 OCTOBER 3 1½ Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 33 1½ x 3-1 rpm 16 1 % % % % 7%.% 1 7% 1 % % 6 % %
8 OCTOBER 3 1½ Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 1½ x rpm 1 1" % % % % 7% 9% 6.% 9% 7% % % 1 % % " ". 6
9 OCTOBER 3 1½ Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 1½ x rpm 3 1" % % % % 3 6.% % 1" 1 % 7% 6% " 1" " 1". 7
10 3 OCTOBER 1 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 1 x rpm 1 1" 3% 3% 37% % %.6% % % 37% 1 3% " ".
11 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 33 x rpm % % 6% 6% 67.3% 7 6 6% 6% %
12 1 16 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B.3 % % % % % ANSI 9 x 3-1 rpm 1 6.1% 1 % % 1 % 6 %
13 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 x rpm 1" % % 6% 61.7% 6% 1 % " " 11
14 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 x rpm 3 3 1" 6% 9% 61% 63% 63.% 63% 1" 61% 9% 6% 1 6% " 1" 3 1 1" 1" 1
15 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 3 x - G 1 rpm % % 63% 6% 71% 73% 7.% 73% 71% 6% 63% 6 % % %
16 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 3 x - 1 rpm % 6% 6% 7% 73% 7% 76% 76.% 76% 7% 73% 7% 6% 6 6%
17 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 3 x rpm 3 1" % % 6% 1 6% 6% 69% 7.% 69% 6% 6% 1 6% " ". 1
18 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 3 x rpm 3 1" % 6% 6% 7% 7% 73% 73.% 73% 3 7% 1" 7% " 1 1" 3 1 1" 1" 16
19 OCTOBER 6 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 x rpm 1" % 6% 6% 7% 9. 7% 76% 7% % 7% 76% 7% 1 7% " " 1 17
20 OCTOBER 6 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 x rpm 3 1" 6% 6% 7% 7% 7% 3 1 1".3% 7% 7% 7% 6% 6% " 1" 3 1 1" 1" 1
21 MARCH Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 7 6 x rpm 3 3 1" 1" % 6% 6% 7% 77% 79% % 1% 1% % 79% 77% 7% 7% 6% 6% Series " 1 1 1" 3, 3, 1" 1" 1, 19
22 6 MARCH Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 7 6 x rpm 1 % 6% 6%7% 7% 7% 1" % % % 3 1" % % % 7% 7% " 1" 1, 3, 1, 1" 1" 1
23 ½" 1" 11½" 1½" MARCH Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B % % 6% 6% 7% 7% 7% % % %6% 6% % % % 7% 7% ANSI 7 x rpm ½" 1½" 1" 11½" 1,, 3,, 1½" 1" 11½" 1½" 1, 1
24 MARCH Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 7 x 1-1G 1 rpm 1 6% 6% 7% 7% % % 6% % 1" % 6% 3 3 1" % % 7% 7% " 6 1" 3 1, 3, 1, 1" 1" 1
25 6 MARCH Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 7 x rpm 1 7% 7% 77% % 3 1½" 1" 13½" 1½" 3% % 7% % 3% % 77% ½" 1" 13½" 6 1½", 3, 1, 1½" 13½" 1" 1½" 1 3
26 3 3 OCTOBER 1½ 1 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B 6. 3% 3% % % % 3% ANSI 33 1 x 1½ rpm..% 3% % 1 " % 3. 1 % 3% " ". 6.
27 7 OCTOBER 1½ 1 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 33 1 x 1½ - 9 rpm 6 % % % 3% 6% % 9.% % 6% 3% % 3 %
28 OCTOBER 3 1½ Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 33 1½ x rpm " % % % 6% 63% 6% 66.% 6% 63% % 6% 1 % ". 3 1 ". 6. 6
29 7 OCTOBER 3 1½ Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 1½ x 3-9 rpm 6 % % % 9% 61.1% 9% % %
30 1 OCTOBER 3 1½ Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 1½ x rpm 1" 6 % % % 7% 9% 61% 61.6% 61% 9% 7% % % " "
31 16 OCTOBER 3 1½ Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 1½ x rpm 1 % % % % 1 1 1" 1" 6% %.6% % 6% % " 1" 6 1" 1" 9
32 1 OCTOBER 1 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 1 x rpm 1 1" % 3% 3% % 3% 6.7% 3% % " ". 3
33 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 33 x rpm % % % 6% 6% 67% 69% 7% 71.% 7% 69% 67% 6% 6% 1. " 1 % ". 6 "
34 7 6 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B.3 % % % % 61% 63% ANSI 9 x 3-9 rpm 63.7% 63% 61% % % 3 %
35 1 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 x rpm 1 6 1" % 6% 6% 6% 6.% 6% 6% 6% % " " 33
36 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 x rpm " 9% 61% 63% 6% 6% 66% 66.% 66% " 6% 6% 63% " 1" " 1" 3
37 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B ANSI 9 3 x - G 9 rpm % % 6% 6% 6% 66% 7% 7% 7.3% 7% 7% 66% 6% 6% 3 6%
38 7 OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B.3 ANSI 9 3 x - 9 rpm 6 6% 6% 7% 7% 7% 1% 3% 3.7% 3% 1% 7% 7% 3 7%
