| Glossary
Term |
Term Definition |
| Absolute
Viscosity |
Absolute Viscosity is
usually measured in centipoises (cp). Water at room temperature has a
viscosity of one cp. |
| Agglomeration |
The recombining of finely
dispersed particles into larger particles, usually caused by a rearrangement
of surface forces resulting from a change of environment. It is the opposite
of dispersion. |
| Agitators |
A device consisting of at
least a Power Package, a shaft and an Impeller to provide agitation of the
contents of a vessel. Agitators commonly mix substances with low viscosities
in low-shear applications. Agitators range in size from small agitators used
in laboratory applications to large industrial agitators with 10,000-gallon
capacities. |
| Alginate |
Salt found in the cell wall
of brown algae. Alginates are used in food processing to stabilize certain
mixtures (e.g. emulsions), to seal in moisture and to thicken texture, among
other things. |
| American
Society of Mechanical Engineers (ASME) |
(ASME) creates consensus
standards for Mechanical Engineering. |
| Anchor
Impeller |
An Impeller with vertical blades whose contour closely
conforms to the vessel bottom and walls. |
| Anchor
Paddle |
An Impeller whose contour
closely conforms to the vessel bottom and walls. |
| Apparent
Viscosity |
The viscosity of a
Non-Newtonian Fluid at a specified shear rate. Also, the consistency of a
material at some particular velocity. |
| Apparent
Viscosity |
The flow resistance of a
Non-Newtonian Fluid at some arbitrary point on its stress-flow curve and the
consistency of a material at some particular velocity. |
| Axial
Flow |
The movement of fluid from
the top to the bottom of a tank. |
| Axial
Turbine |
A Turbine with pitched blades, (usually 45°) whose
discharge is a mixture of Axial and Radial Flows. |
| Baffle |
A stationary device usually
installed at, or near tank walls to prevent liquid swirl and promote vertical
flow in the vessel. |
| Batch
mixers |
Batch Mixers mix one load
of material at a time and are refilled with one load after another. |
| Batch
Mixing |
Mixing process that
involves the weighing and measuring of ingredients, the creation of a mixture
from separate ingredients, the removal of the mixture and the cleaning of the
mixer and mixing tools before the start of a new batch. |
| Bearing
life |
Bearing life is most often
reported as B-10 life, which is the number of hours of operation under a
given set of load conditions during which a bearing has a 10% chance of
failure. The B-10 life is about one-fifth the average life. |
| Bio-Film |
A layer of trace organic
material that can adhere to the interior wall of process line
components. |
| Blade |
One of the vanes on any
type of impeller, sometimes misused to indicate the whole impeller. |
| Blenders |
Blenders usually mix
miscible substances possessing comparable viscosities. Because substance
properties remain similar, blending can usually be accomplished with relative
ease. |
| Blending |
Mixing two or more miscible
liquid components into a more uniform mass. |
| Breaker
Bars |
Baffles positioned adjacent
to the path of the Impeller or the Paddle to prevent the entire mass from
rotating with the Impeller. |
| Brine |
Mineralized water
consisting of sodium chloride, metallic and/or organic contaminants. Brine
solutions are utilized in food processing procedures. |
| Bulk
Density |
The Density of a granule or
powdered solid material including the voids between the particles. It is
always les than the true Density. |
| Centipoise,
Centistoke |
See Viscosity. |
| Cleanup
Impeller |
See Slinger |
| Colloid |
Fine particles of a
substance that remain between the dissolution phase and the suspension phase.
