ANSI/HI Pump Standards, Version 3.1: Master Index for Complete Set

66 Pages·2015·0.46 MB·English

Master Index
for Complete Set:
ANSI/HI Pump Standards,
Version 4.0
This page intentionally blank.
HI Master Index for Complete Set: Version 4.0

ANSI/HI Pump Standards
:
Version 4.0

Master Index for Complete Set

This index is not part of any standard, but is presented to help the user in considering factors beyond the standards.
Note: Bold numbers indicate the standard number, nonbold numbers indicate the page number;
an f. indicates a figure, a t. indicates a table.

"Information completed by" categorization, 50.7: 13 getting started with, 50.7: 23
See also R/D/S field designations, Work process namespaces, 50.7: 26, 30
designations prerequisites and tools, 50.7: 23
"U" value, 9.6.8: 11 structural design, 50.7: 24, 25 f.
scores, 9.6.8: 15 subject type, 50.7: 25, 27 f., 29
Abbreviations and definitions, 50.7: 28 testing conformance to, 50.7: 21
Abrasion–corrosion, defined, 12.1-12.6: 43 use of namespaces, 50.7: 26, 27f., 30
Abrasive fluids and residual mechanical unbalance of versions and revisions system, 50.7: 25
rotating parts, 9.6.4: 17 where to find, 50.7: 23
Abrasive handling capabilities, 3.1-3.5: 2 Affinity rules, 1.3: 69
Abrasive wear, defined, 12.1-12.6: 43 Air core vortex, defined, 9.8: 48
Absolute pressure (p ), 3.6: 3 Air entrainment, 4.1-4.6: 15, 22
a
defined, 3.1-3.5: 19 Air gap, defined, 4.1-4.6: 8, 5.1-5.6: 16
Accelerating Deployment of ISO 15926 project, 50.7: 3 Airborne sound instrumentation
Acceleration head, 6.1-6.5: 31–34, 8.1-8.5: 14 acoustical calibration, 9.1-9.5: 28
Acceleration pressure, 6.1-6.5: 31–34, 7.8: 6, 8.1-8.5: octave-band analyzer, 9.1-9.5: 28
14 recorders, 9.1-9.5: 28
defined, 7.8: 3 sound-level meter and microphone system, 9.1-9.5: 28
Accelerometers, 9.6.9: 12 Airborne sound level test report, 9.1-9.5: 41 f.
Acceptance level Airborne sound readings
Accuracy and performance, defined, 7.8: 3 averaging, 9.1-9.5: 40
Accuracy, 9.6.9: 27 corrections for background noise, 9.1-9.5: 39 t.
defined, 9.6.5: 55 corrections, 9.1-9.5: 39
Acidity, of water, 2.3: 79 Air-operated bellows pumps, 10.1-10.5: 1, 2 f.
Acoustic sensors, in bearing wear monitoring, 9.6.5: 21 bellows selection and materials, 10.1-10.5: 13
Active storage, defined, 9.8: 48 features, 10.1-10.5: 12
Actuating mechanism. See Valve gear handling of harsh chemicals, 10.1-10.5: 12
Adapters, 2.3: 64 handling of hot liquids, 10.1-10.5: 12
Added mass, defined, 9.6.8: 58 malfunction causes and remedies, 10.1-10.5: 20, 22 t.
Adhesive wear resistance of wrought materials, 9.1-9.5: typical services, 10.1-10.5: 11
11 t. Air-operated diaphragm pumps, 10.1-10.5: 1 f., 1
AEX XML Schema, 50.7: 1, 2, 29 and rate of flow, 10.1-10.5: 13
and construction materials and properties, 50.7: 24 diaphragm selection and materials, 10.1-10.5: 13
and W3C schema namespace declaration, 50.7: 26 features, 10.1-10.5: 12
and XPaths, 50.7: 28 handling of hazardous liquids, 10.1-10.5: 11
and XSD file names and associated namespaces, liquids and slurries handled, 10.1-10.5: 11
50.7: 27 malfunction causes and remedies, 10.1-10.5: 20, 21 t.
collection-container type, 50.7: 25, 27f., 29 pump controls, 10.1-10.5: 13
content, 50.7: 23 pumping of dry powders, 10.1-10.5: 12
core data type, 50.7: 24, 27 f., 29 typical applications, 10.1-10.5: 11
core object type, 50.7: 24, 27 f., 29 Air-operated pump tests, 10.6: 1
document namespaces, 50.7: 26 air consumption, defined, 10.6: 6
equipment data foundation files, 50.7: 23 air consumption, measurement of, 10.6: 14
file folder structure, 50.7: 26 cavitation, defined, 10.6: 6
for equipment items, 50.7: 23, 24 f. cycle rate (n) defined, 10.6: 3
Hydraulic Institute Standards, Copyright © 1997-2017, All Rights Reserved 1
HI Master Index for Complete Set: Version 4.0

Air-operated pump; tests – Continued performance tests, 10.6: 6, 7, 7f., 8, 8f.
cycle rate (n), measurement of, 10.6: 14 pressure (p), defined, 10.6: 4
cycle, defined, 10.6: 3 pressure (p), measurement of, 10.6: 14, 15f.