39 1 1" OCTOBER 3 Based on water density 1 kg/m3 and viscosity 1 cst. Head, capacity and efficiency according to ISO Standard : 1973 Annex B % 6% 6% 69% 71% 7% 7.% 7% 71% ANSI 9 3 x rpm 69% 6 6% 6% " " 37
40 Notes 3
41 Notes 39
42
43 BASIC FORMULAS H= Head(m) Q = Flow(m³/h) Eff = Pump Eff% Density = SG Capacity l/sec x 3.6 = m³/h Imp gpm x.71 = m³/h US gpm.6 = l/min 1 kg/hr = Head/Pressure Ft 3. = m Bar x 1 = kpa m x 9. = kpa m x.9 = Bar m x 1. = psi psi x 6.9 = kpa m³/h 3.6 = l/sec m³/h x.3 = Imp gpm l/min x.6 = US gpm 1m³h Density(SG) m x 3. = Ft kpa x.1 = m Bar x 1.19 = m Temperature Deg.C = (deg.f-3) x.6 Deg.F = (1. x deg.c) + 3 Peripheral Speed imp.dia.(mm) x π x N(Rpm) Peripheral Speed(Impeller) = 6 x 1 Viscosity vis Viscous Liquid w Water Given: Qvis in m³/h kinematic viscosity v in mm²/s Hvis in m pvis in kg/dm³ Qvis Qw = CQ Power Hw = Hvis CH hp x.76 = kw kw x 1.33 = hp Qw = C% x %w kw abs = Q x H x SG 367 x Eff(%) kw = Amps x Volts x Power Factor x RPM = Hz x 1 No of Poles Hz = RPM x No Of Poles 1 Velocity m/sec = Q x (Pipe Dia)² Qvis x Hvis x Pvis Pvis = 367 x Eff(%) vis Centrifugal and Axial Flow Pump Affinity Laws: Speed changes & impeller diameter remains the same: Q1/Q = N1/N H1/H = (N1/N)² P1/P = (N1/N)³ Efficiency EFF(%) = Q x H x SG 367 x kw(abs) Impeller diameter changes and speed remains the same: Q1/Q = D1/D H1/H = (D1/D)² P1/P = (D1/D)³
44 6 RAPID 1 Girder Street Isando 161 T: F:
n = Kinematic viscosity (cst) SG = specific gravity or 1 Poise = 100 cp 1 Stoke = 100 cst Q = capacity (m 3 /s) A = tube area (m 2 ) or
Fmulas Designation Fmula Comments Product Viscosity n = m r n = Kinematic viscosity (mm /s) m = Absolute viscosity (mpa.s) n = m SG n = Kinematic viscosity (cst) m = Absolute viscosity (cp) m = n SG 1
EVOTRON WET ROTOR ELECTRONIC CIRCULATORS TECHNICAL DATA APPLICATIONS ADVANTAGES
TECNICAL DATA EVOTRON Operating range: from, -, m3/h with head of up to metres. Pumped liquid temperature range: from - C to + C. Working pressure: bar ( kpa). Protection class: IP X. Insulation class:
LECTURE 6- ENERGY LOSSES IN HYDRAULIC SYSTEMS SELF EVALUATION QUESTIONS AND ANSWERS
LECTURE 6- ENERGY LOSSES IN HYDRAULIC SYSTEMS SELF EVALUATION QUESTIONS AND ANSWERS 1. What is the head loss ( in units of bars) across a 30mm wide open gate valve when oil ( SG=0.9) flow through at a
PUMP PERFORMANCE MEASUREMENTS Jacques Chaurette p. eng. April 2003
PUMP PERFORMANCE MEASUREMENTS Jacques Chaurette p. eng. www.lightmypump.com April 003 Synopsis This article examines how to take flow and pressure measurement and then calculate the total head of a pump
Chapter Four Hydraulic Machines
Contents 1- Introduction. - Pumps. Chapter Four Hydraulic Machines (لفرع الميكانيك العام فقط ( Turbines. -3 4- Cavitation in hydraulic machines. 5- Examples. 6- Problems; sheet No. 4 (Pumps) 7- Problems;
BACHELOR OF TECHNOLOGY IN MECHANICAL ENGINEERING (COMPUTER INTEGRATED MANUFACTURING)
No. of Printed Pages : 6 BME-028 BACHELOR OF TECHNOLOGY IN MECHANICAL ENGINEERING (COMPUTER INTEGRATED MANUFACTURING) Term-End Examination December, 2011 00792 BME-028 : FLUID MECHANICS Time : 3 hours
LES. Single-stage end-suction pumps Identification Type key
Contents Singlestage endsuction pumps Identification Type key Product data Introduction Applications Features and benefits Performance range pole pole 6 pole Construction Sectional drawing Construction
Chapter Four Hydraulic Machines
Contents 1- Introduction. 2- Pumps. Chapter Four Hydraulic Machines (لفرع الميكانيك العام فقط ( Turbines. -3 4- Cavitation in hydraulic machines. 5- Examples. 6- Problems; sheet No. 4 (Pumps) 7- Problems;
TOTAL HEAD, N.P.S.H. AND OTHER CALCULATION EXAMPLES Jacques Chaurette p. eng., June 2003
TOTAL HEAD, N.P.S.H. AND OTHER CALCULATION EXAMPLES Jacques Chaurette p. eng., www.lightmypump.com June 2003 Figure 1 Calculation example flow schematic. Situation Water at 150 F is to be pumped from a
PUMP SYSTEM ANALYSIS AND SIZING. BY JACQUES CHAURETTE p. eng.