Colloids neither dissolve into other substances, remain suspended within the
other substances nor settle out of the substances. |
| Consistency |
The resistance of a fluid 1
deformation when subjected to shear stress, usually synonymous with
Viscosity. |
| Continuous
Mixers |
Continuous Mixers are
important parts of large production lines that typically have paddle type
agitators with a series of mixing stages that progressively move and blend
ingredients. Materials are constantly fed in specified proportions into
continuous mixers, then are mixed, conveyed to the opposite end and
discharged. |
| Continuous
Mixing |
Mixing process, involving
the automatic creation of a series of mixtures, in which the mixer contains a
metering mechanism, such as a pump, and measures, combines and mixes the
ingredients. Because smaller amounts are mixed continuously, cleaning of the mixer
and mixing tools usually remains fast and easy. |
| Critical
Speed |
The rotational speed of a
shaft equal to the frequency of the natural harmonic vibration of the shaft. |
| Crystallization |
Formation of a solid phase
from a liquid solution. It is the opposite of dissolving. |
| Curved
Blade Turbine |
A Radial Turbine whose
blades form arcs. |
| Density |
The mass per unit volume of
a substance. See Bulk Density and Specific Gravity. measured in g/cm3 (grams
per cubic cm). |
| Dilant
Fluid |
A material in which the
(Viscosity increases with increasing shear rate. It is the opposite of
Pseudo-plastic.) |
| Dispersers |
Dispersers are single-shaft
mixers that break apart or dissolve solid particles into liquid using a
high-speed, rotating saw-tooth blade. The blade provides high shear forces
that break apart the ingredients of low viscosity products, such as paints. |
| Dispersion |
A two-phase system in which
one phase is broken into discrete particles which are completely surrounded
by the second phase. Particles may be solid, liquid or gas. For Mixing
purposes, the second phase is generally a liquid. Not to be confused with
Solids Wetting. Small particles of a substance evenly distributed throughout
another substance. Dispersed particles are small, but remain larger than
colloids. |
| Dissolving |
A change of phase from
solid to liquid by combining with a liquid solvent. (Opposite of
Crystallization). |
| Draft
Tube |
A hollow stationary
cylinder mounted concentric with and above or around the Impeller to promote
increased vertical fluid flow during agitation. |
| Drive
Unit |
The mechanism in the
Agitator's Power Package which converts motor Torque into shaft Torque. |
| Drum
Mixers |
Drum Mixers have adjustable
blades in a swing-blade design that maximize liquid movement at all speeds. |
| Dry
Well |
A sleeve around the output
shaft of a gear box to prevent leakage of the gear lubricant down the shaft. |
| Drywell |
A weir or hollow quill
designed around the output shaft of a drive unit to prevent leakage of the
gear lubricant down the shaft. |
| Dual-Shaft
Paddle Mixers |
Dual-Shaft Paddle Mixers
are fast mixers that use horizontal rotating shafts with fixed arms and
attached paddle-shaped feet to impact the solids and throw some of them onto
the second shaft, while pushing the rest toward one end of the device. The
paddles on the other shaft push the solids toward the opposite end and toward
the other shaft and paddle set. |
| Emulsifiers |
Emulsifiers provide high
speed rotation and centrifugal force through a perforated screen to achieve
emulsification. Emulsifiers are very effective where a high shear is
required, as they can provide fast mechanical and hydraulic shear |
| Emulsion |
A suspension in which one
substance is suspended within the other. They are unable to be blended or
mixed but can be combined, though not dissolved (e.g. oil and vinegar). A
colloidal dispersion of two or more liquids which are immiscible with each
other. See Dispersion. |
| Equivalent
Impeller Weight |
The weight, which if placed
at the end of a shaft, would have the same effect as one or more Impellers
located elsewhere on the shaft. |
| Equivalent
Shaft Weight |
The effective weight of a
shaft if it were concentrated at the lower end of the shaft, used in critical
speed calculations. |
| Extraction |
A process involving
material transfer from one phase to another. |
| Flash
Mixer |
An agitator used to mix a
small amount of additive into a continuous stream where the Residence Time is
extremely short (usually less than one minute). It most often refers to
addition of chemicals which cause or aid Flocculation in water or waste
treatment operations. A flash mixer is usually used where all of the addition
is at a single point, whereas Rapid Mixers are used where addition is made at
several points in a channel; however, the terms are somewhat interchangeable. |
| Flocculation |
A mixing process whose
object is to cause fine particles to collide and/or Agglomerate to larger
sizes or to adhere to larger particles so they can more easily be separated
from the liquid. |
| Flooding |
In gas-liquid mixing, an
accumulation of gas which collects with in the impeller, reducing liquid
circulation to a small fraction of normal, and thereby reducing mixing
effectiveness. It can also occur when air is drawn into the liquid from the
surface, either from Vortexing or accompanying solids, which are being