datum, defined, 10.6: 4 pressure (p), tap location, 10.6: 14
definitions, 10.6: 1 priming. see suction lift
displacement per stroke (D), defined, 10.6: 4 rate of flow (capacity) (Q), defined, 10.6: 3
dry suction lift defined, 10.6: 9 rate of flow (capacity) (Q), measurement of, 10.6: 16
dry suction lift, vacuum gauge test method, 10.6: 10 rated condition point, 10.6: 1
dry suction lift, vacuum gauge with enclosed tank test specific weight (γ) of water, defined, 10.6: 3
method, 10.6: 10 speed (cycle rate) measurement, 10.6: 15
dry suction lift, water lift test method, 10.6: 10 standard cubic feet per minute (SCFM), defined, 10.6:
effective diaphragm area (A ), definition and 6
EFF
equation, 10.6: 4, 4f. stroke length (L), defined, 10.6: 3
elevation head (Z), defined, 10.6: 5 subscripts, 10.6: 3t.
elevation pressure (p ), defined, 10.6: 4 suction lift (priming), defined, 10.6: 5
z
gauge pressure (p ), defined, 10.6: 4 suction lift testing, 10.6: 9, 10, 10f.
g
hydrostatic test, on components or assembled pumps, symbols, 10.6: 2t.
10.6: 11 temperature measurement, 10.6: 16
hydrostatic test, parameters, 10.6: 11 test instrumentation. see instrumentation
hydrostatic test, procedure, 10.6: 11 total head (pH), definition and equation, 10.6: 5
instrumentation, 10.6: 12 types of, 10.6: 1
instrumentation, acceptable fluctuation and accuracy, velocity pressure (pv), definition and equation, 10.6: 5
10.6: 13, 13t. volume, standard units of, 10.6: 3
instrumentation, calibration intervals, 10.6: 12, 13t. wet suction lift, test methods, 10.6: 10, 11
instrumentation, for air consumption measurement, Air-operated pumps, 10.1-10.5: 1
10.6: 14, 15 acceleration head (hacc), calculations, 10.1-10.5: 9
instrumentation, for pressure measurement, 10.6: 14, acceleration head (hacc), defined, 10.1-10.5: 9
15f. acceleration pressure (pacc), calculations, 10.1-10.5: 9
instrumentation, for rate of flow (capacity) acceleration pressure (pacc), defined, 10.1-10.5: 9
measurement, 10.6: 16 air chamber, 10.1-10.5: 2
instrumentation, for speed (cycle rate) measurement, air consumption, defined, 10.1-10.5: 10
10.6: 15 air distribution system, 10.1-10.5: 2
instrumentation, for temperature measurement, 10.6: ball check valves, 10.1-10.5: 4 f.
16 bellows, 10.1-10.5: 3
instrumentation, pressure tap location, 10.6: 14 cavitation, defined, 10.1-10.5: 7
maximum allowable air inlet pressure, defined, 10.6: check valves, 10.1-10.5: 4, 4 f.
4 colloidal liquids, defined, 10.1-10.5: 11
maximum allowable discharge pressure, defined, compressed-air properties definitions, 10.1-10.5: 10
10.6: 4 condensation, defined, 10.1-10.5: 10
maximum allowable suction pressure (p ), defined, cycle rate (n), defined, 10.1-10.5: 4
s max
10.6: 5 cycle, defined, 10.1-10.5: 4
mechanical test, 10.6: 6 datum, defined, 10.1-10.5: 6
net positive inlet pressure available (NPIPA), definition definitions, 10.1-10.5: 4
and equation, 10.6: 5 design, 10.1-10.5: 11-14
net positive inlet pressure required (NPIPR) test, 10.6: dew point, defined, 10.1-10.5: 10
7f.., 8, 8f., 9 diaphragm with integral outer plate, 10.1-10.5: 3 f., 3
net positive inlet pressure required (NPIPR), defined, diaphragm, 10.1-10.5: 2
10.6: 6 diaphragm, inner and outer plates, 10.1-10.5: 3
net positive suction head available (NPSHA), definition dilatant liquids, defined, 10.1-10.5: 11
and equation, 10.6: 5 discharge manifold, 10.1-10.5: 3
net positive suction head required (NPSHR) test, 10.6: discharge pressure (pd), defined, 10.1-10.5: 6
7f., 8, 8f., 9 displacement per stroke (D), defined, 10.1-10.5: 6
net positive suction head required (NPSHR), defined, dry suction lift, defined, 10.1-10.5: 7
10.6: 6 duplex, 10.1-10.5: 2
net positive suction head test, 10.6: 7, 7f., 8 effective diaphragm area (AEFF), defined, 10.1-10.5: 4,
noise testing, 10.6: 12 4 f.
normal cubic meter per minute, 10.6: 6 elastomer shelf life, 10.1-10.5: 20
2 Hydraulic Institute Standards, Copyright © 1997-2017, All Rights Reserved
HI Master Index for Complete Set: Version 4.0
Air-operated pumps – Continued specific gravity, and effect on pump performance,
flap check valves, 10.1-10.5: 4 f. 10.1-10.5: 14
flooded suction, defined, 10.1-10.5: 7 standard cubic feet per minute (SCFM), defined, 10.1-
friction loss pressure (p), defined, 10.1-10.5: 7 10.5: 10
f
handling of hazardous liquids, 10.1-10.5: 11 storage, 10.1-10.5: 20
handling of hot liquids, 10.1-10.5: 12 stroke length (L), defined, 10.1-10.5: 4
inlet air pressure (p), defined, 10.1-10.5: 6 submerged suction, defined, 10.1-10.5: 7
i
inlet manifold, 10.1-10.5: 3 subscripts, 10.1-10.5: 4, 6 t.