PUMP SYSTEM ANALYSIS AND SIZING BY JACQUES CHAURETTE p. eng. 5 th Edition February 2003 Published by Fluide Design Inc. www.fluidedesign.com Copyright 1994 I TABLE OF CONTENTS Introduction Symbols Chapter
K DOUBLE-IMPELLER DOUBLE-IMPELLER ELECTRIC PUMPS
K DOUBLE-IMPELLER DOUBLE-IMPELLER ELECTRIC PUMPS ENERGY EFFICIENCY 7.5 TECHNICL DT Operating range: from,2 to 3 m 3 /h with head up to 97 metres. Pumped liquid: clean, free of solids and abrasives, non-viscous,
FE Fluids Review March 23, 2012 Steve Burian (Civil & Environmental Engineering)
Topic: Fluid Properties 1. If 6 m 3 of oil weighs 47 kn, calculate its specific weight, density, and specific gravity. 2. 10.0 L of an incompressible liquid exert a force of 20 N at the earth s surface.
FE Exam Fluids Review October 23, Important Concepts
FE Exam Fluids Review October 3, 013 mportant Concepts Density, specific volume, specific weight, specific gravity (Water 1000 kg/m^3, Air 1. kg/m^3) Meaning & Symbols? Stress, Pressure, Viscosity; Meaning
P U M P S. The quality standard for hydraulic efficiency and suction lift. PERIPHERAL PUMPS TEP/ TSP - SERIES 50Hz
P U M P S THE BENCHMARK FOR PERFORMANCE The quality standard for hydraulic efficiency and suction lift. PERIPHERAL PUMPS TEP/ TSP - SERIES 5Hz I N D E X TEP / TSP SERIES - PERIPHERAL PUMPS Page No. General
CHAPTER EIGHT P U M P I N G O F L I Q U I D S
CHAPTER EIGHT P U M P I N G O F L I Q U I D S Pupmps are devices for supplying energy or head to a flowing liquid in order to overcome head losses due to friction and also if necessary, to raise liquid
P U M P S. The quality standard for hydraulic efficiency and suction lift. PERIPHERAL PUMPS TEP/ TSP - SERIES 50Hz
P U M P S THE BENCHMARK FOR PERFORMANCE The quality standard for hydraulic efficiency and suction lift. PERIPHERAL PUMPS TEP/ TSP - SERIES 5Hz I N D E X TEP / TSP / TRP SERIES - PERIPHERAL PUMPS Page
Northern Lesson 2 Gear Pump Terminology. Gear Pump 101. Lesson 2: Gear Pump Terminology. When your reputation depends on it!
Gear Pump 101 Lesson 2: Gear Pump Terminology When your reputation depends on it! Symbol Term Metric Unit Abbreviation US Customary Unit Abbreviation Conversion factor a A Area square millimeter mm2 square
Signature: (Note that unsigned exams will be given a score of zero.)
Neatly print your name: Signature: (Note that unsigned exams will be given a score of zero.) Circle your lecture section (-1 point if not circled, or circled incorrectly): Prof. Dabiri Prof. Wassgren Prof.
Calculation of Pipe Friction Loss
Doc.No. 6122-F3T071 rev.2 Calculation of Pipe Friction Loss Engineering Management Group Development Planning Department Standard Pump Business Division EBARA corporation October 16th, 2013 1 / 33 2 /
ELECTRONIC WET ROTOR CIRCULATORS
ELECTRONIC WET ROTOR CIRCULTORS Technical Sheet ELECTRONIC CIRCULTORS FOR ETING ND IR CONDITIONING SYSTEMS Energ ia e y GENERL DT compliant with the 3 and european directive ErP 9//EC (ex EuP) pplications
Thermal & Fluids PE Exam Technical Study Guide Errata
Thermal & Fluids PE Exam Technical Study Guide Errata This product has been updated to incorporate all changes shown in the comments on the webpage and email comments as of October, 30 2017. If you have
CHAPTER 12 Turbomachinery
CAER urbomachinery Chapter / urbomachinery 800 / 0 8 8 rad /s, u r 8 8 0 0 m /s, u r 8 8 0 0 8 m /s, rbv, but V u since, n n 0 0 0 0 0 0 m / s V V 0 0 m /s, rb 0 0 0 Vn u 0 8 6 77 m /s, tan tan 0 n t V
ELECTRONIC WET ROTOR CIRCULATORS
ELECTRONIC WET ROTOR CIRCULATORS TECNICAL DATA EVOTRON WET ROTOR ELECTRONIC CIRCULATORS Operating range: from, -, m/h with head of up to metres. Pumped liquid temperature range: from -1 C to +11 C. Working
Worksheet for Sizing Engine Cranking Batteries X/H - Type FNC Batteries. Information Required to Size Batteries for Engine Cranking:
Worksheet for Sizing Engine Cranking Batteries X/H - Type FNC Batteries Information Required to Size Batteries for Engine Cranking: Date: Customer Reference: 1 Engine Make 2 Engine Model 3 Engine Displacement
MULTISTAGE CENTRIFUGAL PUMP TPH 2/4/8/12/25/50T. 50Hz. WALRUS PUMP ISO 9001 Certified
MULTISTAGE CENTRIFUGAL PUMP TPH /////T Hz WALRUS PUMP ISO Certified TPH Applications The WALRUS TPH Series is horizontal multistage centrifugal pump, suitable for clean water/liquid without abrasive matters.
