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Optimization
of Dispersion
Processes
for Liquid Inks
By
Gisbert Schall & Edward Casama
Printing
inks are used to convey a message or to decorate. Because of the
special requirements, such as visual appearance, printing process,
drying systems and other conditions, different types of printing
ink systems and formulations have been developed.
The intent
of this paper is to deal with optimization of dispersion processes
for liquid ink systems, namely Flexographic and Gravure inks.
The main
components of liquid inks:
Pigments,
Resins,
Solvents & Additives
are manifold,
due to the different substrates and end uses. Almost any kind of
substrate from newsprint to coated papers, paper and containerboards,
to flexible films and foils, can be printed.
Therefore,
ink formulations and dispersion processes are of greatest importance.
Inks which
are printed by the Flexographic and Gravure printing processes are
characterized by their extremely fluid nature, hence the name, liquid
inks. The fluidity of Gravure inks allows the recessed cells of
the gravure cylinder to be filled rapidly. Similar fluidity is required
for the Flexographic process as the inking systems depend upon an
engraved cylinder metering the printing ink onto the raised rubber
image.
Highly volatile
solvents are used and most Flexographic and Gravure inks are fast
drying and therefore, the ink is transferred to the substrate as
quickly as possible.
Liquid inks
are formulated to dry by the physical removal of the volatile solvents
from the ink formulation. The pigment is bound to the substrate
by the resin material. The rate of drying depends upon the evaporation
rate of the solvents selected. Evaporation (Fig.1) of water or solvents
in ink depends primarily on the vapor pressure of the vehicle utilized.
The choice of vehicle systems is determined by the materials of
the printing plate, speed requirements and nature of the substrate.

Figure
1. Surface action of liquid ink curing (Evaporation)
Schematic diagram of ink drying by
evaporation The volatile solvents evaporate, leaving a dry ink film
on the printed stock. Evaporation is usually speeded by application
of heat and air.
Most evaporation
inks consist of such solvents as hydrocarbons, alcohols, ketones
and esters and synthetic resin or cellulosic material, which acts
as a binder to hold the pigment to the substrate. Evaporation can
be speeded up by using infrared lamps or by flushing the vapors
by gas jets.
Each type
of ink requires a very careful balance of properties to meet the
requirements of the printing process and the end use of the printed
article.
An ink will
exhibit a good adhesion to the substrate if the pigments are properly
dispersed.
In the Gravure
process, printing is achieved by passing the substrate between the
Gravure cylinder and an impression roller. The substrate is fed
from reels into a nip between the edged cylinder and a rubber covered
impression roller, which supplies the pressure needed to transfer
ink from the cells to the substrate.

Figure
2. Grainting Process
The printed
web runs upwards through a heated drying system where the solvents
are evaporated and extracted. In Gravure printing, each color must
be nominally dry before the succeeding color is printed over it,
therefore, each printing station has its' own individual drying
equipment. The Gravure ink, which usually stored underneath each
unit, is pumped up to the ink trough and usually ink viscosity control
is incorporated in such systems.
In the Flexographic
printing process, the printing images stand up in relief, similarly
to the letterpress process. Low printing pressure is essential to
the process because of the combination of very fluid inks and solt
and flexible printing plates. Rapidly, drying liquid inks are utilized;
therefore, fast-printing speeds can be achieved on non-absorbent
materials, such as films and foils.
For high
quality Flexographic printing, the printing unit is built to very
tight tolerances. Te ability to manufacture to these standards is
one of the factors which is contributing to the current growth in
Flexographic printing in its' use for higher quality product.