inspection, before installation, 10.1-10.5: 15 suction conditions, 10.1-10.5: 7
inspection, for maintenance, 10.1-10.5: 20 suction lift (priming), defined, 10.1-10.5: 7
installation, 10.1-10.5: 14-16, 16 f., 17, 17f. suction pressure (p ), defined, 10.1-10.5: 7
s
liquid chamber, 10.1-10.5: 3 symbols, 10.1-10.5: 4, 5 t.
liquid properties, 10.1-10.5: 11 terms, 10.1-10.5: 4, 5 t.
liquids and slurries handled, 10.1-10.5: 11 thixotropic liquids, defined, 10.1-10.5: 11
maintenance, 10.1-10.5: 20, 21t., 22t. total differential pressure (p ), defined, 10.1-10.5: 7
H
maximum allowable air inlet pressure, defined, 10.1- total suction lift, defined, 10.1-10.5: 8
10.5: 6 types, 10.1-10.5: 1, 1 f.
maximum allowable discharge pressure, defined, typical services, 10.1-10.5: 11
10.1-10.5: 6 units, 10.1-10.5: 4, 5 t.
maximum allowable suction pressure (p ), defined, viscosity, 10.1-10.5: 11, 14
s max
10.1-10.5: 7 wet suction lift, 10.1-10.5: defined, 8
maximum cycle rate, defined, 10.1-10.5: 4 wetted path housings, 10.1-10.5: 3
maximum operating temperature (t ), defined, 10.1- Alarm limits, 9.6.5: 4
max
10.5: 10 defined, 9.6.9: 5
minimum operating temperature (t ), defined, 10.1- leakage guidelines, 9.6.9: 11
min
10.5: 10 power guidelines, 9.6.9: 6
net positive inlet pressure available (NPIPA), defined, rate-of-flow guidelines, 9.6.9: 13
10.1-10.5: 8 speed (rpm) guidelines, 9.6.9: 14
net positive inlet pressure required (NPIPR), defined, temperature guidelines, 9.6.9: 9
10.1-10.5: 8 vibration guidelines, 9.6.9: 13
net positive suction head (NPSH) terminology, Alignment, 3.1-3.5: 58
10.1-10.5: 8 Alkalinity, of water, 2.3: 79
net positive suction head available (NPSHA), defined, Allowable bearing housing vibration pump types BB and
10.1-10.5: 8 OH, 9.6.4: 8 f.
net positive suction head required (NPSHR), defined, at speeds above 600 rpm, 9.6.4: 7, 8 f., 9 f.
10.1-10.5: 8 at speeds of 600 rpm and below, 9.6.4: 10 t.
newtonian liquids, defined, 10.1-10.5: 11 pump types VS1, VS2, VS3, VS4, VS5, VS6, VS7,
nomenclature, 10.1-10.5: 2 VS8, 9.6.4: 8 f.
NPIPA. See net positive inlet pressure available slurry pump types, 9.6.4: 9 f.
NPIPR. See net positive inlet pressure required solids-handling pump types, 9.6.4: 9 f.
NPSH. See net positive suction head Allowable imbalance, 9.6.8: 32
NPSHA. See Net positive suction head available Allowable operating range, defined, 12.1-12.6: 35
NPSHR. See net positive suction head required Allowable operating region (AOR), 9.6.3: 2
operation, 10.1-10.5: 17, 18 f., 19 and bearing life, 9.6.3: 3
pressures terminology, 10.1-10.5: 6 and dip (in head vs. rate-of-flow curve), 9.6.3: 6, 7f.
priming. see suction lift and droop (in head vs. rate-of-flow curve), 9.6.3: 5–6,
pulsation dampeners, 10.1-10.5: 10 6f.
pulsation dampeners, 10.1-10.5: 10 and factory test, 9.6.3: 2
pumping of dry powders, 10.1-10.5: 12 and hydraulic loads, 9.6.3: 3
rate of flow (capacity) (Q), defined, 10.1-10.5: 4 and internal mechanical contact, 9.6.3: 4
rate of flow terminology, 10.1-10.5: 4 and liquid velocity, 9.6.3: 5
relative humidity, defined, 10.1-10.5: 10 and noise, 9.6.3: 4
safety, 10.1-10.5: 19 and NPSH margin, 9.6.3: 5, 5f.
saturation vapor pressure, defined, 10.1-10.5: 10 and power limit, 9.6.3: 4
SCFM. see standard cubic feet per minute and pump size, 9.6.3: 8
semperature, 10.1-10.5: 10 and service life, 9.6.3: 2
simplex, 10.1-10.5: 2 and shaft fatigue life, 9.6.3: 3
Hydraulic Institute Standards, Copyright © 1997-2017, All Rights Reserved 3
HI Master Index for Complete Set: Version 4.0

Allowable operating region (AOR) – Continued maximum forces and moments for use with Equation
and shaft seal life, 9.6.3: 4 Set 1, 9.6.2: 6t.
and suction recirculation, 9.6.3: 7–8, 8f. maximum forces and moments for use with Equation
and temperature rise, 9.6.3: 4 Set 2, 9.6.2: 7t.
and thrust reversal, 9.6.3: 4 maximum forces and moments for use with Equation
and vibration, 9.6.3: 4 Set 3, 9.6.2: 8t.
defined, 9.6.3: 2 maximum forces and moments for use with Equation
factors affecting, 9.6.3: 2–8 Set 4, 9.6.2: 8t.