60 Hz. e-nsc Series HORIZONTAL CENTRIFUGAL ELECTRIC PUMPS EQUIPPED WITH IE3 MOTORS
6 Hz e-nsc Series HORIZONTAL CENTRIFUGAL ELECTRIC PUMPS EQUIPPED WITH IE3 MOTORS Cod. 19112831 Rev. B Ed.7/217 Xylect TM Xylect TM is a pump solution software with an extensive online database of product
FLUID MECHANICS D203 SAE SOLUTIONS TUTORIAL 2 APPLICATIONS OF BERNOULLI SELF ASSESSMENT EXERCISE 1
FLUID MECHANICS D203 SAE SOLUTIONS TUTORIAL 2 APPLICATIONS OF BERNOULLI SELF ASSESSMENT EXERCISE 1 1. A pipe 100 mm bore diameter carries oil of density 900 kg/m3 at a rate of 4 kg/s. The pipe reduces
CVE 372 HYDROMECHANICS EXERCISE PROBLEMS
VE 37 HYDROMEHNIS EXERISE PROLEMS 1. pump that has the characteristic curve shown in the accompanying graph is to be installed in the system shown. What will be the discharge of water in the system? Take
INTERNATIONAL STANDARD
INTERNATIONAL STANDARD ISO 8426 Second edition 2008-02-01 Hydraulic fluid power Positive displacement pumps and motors Determination of derived capacity Transmissions hydrauliques Pompes et moteurs volumétriques
Prima range. Alifter range. magnetical driven pumps in thermoplastic materials TMP TMA. centrifugal. self-priming
Prima range TMP centrifugal Alifter range magnetical driven pumps in thermoplastic materials TMA self-priming Prima - Alifter In this catalog Argal proposes the range of PRIMA pumps, magnetical driven,
High Pressure fi lters. FHB series. Maximum working pressure up to 32 MPa (320 bar) - Flow rate up to 485 l/min
High Pressure fi lters FHB series Maximum working pressure up to MPa (0 bar) - Flow rate up to 8 l/min High Pressure fi lters Introduction FILTER SIZING INDEX CALCULATION CORRECTIVE FACTOR Page Introduction
NKVE VERTICAL AXIS MULTISTAGE CENTRIFUGAL PUMPS WITH MCE/P INVERTER
NKVE 1-1--3--6-9 VERTICAL AIS MULTISTAGE CENTRIFUGAL PUMPS WIT MCE/P INVERTER TECNICAL DATA Operating range: fro to 118 3 /h with head up to 31 etres. Puped liquid: clean, free of solids and abrasives,
Centrifugal Machines Table of Contents
NLNG Course 017 Table of Contents 1 Introduction and Basic Principles... 1.1 Hydraulic Machines... 1.... 1.3 Pump Geometry... 1.4 Pump Blade Geometry...3 1.5 Diffusers...5 1.6 Pump Losses...6 1.7 Example
CMA - B - C - D - CMR
Cast iron self-priming electric pumps. APPLICATIONS Pressure boosting domestic plants Small-scale irrigation Moving non-aggressive liquids for civil and industrial use Washing plants Washing vehicles CMA-B-C-D
Fachgesprach 12. HVAC Pumps. For Project Managers
Fachgesprach 12 HVAC Pumps For Project Managers WTF Philosophy: If you don t remember a certain formula, it's OK - you can always GoogleTheS h i t. But bad engineering CONCEPTS can hurt you. WTF Institute
Fast and Ultimate Vibration Field Solution: From Problem Detection to Field Performance Validation
Fast and Ultimate Vibration Field Solution: From Problem Detection to Field Performance Validation Giancarlo CICATELLI Flowserve - Italy Bruno SCHIAVELLO Flowserve Corporation - USA First Middle East Turbomachinery
Name Class Date. Section: Measurements and Calculations in Chemistry
Skills Worksheet Concept Review Section: Measurements and Calculations in Chemistry Answer the following questions in the space provided. 1. What is the difference between accuracy and precision? 2. Suppose
SVH with HYDROVAR (HVL range)
SVH with HYDROVAR (HVL range) SVH-HVL Rev. B Ed.9/1 (EN) SVH SERIES (e-sv WITH HYDROVAR) Background and context For all pumping needs in commercial or residential building and in industry applications,
TPH Series 50Hz Multi-stage Centrifugal Pump
WLRUS PUMP T Series Hz Multistage Centrifugal Pump ll specifications are subject to change without notice. 9 T Product data pplications Page Standard mode Page Operation conditions Page Pump construction
Campus Mail Box. Circle One: Richards 03 Richards 04 Lui 05 Lui - 06
ES 202 - Exam I Winter 2002-2003 Richards/Lui Name: Campus Mail Box Circle One: Richards 03 Richards 04 Lui 05 Lui - 06 Problem 1 Problem 2 ( 10 ) ( 45 ) Problem 3 ( 45 ) TOTAL ( 100 ) General Comments
Contents. Identification LHC. Horizontal split case pumps. Type key. Identification Type key
Contents dentification Type key Product data ntroduction Applications Features and benefits Performance range pole pole pole Construction Sectional drawing Construction features Test pressure Operating
Contents. Performance Curves/Technical Data. General Data Performance Range Sectional Drawing TPH 2T TPH 4T TPH 8T TPH 12T TPH 25T TPH 50T
Contents General Data Performance Range Sectional Drawing Performance Curves/Technical Data T T T T T 8T T T T T T T 7 9 T Series Multistage Centrifugal Pump Hz Power:.. kw Head: Up to 7M Flow: Up to L/min
Department of Energy Fundamentals Handbook. THERMODYNAMICS, HEAT TRANSFER, AND FLUID FLOW, Module 3 Fluid Flow
Department of Energy Fundamentals Handbook THERMODYNAMICS, HEAT TRANSFER, AND FLUID FLOW, Module 3 REFERENCES REFERENCES Streeter, Victor L., Fluid Mechanics, 5th Edition, McGraw-Hill, New York, ISBN 07-062191-9.