wetted. |
| Ford
Cup |
A common tool for measuring
Kinematic Viscosity, used in the paint industry. |
| Full
Vacuum |
A zero pressure on the
absolute pressure scale. Theoretically, no molecules are left in the system;
practically, it is the minimum pressure obtained with the vacuum equipment
being used and should be defined numerically. It is usually 26-27" of
mercury (29.95" = theoretical limit). |
| Fusion |
The melting together of
filler metal and base metal, or of base metal only, that results in
coalescence. |
| Gate
Impeller |
An Anchor type Impeller having additional horizontal and
vertical blades. Gate Impeller |
| Gear
Box Rating |
The horsepower capacity of
a gear box meeting life and strength standards established by the American
gear Manufacturers Association. |
| Gear
Rating |
The horsepower capability
of a drive unit meeting life and strength standards established by the
American Gear Manufacturers Association. |
| Gear
Types |
SPIRAL BEVEL: A
curved-tooth gear form used to connect intersection shafts. |
| Gear
Types |
HELICAL: An angle-tooth
gear used to connect parallel or non-intersecting shafts. |
| Helix |
A type of Impeller
consisting of one or more narrow ribbons which spiral around the shaft,
affixed to arms mounted on the shaft, affixed to arms mounted on the shaft,
and having a diameter near that of the vessel. It is used for high viscosity
liquids or solids. |
| Heterogeneous |
Consisting of different
components that may not be distributed evenly throughout a mixture. The
components, while mixed together, still remain separate entities. |
| High
Shear Mixers |
High Shear mixers utilize
counter-current mixing, which places very high parallel forces upon
substances. During counter-current mixing, the mixing pan and the mixing
tools rapidly revolve in opposite directions, resulting in substance
uniformity. |
| High
Speed Dispersion Mills |
High Speed Dispersion Mills
are continuous mixers that break down particle masses to efficiently provide
fine dispersions and stable emulsions. |
| Hindered
Settling |
Behavior of a Slurry having
a high frequency of particle collisions, evidenced by reduced Settling
Velocity and Non-Newtonian behavior of the Slurry. Generally, it becomes
noticeable at solids concentrations above 40-50% by volume, but may occur at
much lower concentrations if the particles are extremely fine or highly
irregular in shape. Most Non-Newtonian Slurries are Pseudoplastic but a few
are Dilatant. |
| Hold-Up |
In gas-liquid mixing, the
increase in batch volume over the liquid volume, resulting from the gas which
is Dispersed in the liquid. |
| Homogenizing
Mixers |
Homogenizing mixers are
high-shear mixers that subject mixtures of varying viscosities to intense
mechanical and hydraulic forces, reducing mixing time and assuring uniform
blend. |
| Homogenous |
Consisting of identical
components distributed uniformly throughout the mixture. The components no
longer remain separate entities, but have become one entity, as in a
solution. |
| Horizontal
Mixers |
Horizontal mixers have
three or four augers and are used for quick mechanical mixing of particular
substances, especially in feed processing. |
| Impeller |
The part of the agitator
that imparts force to the material being mixed. Examples of impellers are
propellers, turbines, gates, anchors and paddles. |
| In-line
Mixers |
In-Line Mixers are being
used more and more in large volume operations, as they can handle an
extremely large batch with much lower horsepower and with predictable batch
turnover. Dynamic in-line mixers utilize a combination of pump pressure and
high-speed rotating elements, while static in-line mixers have specially
contoured stationary mixing elements located in a tubular housing that serves
as part of the pipeline. |
| Interfacial
Area |
The average total area
between phases in a dispersion. As interfacial area is increased, more power
is required to create and/or maintain it. |
| Involute
Helicoid Worm Gear |
Involute Helicoid Worm Gear
- A high efficiency type of Worm Gearing equivalent to wrapping helical teeth
around a cylinder rather than around the edge of a disc. |
| Kinematic
Viscosity |
Kinematic Viscosity is
reported in manydifferent forms depending on the measuring instrument. It is
convertible into centistokes. Centipoises equals centistokes multiplied by
Specific Gravity of the fluid. |
| Kinetic
Energy |
The use of motion to create
and transmit power. |
| Krebs
Unit (KU) |
A common method of
reporting Consistency of paint and other coatings. |
| Laboratory
Mixers |
Laboratory Mixers are an
integral part of any laboratory or processing environment, as they can
perform a variety of functions, such as mixing, emulsifying, homogenizing,
disintegrating and dissolving. Types of lab mixers include compact,
dual-shaft, constant-torque and high viscosity. |
| Laminar
Flow |
Fluid flow characterized by
long, smooth flow currents, mainly in the same direction as the bulk of the
flow with little interaction between them. See Turbulent Flow. |
| Lifter
Turbine |
A Single Inlet Turbine
which is open at the bottom of the blades. |
| Mechanical
Seal |
A device for sealing
against pressure where the agitator shaft enters the vessel. It consists of
two rings, one of which is stationary and the other rotating with the shaft.