Allowable operating region defined, 1.1-1.2: 71, 2.1-2.2: metallic pump adjustment of maximum forces and
34 moments, 9.6.2: 5
Alnico magnet, defined, 5.1-5.6: 17 metallic pump combined force/moment capability,
Alnico, defined, 4.1-4.6: 9 9.6.2: 5
Aluminum, 9.1-9.5: 21 metallic pump load capability, 9.6.2: 5
alloy 319, 9.1-9.5: 21 metallic pump temperature and material adjustment
alloy 355, 9.1-9.5: 21 values, 9.6.2: 10t.
alloy 356, 9.1-9.5: 21 metallic pumps, 9.6.2: 5
alloy 7075 (AI-Zn-Mg-Cu-Cr), 9.1-9.5: 22 ANSI/ASME B73.1 pumps
alloy ASTM B211, alloy 2011, 9.1-9.5: 22 example assessments of applied nozzle loads (1.5×1-8
alloy ASTM B211, alloy 6061, 9.1-9.5: 22 CF8M Type 316, 9.6.2: Class 150 flanges, at 100
alloy B750, 9.1-9.5: 22 °F, fully grouted metal baseplate), 9.6.2: 24
alloy C-355-T6, 9.1-9.5: 21 example assessments of applied nozzle loads (1.5×1-
alloy TP-220-T4, 9.1-9.5: 21 8, material with a modulus of elasticity greater than
aluminum copper (AI/Cu) SAE AA2017, 9.1-9.5: 22 1.0 × 106, at 110 °F, fully grouted nonmetal
compatibility with other materials, 9.1-9.5: 21 baseplate), 9.6.2: 29
tenzalloy, 9.1-9.5: 22 example assessments of applied nozzle loads (3×1.5-
American Bearing Manufacturers Association, 5.1-5.6: 46 13 Alloy 20, Class 300 flanges, at 400 °F, fully
American Petroleum Institute, 5.1-5.6: 46 grouted metal baseplate), 9.6.2: 27
American Society for Heating, Refrigerating, and Air- ANSI/ASME B73.1 Specification for Horizontal End
Conditioning Engineers (ASHRAE), 50.7: 3 Suction Centrifugal Pumps for Chemical Process,
American Society for Testing and Materials, 5.1-5.6: 48 50.7: 1, 3, 8
American Society of Mechanical Engineers, 5.1-5.6: 46 ANSI/ASME B73.2 pumps
Amplification chart, 9.6.8: 85f. example assessments of applied nozzle loads
Amplification factor, defined, 9.6.8: 58 (4030/28, 2-in discharge, 13-in nominal impeller,
Analyses beyond scope of document, 9.6.8: 7 Alloy 20, Class 300 flanges, at 400 °F), 9.6.2: 33
Analysis complexity levels, 9.6.8: 28t. example assessments of applied nozzle loads (size
Analysis level, 9.6.8: 3 2015/17, 1.5-in discharge, 8-in nominal impeller,
elements, 9.6.8: 36 CF8M Type 316, Class 150 flanges, at 100 °F),
limitations, 9.6.8: 36 9.6.2: 32
Analysis level definitions, 9.6.8: 33 ANSI/ASME B73.2 Specification for Vertical In-Line
level 1, 9.6.8: 33 Centrifugal Pumps for Chemical Process, 50.7: 1, 3,
level 2, 9.6.8: 34 8
level 3, 9.6.8: 36 ANSI/ASME B73.3 sealless pump assessment of applied
Analysis levels introduction, 9.6.8: 27 nozzle loads, 9.6.2: 8
See also Levels of analysis ANSI/HI 1.6 Centrifugal Pump Tests, 14.6: 1
types, 9.6.8: 27 ANSI/HI 11.6 Submersible Pump Tests, 14.6: 1
Analysis reporting format, 9.6.8: 92 ANSI/HI 2.6 Vertical Pump Tests, 14.6: 1
Analysis, 40.6: 11 ANSI/HI 5.1–5.6 Sealless Rotodynamic Pumps for
translation of the test results into data based on the Nomenclature, Definitions, Design, Application,
specified speed of rotation (or frequency), 40.6: 11 Operation, and Test, 14.6: 1
translation of the test results to the rated speed of Anti-reverse rotation devices, 2.3: 27
rotation, 40.6: 11 Anti-rotation baffles defined, 9.8: 48
Angular momentum, 1.3: 1 and rectangular wet wells, 9.8: 32
Annular seal, defined, 9.6.8: 58 and trench-type wet wells, 9.8: 26f., 27
ANSI/ASME B73.1 pump assessment of applied nozzle API 610 Standard for Centrifugal Pumps for Petroleum,
loads, 9.6.2: 5 Petrochemical and Natural Gas Industries, 50.7: 1,
composite pumps, 9.6.2: 8 3, 8
Equation Sets 1-5, 9.6.2: 5t. additional data to support data sheet, 50.7: 14
4 Hydraulic Institute Standards, Copyright © 1997-2017, All Rights Reserved
HI Master Index for Complete Set: Version 4.0
API 610 Standard for Centrifugal Pumps for Petroleum, application, 5.1-5.6: 33
Petrochemical and Natural Gas Industries – uses of sealless pumps, 5.1-5.6: 33
Continued Applications, 1.3: 113, 12.1-12.6: 44–45
and HI-EDE implementation, 50.7: 20 booster service, 1.3: 114
data sheet, 50.7: 8, 9 f. dry pit (nonclog) pumps, 1.3: 117, 118f.