High Pressure fi lters. FHA 051 series. Maximum working pressure up to 56 MPa (560 bar) - Flow rate up to 140 l/min. High Pressure fi lters
High Pressure fi lters FHA 0 series Maximum working pressure up to 6 MPa (60 bar) Flow rate up to 0 l/min 99 High Pressure fi lters Introduction FILTER SIZG DEX CALCULATION CORRECTIVE FACTOR Page Introduction
TPH. 60Hz. Standard mode TPH 4T 2K. Code TPH 4T 2K S F A H
C US NSF/ANSI TPH Applications: The TPH Series are modernly designed with quiet and high efficient operation pumps, suitable for dependable water transfer, circulating or booster service. -Industrial circulation
ELECTRONIC CIRCULATORS FOR HEATING AND COOLING SYSTEMS. ErP. eady
ELECTRONIC CIRCULATORS OR EATING AND COOLING SYSTEMS ErP eady TECNICAL DATA EVOSTA 2 WET ROTOR ELECTRONIC CIRCULATORS Operating range:,-3,6 m 3 /h with head up to 6,9 metres. Pumped liquid temperature
NEBB Fundamental Formulas
Approved NEBB - May 1, 17 Page 1 of 8 Version 1.3 A = Area (ft²) IP, (m²) SI M = Mass (lb) IP, (kg) SI ACH = Air Changes per Hour ma = Mixed Air Ak = Effective Area m = meter (metre) AV = Average m³/s
Fluid Dynamics Midterm Exam #2 November 10, 2008, 7:00-8:40 pm in CE 110
CVEN 311-501 Fluid Dynamics Midterm Exam #2 November 10, 2008, 7:00-8:40 pm in CE 110 Name: UIN: Instructions: Fill in your name and UIN in the space above. There should be 11 pages including this one.
Lecture (20) DC Machine Examples Start of Synchronous Machines
Lecture (20) DC Machine Examples Start of Synchronous Machines Energy Systems Research Laboratory, FIU All rights reserved. 20-1 Energy Systems Research Laboratory, FIU All rights reserved. 20-2 Ra R f
Working pressure. 320 bar. Style T. Style D. Style S. Style B B B D.I. D.I. D.I. D.I.
8 FB SERIES FB Working pressure 0 bar Style S Style B Style T Style D B B B B D.I. D.I. D.I. D.I. A A A A 8 Technical data Filter body (Materials) ead: Cast iron (chemical heat treatment) ousing: Steel
PIPING SYSTEMS. Pipe and Tubing Standards Sizes for pipes and tubes are standardized. Pipes are specified by a nominal diameter and a schedule number.
PIPING SYSTEMS In this chapter we will review some of the basic concepts associated with piping systems. Topics that will be considered in this chapter are - Pipe and tubing standards - Effective and hydraulic
Signature: (Note that unsigned exams will be given a score of zero.)
Neatly print your name: Signature: (Note that unsigned exams will be given a score of zero.) Circle your lecture section (-1 point if not circled, or circled incorrectly): Prof. Dabiri Prof. Wassgren Prof.
Lecture 4. Lab this week: Cartridge valves Flow divider Properties of Hydraulic Fluids. Lab 8 Sequencing circuit Lab 9 Flow divider
91 Lecture 4 Lab this week: Lab 8 Sequencing circuit Lab 9 Flow divider Cartridge valves Flow divider Properties of Hydraulic Fluids Viscosity friction and leakage Bulk modulus Inertance Cartridge Valves
Pipe Flow Design 1. Results Data
Pipe Flow Design 1 Results Data Color of Pipe: Velocity in m/sec 1.9 2.2 2.4 2.7 2.9 3.2 Pipe Flow Expert Results Key f = flow in Modelling a 'Tee' fitting: The flow rate through the 'Tee' w ill be different
Brueninghaus Hydromatik Rexroth A4VSG Pump
Brueninghaus Hydromatik Rexroth A4VSG Pump Pump model A4VSG71 A4VSG125 A4VSG180 A4VSG250 A4VSG355 A4VSG500 A4VSG750 A4VSG1000 www.hydpump.com Closed circuit variable hydraulic piston A4VG pump Axial piston,
Basic Math Concepts for Water and Wastewater Operators. Daniel B. Stephens & Associates, Inc.