The accurately machined faces of these rings are forced together either by
springs or by the tank pressure. When used to seal vapor (as on top-entering
agitators) the seal must be lubricated by a liquid separate from the tank
contents. For higher pressures, Double Mechanical Seals consisting of two
opposed seals in a pressure-tight housing are used. A pressurized liquid
lubricant and coolant is introduced to or flushed through the cavity between
the seals. Many variations in construction and materials are available to
meet special requirements. |
| Micrometer
or Micron |
A unit of measurement
equivalent to one-millionth of a meter. |
| Mixer |
See Agitator. |
| Mixers |
Mixers create a uniform
mixture from various combined substances. |
| Mixing |
The process of putting
power into a system, usually for the purpose of producing greater material
uniformity. |
| Mixing
Blades |
push materials around the
mixer. |
| Mixture |
A substance containing two
or more substances that may not be distributed evenly throughout and do not
bond together chemically. Substances in mixtures, although combined, maintain
separateness. |
| Motionless
Mixers |
Motionless Mixers are also
known as static mixers, inline mixers and pipeline mixers, are continuous
mixers that operate inline and have no moving parts. Motionless mixers allow
for the blending of two or more fluids and disperse treatment chemicals into
fluid streams. |
| Non-Newtonian |
A fluid whose rate of flow
is non-proportional to the stress applied. The Viscosity is variable and may
increase or decrease with shear rate, with time, or with a combination of
both. See also Pseudoplastic, Thixotropic, Dilatant. |
| Non-Newtonian
Fluid |
A fluid whose rate of flow
is not proportional to the stress applied. The Viscosity is variable and may
increase or decrease with stress, with time, or with a combination of both.
See also Pseudoplastic, Thixotropic, Dilatant. |
| Paddle |
A two-bladed impeller whose
diameter is somewhat larger than the radius of the tank. It is sually greater
than 60% of the tank diameter. |
| Particle
Diameter |
The size to which the
individual bodies of the dispersed phase are reduced in a two-phase
Dispersion. Often called drop diameter if the dispersed phase is a liquid or
bubble diameter if the dispersed phase is a gas. The smaller the particle
size, the larger the Interfacial Area. |
| Paste
Mixer |
A mixer with a modified
Anchor Impeller, having several vertical bars or fingers which intermesh with
stationary Baffles extending down from the tank top. Used to make low to
medium Viscosity pastes such as caulking compound. |
| Pharmaceutical
Mixers |
Pharmaceutical Mixers are
used in processing a variety of liquids, powders and crystalline solids in
the pharmaceutical processing industry. Common applications that utilize
pharmaceutical mixers include the mixing of medicine, such as cough syrups
and the creation of tablet coatings for pills. |
| Pitch |
For a turbine, the angle
the blades make with a horizontal plane. |
| Poise |
The absolute unit of
Viscosity in the C.G.S. system. One Poise equals one dyne-second per square
centimeter, equals one hundred Centipoises. |
| Power
Number |
A dimensionless ratio used
in calculating Impeller power loadings. Impellers of similar design but
different sizes will have equal power numbers under dynamically equal
conditions. |
| Power
Package |
The portion of an Agitator,
normally above the vessel, to which the Agitator shaft is coupled. It
converts power into the mechanical energy for mixing. |
| Production
Mills |
Production mills are
efficient, high-speed dispersion mills that can quickly disperse, emulsify,
suspend, cook, aerate and deaerate masses of particles. Material can be put
in the production mill through radial slots where they are hurled off the
slot tips against the stator slots, which produces efficient wetting-out of
the solid phase and the quick achievement of stable suspensions, dispersions
and emulsions. |
| Progressive
Polishing |
A mechanical grinding
procedure where a coarse grit material is used first and the successive
operations use finer and finer grit until the desired surface roughness is
achieved. |
| Propeller |
A three or four bladed
Axial Flow Impeller, having helically shaped blades. |
| Proportional
Mixers |
Proportional Mixers
properly mix concentrations of water to produce working and make-up solutions
for applications that include coolants, cleaners, strippers, degreasers,