See also R/D/S/A compliance pump as turbine (PAT), 1.3: 114, 115f., 117
API double suction pumps, 20.3: 5 t. self-priming pumps, 1.3: 119, 120f., 121f., 123
API end suction pumps, 20.3: 5 t. transfer pumping, 1.3: 113
API Plan 02, 12.1-12.6: 84 two-phase pumping (liquid and gas), 1.3: 122, 122f.,
API Plan 11, 12.1-12.6: 84 123f., 124f., 125f.
API Plan 32, 12.1-12.6: 84 type OH pumps as self-priming pumps, 1.3: 120
API Plan 52, 12.1-12.6: 84 Approach channel, defined, 9.8: 48
API Plan 53, 12.1-12.6: 84 Approach flow patterns
API Plan 54, 12.1-12.6: 84 at various intakes, and effects on velocity, 9.8: 62f.
API Plan 62, 12.1-12.6: 85 for various combinations of pumps, 9.8: 63f.
API Standard 610 (impellers), 1.3: 35 remedial measures for, 9.8: 60, 62f., 63f., 64f., 65f.
API-type, single-stage, end suction process pump, 20.3: 3 with multiple pumps in open and partitioned sumps,
Apparent viscosity, 6.1-6.5: 34 9.8: 64f.
defined, 3.1-3.5: 37, 12.1-12.6: 38 Approval process
Appeals, 40.7: 8 applicable standards, 40.7: 3
Application considerations, 4.1-4.6: 13 application approved, 40.7: 3
bearings, 4.1-4.6: 17 application for approval, 40.7: 3
containment shell thickness and materials, 4.1-4.6: application rejected, 40.7: 3
17 approval decision, 40.7: 5
coupling selection, 4.1-4.6: 13 approval denied, 40.7: 5
entrained air or gas, 4.1-4.6: 15 approval granted upon remedy of nonconformities,
high viscosity, 4.1-4.6: 14 40.7: 5
liquid classification, 4.1-4.6: 16 audit flowchart, 40.7: 17 f.
liquid properties, 4.1-4.6: 14 confidentiality, 40.7: 4
liquid vapor pressure, 4.1-4.6: 15 demonstrations of pump testing procedures, 40.7: 5
low viscosity, 4.1-4.6: 15 documents needed for audit, 40.7: 16
lubricating liquid, 4.1-4.6: 16 general, 40.7: 3
magnets, 4.1-4.6: 13, 17 languages used, 40.7: 4
materials, 4.1-4.6: 17 on-site assessment, 40.7: 4
mechanical safety, 4.1-4.6: 18 opening meeting, 40.7: 4
monitoring devices, 4.1-4.6: 18 records review, 40.7: 5
nonlubricating liquid, 4.1-4.6: 16 renewal of approval, 40.7: 6
off-design rating procedures, 4.1-4.6: 16 role of Auditor, 40.7: 4
particles, 4.1-4.6: 15 staff interviews, 40.7: 5
pump, 4.1-4.6: 17 ASME B73 (baseplates), 1.3: 101, 101f.
safety, 4.1-4.6: 17 ASME B73 pumps, 20.3: 5 t.
shear sensitivity, 4.1-4.6: 16 ASME B73.1 (impellers), 1.3: 35
specific gravity, 4.1-4.6: 15 ASME/ANSI B73.1
specific heat, 4.1-4.6: 15 Asynchronous, defined, 9.6.8: 58
stripping applications, 4.1-4.6: 16 ATEX Certification, 1.4: 8, 2.4: 8
temperature, 4.1-4.6: 14 Atmospheric head (h ), 1.1-1.2:
atm
variable viscosity, 4.1-4.6: 15 defined, 2.1-2.2: 33, 70, 11.6: 8, 12.1-12.6: 35
viscosity, 4.1-4.6: 14 Attainable efficiency example (metric units)
Application guidelines, 5.1-5.6: 33, 8.1-8.5: 13 Attainable efficiency example (US customary units) single-
canned motor or magnet component temperature, stage, end suction, solids-handling submersible
5.1-5.6: 38 sewage type pump, 20.3: 4
containment expectations, 5.1-5.6: 33 Audit flowchart, 40.7: 17 f.
pump selection, 5.1-5.6: 36 Audit requirements changes to, 40.7: 7 t.
safety considerations, 5.1-5.6: 34 Auditor, defined, 40.7: 1
sealless pump advantages, 5.1-5.6: 33 Austenitic stainless steels, 12.1-12.6: 67
sealless pump limitations, 5.1-5.6: 33 Auxiliary drive (steam) valve, 8.1-8.5: 6
unit design and circulation plan selection and
Hydraulic Institute Standards, Copyright © 1997-2017, All Rights Reserved 5
HI Master Index for Complete Set: Version 4.0

Average particle size (d50), 12.1-12.6: 39t. scope, 9.6.2: 15
defined, 12.1-12.6: 39 b . See Impeller width at discharge
2
Axial flow (propeller) pump, defined, 9.8: 48 (b ) Barrier fluid, 1.3: 63
2
Axial flow impeller, 2.1-2.2: 19, 2.3: 6, 6 f., 9 Back pull-out assembly, defined, 1.1-1.2: 42, 43 f.