Basic Math Concepts for Water and Wastewater Operators Topics Hierarchy of operations Manipulating equations Unit/dimensional analysis and conversion factors Electricity Temperature Geometry Flow hydraulics
Lecture 3: Electrical Power and Energy
Lecture 3: Electrical Power and Energy Recall from Lecture 2 E (V) I R E Voltage Similar to water pressure Unit: Volts (V) I Current Similar to water flow Unit: Amperes (A) R Resistance Similar to water
BME-A PREVIOUS YEAR QUESTIONS
BME-A PREVIOUS YEAR QUESTIONS CREDITS CHANGE ACCHA HAI TEAM UNIT-1 Introduction: Introduction to Thermodynamics, Concepts of systems, control volume, state, properties, equilibrium, quasi-static process,
Fluid Dynamics Exam #1: Introduction, fluid statics, and the Bernoulli equation March 2, 2016, 7:00 p.m. 8:40 p.m. in CE 118
CVEN 311-501 (Socolofsky) Fluid Dynamics Exam #1: Introduction, fluid statics, and the Bernoulli equation March 2, 2016, 7:00 p.m. 8:40 p.m. in CE 118 Name: : UIN: : Instructions: Fill in your name and
M E 320 Professor John M. Cimbala Lecture 23
M E 320 Professor John M. Cimbala Lecture 23 Today, we will: Discuss diffusers and do an example problem Begin discussing pumps, and how they are analyzed in pipe flow systems D. Diffusers 1. Introduction.
MRH. Return Filters RETURN FILTER
MRH Return ilters RETUR ILTER Return ilters MRH MRH MPa (0 bar) Port sizes: / / low rates:.00 l/min TECHICAL ATA Max. working pressure: MPa (0 bar) Max. test pressure: MPa ( bar) ursting pressure: 6 MPa
Problem 1.6 Make a guess at the order of magnitude of the mass (e.g., 0.01, 0.1, 1.0, 10, 100, or 1000 lbm or kg) of standard air that is in a room 10
Problem 1.6 Make a guess at the order of magnitude of the mass (e.g., 0.01, 0.1, 1.0, 10, 100, or 1000 lbm or kg) of standard air that is in a room 10 ft by 10 ft by 8 ft, and then compute this mass in
MOTOR WIRING DATA From National Electrical Code 3 PHASE SQUIRREL CAGE INDUCTION MOTORS 230 Volt 460 Volt Min. # Max. Rating
MOTOR WIRING DATA From National Electrical Code PHASE SQUIRREL CAGE INDUCTION MOTORS 20 Volt 0 Volt Min. # Max. Rating Min. Size Size of Full Size Wire Conduit Branch Circuit Load Wire AWG (inches) Fuses
S.E. (Mech.) (First Sem.) EXAMINATION, (Common to Mech/Sandwich) FLUID MECHANICS (2008 PATTERN) Time : Three Hours Maximum Marks : 100
Total No. of Questions 12] [Total No. of Printed Pages 8 Seat No. [4262]-113 S.E. (Mech.) (First Sem.) EXAMINATION, 2012 (Common to Mech/Sandwich) FLUID MECHANICS (2008 PATTERN) Time : Three Hours Maximum
SINGLE IMPELLER CENTRIFUGAL ELECTRIC PUMPS in cast iron
Cast iron self-priming electric pumps. APPLICATIONS Pressure boosting domestic plants Small-scale irrigation Moving non-aggressive liquids for civil and industrial use Washing plants Washing vehicles CMA-B-C-D
TIMING PULLEYS & BELTS Timing Belts and Pulleys
Timing Belts and Pulleys Z e d o1 F U1 v n1 d k1 z 1 a = Centre distance (mm) M B = Acceleration torque (Nm) t B = Acceleration time (s) d = Bore (mm) r = Density (kg/dm 3 ) M = Torque (Nm) n = RPM d k
CE Final Exam. December 12, Name. Student I.D.
CE 100 - December 12, 2009 Name Student I.D. This exam is closed book. You are allowed three sheets of paper (8.5 x 11, both sides) of your own notes. You will be given three hours to complete four problems.
Laboratory work No 2: Calibration of Orifice Flow Meter
Laboratory work No : Calibration of Orifice Flow Meter 1. Objective Calibrate the orifice flow meter and draw the graphs p = f 1 (Q) and C d = f (Re ).. Necessary equipment 1. Orifice flow meter. Measuring
DOMESTIC HOT WATER PUMPS WITH FIXED-SPEED MOTOR, 3x400V AP-, AKP- and AEP- series, threaded G1/2 G1 ¼ LOREM IPSUM JE ZULT MAAR 60 HZ.