fertilizers and fungicides. Venturi proportional mixers use water passing
over an orifice to create suction to draw the concentrate from the container
and mix it with water, while water-driven mixers use water to drive a piston,
which then pumps concentrate into a mixing chamber where the concentrate is
mixed with water. |
| Proximity
Factor |
A correction factor used in
Impeller power calculations to account for geometric variations, such as
Impeller-to-tank bottom distance, Impeller-to-liquid surface distance,
multiple Impeller spacing, etc. |
| Pseudoplastic
Liquid |
A liquid or slurry in which
the apparent Viscosity decreases with increasing shear rate. |
| Pumping
Rate |
The volumetric discharge
rate of an Impeller operating at a given speed, measured at the Impeller. |
| Radial
Flow |
The movement of a fluid
generally from the center of the tank to the wall. |
| Radial
Turbine |
A turbine whose blades are
vertical and whose discharge creates Radial Flow. |
| Rapid
Mixer |
See Flash Mixer. |
| Residence
Time |
The average time a process
component remains in the mixing environment in a continuous process. |
| Reynolds
Number |
A dimensionless number used
to characterize fluid flow data. The ratio of inertial to viscous forces. |
| Ribbon
Mixers |
Ribbon Mixers create an
extremely diverse velocity field by using a counter-transport mechanism
consisting of an outside right-hand ribbon and an inside left-hand ribbon,
both connected to the same horizontal shaft. Ribbon mixers provide fast
blending and mixing in the vertical plane, as they can transport an entire
mass of solids a short distance in both directions of the axis of the shaft
while lifting a portion of the solids a short distance in each direction;
however, they are slow when mixing end to end. |
| Rotary
Drum Mixers |
Rotary Drum Mixers contain
blades that spin around the axis of the drum, mixing the substances, such as
concrete. Drum mixer axes may be either horizontal or inclined. |
| Rotor
Stator Technology |
Rotor Stator Technology
includes high-speed mixers that utilize a rotor and stationary stator to
produce high rotor tip speeds. The differential speed between the rotor and
the stator in these mixers imparts extremely high shear and turbulent energy
in the gap between the rotor and stator. |
| Saybolt
Seconds Universal (SSU) |
A method of reporting
Kinematic Viscosity, most common in the petroleum industry; 100 centistoke:
equals 462 SSU. |
| Scrapers |
Flexible or hinged members
attached to the outer periphery of an Anchor Impeller to scrape the vessel
wall, preventing buildup and improving heat transfer. |
| Service
Factor |
A numerical rating system c
gear trains based on operating time, type of drive and duty required. See
Gear Rating. |
| Settling
Velocity |
The velocity attained b a
particle freely falling in a fluid due to gravity. See Terminal Settling
Velocity and Hindered Settling. |
| Shear |
As applied to liquid
mixing, it is that portion of the applied power, which appears as turbulence,
velocity head, recycling, drag on the blades, etc. It is the action, which
produces intimate mixing on a microscopic and molecular scale. |
| Single
Inlet Turbine |
A Radial Turbine with one
face shrouded for the purpose of controlling the direction of fluid flow. See
Lifter Turbine. |
| Size
Reduction |
The breakdown of immiscible
particles in a mixture that cannot be dissolved. |
| Slinger |
A device attached to a
shaft above the liquid level to prevent the liquid from climbing or splashing
up on the shaft. Also a small Impeller placed as low as possible in a tank to
agitator the "heel" when the tank is nearly empty. Sometimes called
a Cleanup Impeller or heel agitator. |
| Slurry |
A mixture of liquids and
insoluble solids; a Solid Suspension. |
| Solid
Suspension |
The mixture of an insoluble
solid material in a liquid. Thee are three degrees of suspension used in
mixing: (1) "complete motion" wherein all solid particles are
merely maintained in motion; (2) "complete suspension" wherein the
solid particles are all lifted from the bottom but not necessarily to the
top; and (3) "complete uniformity" where the heavies particles
break the surface frequently and particle distribution is uniform through all
but the top 3 to 5% of the liquid. See Hindered Settling. |
| Solids
Wetting |
Dispersing solid particles
so that a liquid film coats each particle |
| Solute |
In a solution, the liquid,
gaseous or solid substance or substances that dissolve into a liquid or