Axial flow pumps, 1.1-1.2: 10 f., 11, 11 f. Backpressure valves, 7.8: 12
Axial load, 1.3: 34 Backwall clearance defined, 9.8: 49
Axial load, defined, 5.1-5.6: 14 remedial measures for, 9.8: 72
Axial piston pumps, 3.1-3.5: 1f., 3t., 4t., 5f., 6f., 14f. Backwall splitter, defined, 9.8: 49
description, 3.1-3.5: 7 Backwall, defined, 9.8: 48
fixed displacement, 3.1-3.5: 8 Baffles
range chart, 3.1-3.5: 8 anti-rotation baffle between end pump and backwall in
variable displacement, 3.1-3.5: 8 performance enhancement of trench-type wet wells,
Axial split case pumps (single-stage double suction and 9.8: 26f., 86f., 87
two-stage single suction) defined, 9.8: 49
example assessments of applied nozzle loads (4-in inlet baffles in performance enhancement of trench-
discharge, 7/8-in hold-down bolts, cast-iron class type wet wells, 9.8: 85, 85f.
125 flanges), 9.6.2: 34 See also Anti-rotation baffles
Axial thrust factor (K ), 1.3: 22, 22f. to improve flow pattern downstream from dual flow
A
Axial thrust, 2.3: 8, 9 f. screen, 9.8: 67f.
calculating by manufacturer’s thrust factor method, Balance machines, 9.6.4: 13
2.3: 14 weight rating, 9.6.4: 14
calculating for impellers with back rings (at BEP), 2.3: Balancing
13 and inherent balance, 9.6.4: 15
calculating for impellers with no back rings (at BEP), and keys and keyways in balancing arbors, 9.6.4: 16
2.3: 11, 12 f. and removal or addition of material, 9.6.4: 17
calculating, 2.3: 9 and runout in balancer drive or balancing arbor, 9.6.4:
calculation for axial flow pump impellers, 1.3: 31 15
calculation for enclosed impeller with plain back excessive looseness between impeller hub and
shroud, 1.3: 23f., 23, 26 balancing arbor, 9.6.4: 16
calculation for impeller with back ring, 1.3: 25f., 25, 27 Bare rotor
calculation for impellers, 1.3: 21 defined, 2.1-2.2: 43
calculation for semi-open impellers, 1.3: 29, 29f. terms, 2.1-2.2: 41
calculation of axial force due to momentum change, Barometric pressure, 6.1-6.5: 28t., 28, 8.1-8.5: 11
1.3: 31 and altitude, 8.1-8.5: 11, 12t.
on enclosed impellers, 1.3: 21, 21f. Barrel design. See Pump type BB4
shaft upthrust force from enclosed suction can pumps, Barrel or can (line shaft) pumps, 2.1-2.2: 11
2.3: 10 f., 10 Barrel suction, defined, 9.8: 49
shaft upthrust force from shaft sleeves through Barrier fluid flow leakage monitoring, 9.6.9: 10, 10t.
packing or mechanical seals, 2.3: 10, 11 f. Barrier fluid, defined, 12.1-12.6: 38
shaft upthrust force from shaft sleeves through Baseline measurements, 9.6.5: 3
pressure breakdown bushings, 2.3: 10, 11 f. Baseline, 9.6.9: 27
static component of, 2.3: 10 defined, 9.6.5: 55
terminology, 2.3: 8 Baseplates, 1.3: 94
versus rate of flow, 2.3: 14, 15 f. selection parameters, 1.3: 95t.
Axially split one- and two-stage pumps (BB1) alignment blocks or guides for thermal expansion of
assessment of applied loads, 9.6.2: 17 the pump case, 1.3: 108
casing hold-down bolts, 9.6.2: 17 coupling alignment, 1.3: 107
coordinate system, 9.6.2: 16f. drip rims, 1.3: 108
criteria for loading allowances, 9.6.2: 16 epoxy grouting, 1.3: 108
definitions, 9.6.2: 15 fasteners, 1.3: 108
driver/pump coupling arrangement, 9.6.2: 16 formed polymer, 1.3: 102, 103f.
effect of nozzle loading on hold-down bolts, 9.6.2: 17 freestanding, 1.3: 99, 100f.
limiting factors, 9.6.2: 16 functional requirements, 1.3: 95, 95t.
maximum forces and moments to assess applied loads grout holes, 1.3: 109
based on hold-down bolts, 9.6.2: 18t. grouted, 1.3: 97, 97f., 98f.