LOREM IPSUM JE ZULT MAAR HZ m Head m/s m/s m/s m/s m/s Ø m Ø Ø Ø Ø l/s Flow kw Shaft power P Ø m/h Ø 9 Ø Ø kw 9 Total input power P Ø DOMESTIC HOT WATER PUMPS WITH FIXED-SPEED MOTOR, xv AP-, AKP- and AEP-
APPENDIX A USEFUL EQUATIONS (METRIC AND IMPERIAL SYSTEMS) THE DEFINITION OF VISCOSITY RHEOLOGICAL (VISCOUS BEHAVIOR) PROPERTIES OF FLUIDS
APPENDIX A USEFUL EQUATIONS (METRIC AND IMPERIAL SYSTEMS) THE DEFINITION OF VISCOSITY RHEOLOGICAL (VISCOUS BEHAVIOR) PROPERTIES OF FLUIDS A APPENDIX A APPENDIX A Flow vs. velocity Specific gravity vs.
e-sh Series Lenntech 60 Hz Tel Fax
Hz e-sh Series HORIZONTAL CENTRIFUGAL ELECTRIC PUMPS ACCORDING TO EN 733 MADE IN AISI 31 STAINLESS STEEL AND EQUIPPED WITH IE3 MOTORS Lenntech info@lenntech.com Tel. +31-1-1-9 www.lenntech.com Fax. +31-1-1-89
Exam #1. A. Answer any 1 of the following 2 questions. CEE 371 October 8, Please grade the following questions: 1 or 2
CEE 37 October 8, 009 Exam # Closed Book, one sheet of notes allowed Please answer one question from the first two, one from the second two and one from the last three. The total potential number of points
Chemical Engineering 374
Chemical Engineering 374 Fluid Mechanics Pump Scaling 1 Spiritual Thought 2 How the Atonement was wrought, we do not know. No mortal watched as evil turned away and hid in shame before the light of that
Design of Monoblock Centrifugal Pump Impeller
Design of Monoblock Centrifugal Pump Impeller Authors Mr. Chetan Kallappa Tambake 1, Prof. P. V. Salunke 1 Department of Mechanical Engineering, Walchand Institute of Technology, Ashok Chowk, Solapur-413006,
Air Cooler Industry AC-LN 1-7 / ACA-LN 2-7 / ACAF-LN 2-7
ir ooler Industry -LN -7 / -LN -7 / F-LN -7 Symbol General The -LN -7 air cooler series can be used in all areas where either oil or water-glycol is to be cooled with air. The coolers with an axial fan
Wake Frequency Calculations Solid Drilled Thermowells
Technical Description TD/TP 002 Issue 1 Wake Frequency Calculations Solid Drilled Thermowells What is a thermowell? A thermowell is a pressure-tight receptacle that protrudes into a pressure vessel. What
50 Hz n= 2900 rpm. Standardised EN 733 centrifugal pumps INSTALLATION AND USE. PERFORMANCE RANGE Flow rate up to 6000 l/min (360 m³/h) Head up to 98 m
F Standardised EN 733 centrifugal pumps Hz n= 9 rpm Clean water Industrial use PERFORMNCE RNGE Flow rate up to (3 ) Head up to 9 m PPLICTION LIMITS Manometric suction lift up to 7 m Liquid temperature
High Pressure fi lters. FHB series. Maximum pressure up to 320 bar - Flow rate up to 485 l/min. High Pressure fi lters
High Pressure fi lters FHB series Maximum pressure up to 0 bar - Flow rate up to 8 l/min 8 High Pressure fi lters FILTER SIZING The correct filter sizing have to be based on the variable pressure drop
EVO Product SAE Flange Chart
Permco is proud to introduce a new line of vane products; you will find our EVO vane line to be both versatile and ruggedly built for the toughest of applications. The EVO line comes in (3) series, PT6,
RFM. 300 kpa (3 bar) Return Filters RFM. Ports: 3/8 2 1/2 Flow rates: l/min
Return Filters RFM RFM kpa (3 bar) Ports: 3/ 2 1/2 Flow rates: 0 l/min ECHNICAL DAA Max. working pressure: kpa (3 bar) Max. test pressure: 00 kpa ( bar) Bursting pressure: 1 MPa (10 bar) Fatigue test:
Figure 3: Problem 7. (a) 0.9 m (b) 1.8 m (c) 2.7 m (d) 3.6 m
1. For the manometer shown in figure 1, if the absolute pressure at point A is 1.013 10 5 Pa, the absolute pressure at point B is (ρ water =10 3 kg/m 3, ρ Hg =13.56 10 3 kg/m 3, ρ oil = 800kg/m 3 ): (a)
Maximum pressure 420 bar Flow rate to 152 l/min. 560 bar. 140 l/min. Flow rate l/min FMM 050 1/2 1,50 3/4 1,00. Δp bar 0,50 0,00 FHA 051 1,50 1,00
FMM 00 Maximum pressure 0 bar Flow rate to l/min FHA 0 Maximum pressure 60 bar Flow rate to 0 l/min Technical data FMM 00 Filter housing (Materials) Head: Cast iron (chemical heat treatment) Housing: Steel
Return fi lters. MPI series. Maximum working pressure up to 1 MPa (10 bar) - Flow rate up to 3000 l/min
Return fi lters series Maximum working pressure up to MPa (0 bar) Flow rate up to 000 l/min 0 Return fi lters Introduction FILTER SIZING INDEX CALCULATION CORRECTIVE FACTOR Page Introduction Calculation
The FLUX F 430 with mechanical seal
The FLUX F 0 with mechanical seal Flexible coupling between motor and pump The pump must be used with many varying liquids, consequently the smallest residual left within the pump is unacceptable. You
Exam #2: Fluid Kinematics and Conservation Laws April 13, 2016, 7:00 p.m. 8:40 p.m. in CE 118
CVEN 311-501 (Socolofsky) Fluid Dynamics Exam #2: Fluid Kinematics and Conservation Laws April 13, 2016, 7:00 p.m. 8:40 p.m. in CE 118 Name: : UIN: : Instructions: Fill in your name and UIN in the space
High Pressure fi lters. FHM series. Maximum pressure up to 320 bar - Flow rate up to 450 l/min. High Pressure fi lters
High Pressure fi lters FHM series Maximum pressure up to 0 bar - Flow rate up to 0 l/min 67 High Pressure fi lters FILTER SIZING The correct filter sizing have to be based on the variable pressure drop
Suction fi lters. SF series. Flow rate up to 160 l/min. Suction fi lters
Suction fi lters SF 00 series Flow rate up to 60 l/min Suction fi lters FILTER SIZING The correct filter sizing have to be based on the variable pressure drop depending by the application. For example,
E 094 E 103 E 143. Tank top mounting Connection up to G1 Nominal flow rate up to 135 l/min e
R e t u r n F i l t e rs E 094 E 103 E 143 Tank top mounting Connection up to G1 Nominal flow rate up to 135 l/min 20.30-5e D e s c r i p t i o n Application In the return line circuits of hydraulic systems.