gaseous substance, called a solvent. Solutes usually consist of smaller
quantities than the substance into which they are dissolved. |
| Solution |
A homogenous formation
created by the dissolution of a substance or substances into another
substance. |
| Solvent |
The liquid or gaseous
substance into which a liquid, gaseous or solid substance, known as a solute,
is dissolved. |
| Sparger |
A pipe or pipe construction
for introducing fluid below the liquid surface in a tank; most often a ring
or spider with many small holes, located below the Impeller, through which
gas is bubbled. |
| Specific
Gravity |
The Density of a material
compared to the density of water at standard conditions. In the metric
system, water has a density of 1 gram/ml, so density and specific gravity are
numerically equal. |
| Stabilizer |
A device attached to an
Impeller which directs the fluid flow pattern generated by rotation so as to
resist shaft deflection, thereby allowing the use of longer shafts without
Steady Bearings |
| Static
Mixers |
Static mixers are also
referred to as in-line mixers, are motionless mixers that operate
continuously. Static mixers remain quite efficient and generally require very
little maintenance. |
| Steady
Bearing |
A radial shaft support
bearing mounted in the vessel bottom used to reduce deflection in long shaft
installations. Sometimes called a "foot bearing". |
| Stuffing
Box |
A device for sealing
against pressure where the agitator shaft enters the vessel. It consists of a
stationary tube around the shaft with several rings of close fitting braided
fibrous packing in the annular space between the tube and shaft. Usually
included are means to lubricate the packing, a lantern ring to store and
distribute lubricant, and a follower or glad to compress the packing further
as it wears. Many special variations or features are available. |
| Superficial
Velocity |
An average velocity value
used in computations of fluid flow due to the complexity of velocity
distribution in the system. Usually encountered in gas-liquid systems, where
it is the volumetric gas flow-rate divided by the cross sectional area of the
tank. |
| Suspension |
A heterogeneous mixture in
which fine particles of a solid neither dissolve into a liquid or gaseous
substance nor settle out, but remain within the substance supported by
buoyancy. In suspension, both substances remain separate entities. |
| Swirl |
The rotation of a liquid
about an agitator shaft where little relative motion within the liquid is
obtained. |
| Thixotropic |
A material whose Viscosity
drops gradually at a constant shear rate, as opposed to materials whose
viscosity changes instantaneously with changing shear rate. When shear is
removed, Viscosity of Thixotropic materials gradually increases again. These
materials may also be Pseudoplastic or Dilatant. |
| Torque |
The torsional moment
exerted by a body (such as an Impeller) rotating at constant speed. |
| Turbine |
A multibladed (usually four
or more), relatively short armed Impeller. The impeller diameter to tank
diameter ratio usually varies from 0.2 to 0.5 for turbines. |
| Umbrella
Seal |
A liquid "trap"
around a shaft to prevent vapor leakage from the vessel, used only in very
low pressure systems. |
| Vacuum
Mixers |
Vacuum Mixers have either
top- or bottom-mounted mixers and are used to eliminate air pulled into the
material during mixing, which increases product quality. |
| Viscosity |
The measure of resistance
of a fluid to flow when a force is applied to it. See Apparent Viscosity.
ABSOLUTE VISCOSITY is usually measured in centipoises (cp.). Water at room
temperature has a viscosity of 1 cp. KENEMATJC VISCOSITY is reported in many
different forms depending on the measuring instrument. It is convertible into
centistokes. Centipoises equals centistokes multiplied by Specific Gravity of
the fluid. |
| Viscosity
Factor |
The correction factor
applied to standard Impeller power draw to account for the difference caused
by high liquid Viscosity. |
| Vortex |
A depression occurring in a
liquid surface when an agitator Swirls the liquid; a whirlpool. |
| Water
Horsepower |
The standard brake HP an
Impeller will draw when operated in a water-like liquid (Viscosity = 1
centipoise, Specific Gravity = 1.0) under standard conditions of Baffling and
geometric arrangement. |
| Wetting |
See Solids Wetting. |
| Worm
Gears |
A gear form used for
obtaining large speed reduction between non-intersecting shafts whose axes
are at a 90° angle from each other. |