maximum forces and moments to assess applied loads jacking pads and screws, 1.3: 108
based on nozzle stress, 9.6.2: 18t. leveling screws, 1.3: 108
6 Hydraulic Institute Standards, Copyright © 1997-2017, All Rights Reserved
HI Master Index for Complete Set: Version 4.0
Baseplates – Continued Bearing whirl, defined, 9.6.8: 58
lifting requirements, 1.3: 108 Bearing, defined, 3.1-3.5: 16
nongrout, 1.3: 97, 98f. Bearings, 1.3: 43, 12.1-12.6: 69–71
offshore skid type, 1.3: 104, 105f. adjusted rating life, Lna, 1.3: 47, 50, 50t.
oil pipeline skid type, 1.3: 104, 105f. air entrainment in lubricants, 1.3: 56
pedestal, 1.3: 103, 104f. and contact seals, 12.1-12.6: 69
polymer, 1.3: 102 and labyrinth seals, 12.1-12.6: 69, 70f.
pregrouted, 1.3: 98, 99f. and lip seals, 12.1-12.6: 69, 69f.
shims and fasteners, 1.3: 108 axial adjustment of housing, 12.1-12.6: 92
slide-bearing, 1.3: 100, 100f. axial load, Fa, 1.3: 47
sloped deck plates, 1.3: 108 ball bearings, 1.3: 46f.
soleplates, 1.3: 99, 100f. basic dynamic radial load rating, Cr, 1.3: 47
solid polymer concrete, 1.3: 103, 103f. basic rating life, L10, 1.3: 47, 49
standards, 1.3: 101, 101f., 102f. contamination factor, ηc, 1.3: 51, 52t.
stress and rigidity requirements, 1.3: 107 contamination prevention in lubricants, 1.3: 56
three-point mount, 1.3: 106, 106f. cylindrical-type radial journal (sleeve) bearings, 1.3:
tolerancing, 1.3: 107 45f.
types, 1.3: 96 degradation improvement in lubricants, 1.3: 57
Bays dynamic equivalent radial load, (P), 1.3: 47
r
and adequate width (rectangular intakes for clear factors, 1.3: 48
liquids), 9.8: 3 failure mode indicated by temperature monitoring,
defined, 9.8: 49 9.6.9: 7
flow-guiding devices at entrance to, 9.8: 65, 65f. failure mode indicated by vibration monitoring, 9.6.9:
narrow widths, remedial measures for, 9.8: 72 12
trash racks and effect on velocity distribution entering fatigue life, 12.1-12.6: 71, 71t.
pump bay, 9.8: 64f. fatigue limit load, Cu, 1.3: 51
BB1-BB5. See Pump type BB1-Pump type BB5 friction losses due to viscosity, 2.3: 50
Bearing arrangements, 1.3: 31 grease lubrication, 1.3: 53
Bearing bushings, 2.3: 16 heat and oil oxidation, 1.3: 56
in adapters, 2.3: 64 heat stabilization temperature, 1.3: 53
intermediate, 2.3: 64 high level of lubricant, 1.3: 55
losses due to viscosity, 2.3: 50 hydrodynamic radial, 9.6.9: 7
Bearing housing, 2.3: 64, 73 isolators, 12.1-12.6: 70, 70f.
and temperature monitoring, 9.6.9: 7 life (horizontal pumps), 1.3: 46
and vibration monitoring, 9.6.9: 12 life modification factor, axyz, 1.3: 49
Bearing housing closures, 2.3: 26 life, 1.3: 48
Bearing housings liquid film, temperature monitoring, 9.6.5: 7
acceleration in vibration monitoring, 9.6.5: 15 low level of lubricant, 1.3: 55
vibration control limits, 9.6.5: 15–16 lubrication methods, 1.3: 43
vibration monitoring, 9.6.5: 15, 16 lubrication, 1.3: 53
Bearing isolators, 2.3: 26 lubrication, 2.3: 19
Bearing materials, 4.1-4.6: 17 material adjustment factor, a2, 1.3: 48
Bearing wear monitoring, 9.6.5: 20 minimum load, 1.3: 46
by acoustic sensors, 9.6.5: 21 modified rating life, Lnm, 1.3: 48, 50
by contact or continuity switches, 9.6.5: 21 moisture elimination in lubricants, 1.3: 57
by power monitors, 9.6.5: 21 oil lubrication, 1.3: 54
by proximity sensing devices, 9.6.5: 21 operating conditions adjustment factor, a3, 1.3: 48
by temperature probes, 9.6.5: 21 outboard (antifriction), 2.3: 73
by vibration sensors, 9.6.5: 21 outboard, 2.3: 64
carbon bearings, 9.6.5: 21 particle contamination of lubricants, 1.3: 56
component contact detection, 9.6.5: 21 pivot-shoe thrust bearings, 1.3: 45, 45f.
control limits, 9.6.5: 22 product lubrication, 1.3: 55
detection methods, 9.6.5: 21 quality of lubrication, 1.3: 55
of plain bearings in sealless pumps, 9.6.5: 20 quality of oil, 1.3: 55
progressive monitoring, 9.6.5: 21 quantity improvement of lubricants, 1.3: 56
silicon carbide bearings, 9.6.5: 21 radial load, Fr, 1.3: 47
Bearing whip, defined, 9.6.8: 58 reliability adjustment factor, a1, 1.3: 48
Hydraulic Institute Standards, Copyright © 1997-2017, All Rights Reserved 7
HI Master Index for Complete Set: Version 4.0

Bearings – Continued Bowl assembly input power (P ), defined, 2.1-2.2: 36
ba
reliability, 1.3: 47 Bowl assembly total head (H ), defined, 2.1-2.2: 33
ba
retainer, 2.3: 64 Bowl assembly total head determination for vertically
roller bearings, 1.3: 46f. suspended pump with a closed suction, 40.6: 20 f.