Chapter (6) Energy Equation and Its Applications
Chapter (6) Energy Equation and Its Applications Bernoulli Equation Bernoulli equation is one of the most useful equations in fluid mechanics and hydraulics. And it s a statement of the principle of conservation
Polígono Indutrial O Rebullón s/n Mos - España -
FB 8 Polígono Indutrial O Rebullón s/n. 646 - Mos - España - rodavigo@rodavigo.com SERIES FB Working pressure 0 bar Style S Style B Style T Style D B B B B D.I. D.I. D.I. D.I. A A A A 8 Polígono Indutrial
Estimation of Power Consumption by Centrifugal Pump with Reduced Impeller Size
Estimation of Power Consumption by Centrifugal Pump with Reduced Impeller Size Somchart Chantasiriwan Faculty of Engineering, Thammasat University, Pathum Thani 111, Thailand Correspondence: Somchart Chantasiriwan
High Pressure fi lters. FMP 039 series. Maximum pressure up to 110 bar - Flow rate up to 80 l/min. High Pressure fi lters
High Pressure fi lters FMP 09 series Maximum pressure up to 0 bar Flow rate up to 80 l/min 7 High Pressure fi lters FILTER SIZING The correct filter sizing have to be based on the variable pressure drop
Suction fi lters. MPA - MPM series. Flow rate up to 875 l/min. Suction fi lters
Suction fi lters & MPA MPM series Flow rate up to 87 l/min 7 Suction fi lters FILTER SIZING The correct filter sizing have to be based on the variable pressure drop depending by the application. For example,
e-mp Series MPA, MPR, MPD, MPV Lenntech 50 Hz Tel Fax
Hz e-mp Series MPA, MPR, MPD, MPV HIGH PRESSURE MULTISTAGE PUMPS ACCORDING TO ISO 199 Lenntech info@lenntech.com Tel. +31-1-1-9 www.lenntech.com Fax. +31-1-1-9 Cod. 1911 Rev. A Ed.3/17 Xylect TM Xylect
Direct-operated 2/2-way solenoid valves Type EV210B
Data sheet Direct-operated 2/2-way solenoid valves Type EV20B EV20B covers a wide range of direct-operated 2/2-way solenoid valves for universal use. EV20B is a very robust valve program with high performance
ESTIMATING PRODUCTION AND BOOSTER PUMP LOCATION FOR LONG DISTANCE PUMPING
ESTIMATING PRODUCTION AND BOOSTER PUMP LOCATION FOR LONG DISTANCE PUMPING R.E. Randall, Director Center for Dredging Studies Texas A&M University 1WEDA33/TAMU44 Acknowledgements Co author Po hung Yeh Graduate
Middle East Technical University Department of Mechanical Engineering ME 305 Fluid Mechanics I Fall 2018 Section 4 (Dr.
Middle East Technical University Department of Mechanical Engineering ME 305 Fluid Mechanics I Fall 2018 Section 4 (Dr. Sert) Study Set 7 Reading Assignment R1. Read the section Common Dimensionless Groups
3 Energy Exchange in Turbomachines
3 Energy Exchange in Turbomachines Problem 1 The solved and unsolved examples of this chapter are meant to illustrate the various forms of velocity triangles and the variety of the turbomachines. In addition,
TECHNICAL INFORMATION Bulletin
Peerless Pump Company 005 Dr..L. King Jr. Street, P.O. Box 706, Indianapolis, IN 4607-706, USA Telephone: (17) 95-9661 Fax: (17) 94-78 www.peerlesspump.com www.epumpdoctor.com TECHNICAL INFORATION Bulletin
EFFECT OF PIPE ROUTING ON TURBINE FLOW METER READINGS AND SUBSEQUENT DISCREPANCIES IN CONDENSATE LOADING AT BANGORA GAS FIELD
International Journal of Chemical & Petrochemical Technology (IJCPT) ISSN 77-4807 Vol., Issue, Jun 01, 41-54 TJPRC Pvt. Ltd. EFFECT OF PIPE ROUTING ON TURBINE FLOW METER READINGS AND SUBSEQUENT DISCREPANCIES