rolling element bearing failure, 9.6.9: 5, 15t. Bowl assembly total head determination for vertically
rolling element bearings, 1.3: 44, 44t. suspended pumps, 14.6: 33 f. , 40.6: 19 f.
rolling element defects, 9.6.9: 12 with a closed suction, 14.6: 37 f.
rolling element temperature monitoring, 9.6.9: 7 Bowl assembly total head, definition, 40.6: 17
rolling element, defects in vibration monitoring, 9.6.5: Bowl efficiency
15 and losses due to viscosity, 2.3: 50
sleeve bearing failure, 9.6.9: 5 Brake horsepower. See Pump input power
sleeve bearing temperature monitoring, 9.6.9: 7 Bromobutyl, 12.1-12.6: 68
sleeve bearings, 1.3: 44, 45f. Bubble test, 4.1-4.6: 26
spacing, 2.3: 19 Buffer fluid, 1.3: 63, 12.1-12.6: 79
temperature, 1.3: 53 defined, 12.1-12.6: 38
thrust, 9.6.9: 7 Building services (HVAC), 9.6.1: 12
type BB4 multistage radial split single casing pump, Bull ring packing, 6.1-6.5: 77f., 77
1.3: 46f. Butyl, 12.1-12.6: 68
water contamination of lubricants, 1.3: 56 Bypass valves, 9.6.9: 8
Bell inlet velocity, defined, 9.8: 40 Calculations, 7.6: 11
Bell, defined, 9.8: 49 of NPSHA on dry-pit pump, 11.6: 48
Benching, defined, 9.8: 49 of NPSHA on wet-pit pump, 11.6: 47
BEP rate of flow [Q ], defined, 1.1-1.2: 68, 71 2.1-2.2: 30, of performance based on change in pump impeller
opt
34 diameter, 11.6: 46
BEP. See Best efficiency point of performance based on change in pump speed, 11.6:
Best efficiency point (BEP), 1.3: 1, 15, 9.6.3: 1, 9.6.8: 58, 45
12.1-12.6: 64, 64t. of performance tolerance bands for pump acceptance
defined, 2.3: 41, 11.6: 5, 12.1-12.6: 35 according to grade 1E and 2B, 11.6: 49
operation above, 2.3: 41 Calibration columns, 7.8: 15
operation away from, 1.3: 71 Campbell diagram for variable frequency unit, 9.6.8: 85f.
operation below, 2.3: 41 Campbell diagram, 9.6.8: 30, 33
Best efficiency point (BEP) values, 20.3: 1 defined, 9.6.8: 58
Best efficiency point (BEP), and NPSH margin, 9.6.1: 4, for lateral critical speeds, 9.6.8: 31f.
4f. for torsional critical speeds, 9.6.8: 34f.
Between bearings, multistage, axially split pump, 1.1-1.2: Can pump, defined, 9.8: 17
31 f. Can vertical turbine pump intakes (clear liquids), 9.8: 17
Between bearings, multistage, radially split, double casing can pump, defined, 9.8: 17
pump, 1.1-1.2: 33 f. closed bottom, 9.8: 18, 19, 21f.
Between bearings, multistage, radially split, single casing design considerations, 9.8: 19
pump, 1.1-1.2: 32 f. open bottom, 9.8: 18, 19, 20f.
Between bearings, single stage, axially split pump, 1.1- Canned motor pump
1.2: 29 f. cooling and lubrication, 5.1-5.6: 1
Between bearings, single stage, radially split pump, 1.1- end suction, 5.1-5.6: 2
1.2: 30 f. end suction, overhung impeller, 5.1-5.6: 4f.
Between-bearings (BB) type, 1.3: 1, 33, 33f., 110, 112f. in-line, 5.1-5.6: 2
axial load for multistage pumps, 1.3: 34 motor and pump separated by thermal barrier (plan
double suction pumps, 1.3: 33, 34f. 123), 5.1-5.6: 55f.
multistage pumps, 1.3: 34, 34f. motor insulation temperature limits, 5.1-5.6: 38t.
radial load for multistage pumps, 1.3: 34 multistage end suction, 5.1-5.6: 54
shaft support for multistage pumps, 1.3: 34 multistage, 5.1-5.6: 57f.
Between-bearing impeller pumps icons, 1.1-1.2: 78 f.–79 f. retrofit end suction design, 5.1-5.6: 54
Between-bearing pump defined, 9.6.8: 27 retrofit with external circulation, 5.1-5.6: 56f.
Bibliography, 9.1-9.5: 44, 9.6.7: 27 reverse circulation (plan 113), 5.1-5.6: 55f.
Body, defined, 3.1-3.5: 16 reverse circulation end suction (circulation plan 113)
Bolted couplings, 2.3: 29 design, 5.1-5.6: 54
Boltproof load, defined, 5.1-5.6: 18 self-priming end suction, 5.1-5.6: 54
Bowl assembly efficiency (η ), defined, 2.1-2.2: 37 self-priming, 5.1-5.6: 57f.
ba
8 Hydraulic Institute Standards, Copyright © 1997-2017, All Rights Reserved