Figure
3. Flexographic Printing Process
Printed
images are given color by pigments that are substantially insoluble
in the vehicle and in water. In addition to color, pigments determine
such ink properties as bulk, opacity, specific gravity, viscosity
and yield value. Pigments are finely divided particles, when adequately
dispersed in the medium, absorb and scatter light. If the absorption
is selective, the pigmented will be colored. Pigments may be entirely
inorganic or organic, they may also be metallic salts of complex
acids, or consists of organic dyes laked on to inorganic substances.
Pigment opacity depend normally upon its' ability to scatter incident
light, but absorption also plays a part and the overall opacity
is due to combination of both properties. In the case of titanium
dioxide, little or no absorption occurs, and opacity is due almost
entirely to scatter. On the other hand, as the refractive index
of a pigment approaches that of the medium, in which it is dispersed,
the amount of light scattered decreases and the pigment becomes
more transparent. Transparency of a pigment therefore is partially
dependent upon the medium used o disperse it.
The tinting
strength of a pigment is a measure of its' ability to impart color
to a system. The color strength of a pigment is primarily related
to chemical composition, particle size and distribution. In the
case of printing ink, the actual value will depend also upon the
film thickness and concentration of pigment in the in the ink. Most
printing inks are more or less transparent. The substrate will influence
the final color of the printed matter.
The film
forming materials of liquid inks are typically solvent/resin vehicles,
which cure by evaporation. In Gravure inks, low boiling hydrocarbon
solvents are generally used with gums and resins. Flexographic inks
normally contain alcohols, water or other fast evaporating solvents
mixed with suitable resins and/or gums.
Resins contribute
to the properties of hardness, gloss, adhesion and flexibility in
the ink. Resins are of two types, natural and synthetic. Synthetic
resins are prepared by polymerization involving condensation or
addition reactions between relatively small molecules.
Solvents
used in liquid inks are capable of dissolving another substance,
such as resins to form a solution. They are used to dissolve materials
in the vehicle, assist in the dispersing of the pigments and additives
and to adjust viscosity. Combinations of solvents are often selected
for different types of ink on the bases of printability, drying
speed, economy and odor. Flexographic and Gravure inks contain as
much as 80% organic solvents. Gravure inks usually employ one solvent,
either xylene or toluene. The printing of solvent-based inks is
under regulation to control solvent emissions to the atmosphere.
INK
MANUFACTURING PROCESSES
The manufacture
of printing ink is a technologically advanced, highly specialized
and complex process. The manufacturing systems utilized in the process
depends upon the volume of the particular ink to be manufactured,
the properties of the materials in the formulation and the end use
requirements of the printing ink. Essentially, printing ink manufacturing
is the combining of the basic ingredients such as pigments, vehicles
and additives in such a manner so that the ink will meet its' product
specifications required for its' intended use. A number of printing
inks are completed in a one or two-step mixing/dispersing process
because pigments are purchased in such pre-dispersed forms as chips,
bulk or other wetted forms.
Gravure
inks or Flexographic inks are typically prepared by a combination
of batch and continuous processing in totally enclosed media mills,
sometimes even stir ball mills. These types of inks are to be processed
only in totally enclose dispersion systems because of the very volatile
nature of the solvents used.
As the pigment
in most printing inks is the most expensive part of the formulation,
economics of pigment selection and proper dispersion equipment,
is vital importance. In the case of Gravure inks, the process of
dispersion of the pigment into the vehicle system can be achieved
by a number of different manufacturing techniques. Here, the relationship
of the dispersion process to the end properties of the ink is of
great importance. The options available for dispersion of the pigment
range from the use of chips and pre-dispersed pigments to conventional
dispersion methods in equipment such as small media mills, ball
mills or sometimes, high speed dispersers.
The uses
of pigment chips and to a lesser extent, pre-dispersed pigments,
tend to produce short thixotropic inks with very high gloss and
transparency. Dissolving the pigment chips or pigment paste is usually
carried out on a high shear mixer, suitable to produce ink with
acceptable dispersion. There are advantages in using pigment chips,
particularly with pigments that are difficult to grind.
The high
cost of the pre-dispersion process, together with shortness of the
flow, which places a limit on ink strength attainable, means that
such techniques are normally used only when no other option is feasible.
The most common process for the production Gravure inks is dispersion
of the pigments utilizing a small media mill. Different media mills
are available which enable different diameter bead sizes to be utilized.
In general terms, the smaller the bead size, the better the dispersion.
Alterations in milling conditions will give rise to variations in
quality of dispersion, therefore, they have carefully monitored.
While dispersion
process represents a major part in producing dispersion, there is
considerable influence and inner dependence between the binder,
pigment and solvent. All are equally important to the final result,
particularly with respect to the dispersion stability. Finding the
optimum conditions and formulation balance for maximizing dispersion
can be time consuming with many experiments required.
Ink makers
are required to provide consistent quality and quick delivery. Moreover,
the ink maker must cater to a wide variety of requirements. Therefore,
flexibility in formulation and dispersing methods has to be retained.
The basic
need to grind out pigment agglomerates/aggregates represents a high
share of the cost in making printing inks. Therefore, it is imperative
to continuously improve and further develop the process of pigment
dispersion. These efforts concentrate on improving:
a) Pigment dispersability
b) The efficiency of available wet grinding and dispersing equipment
The physical
properties of pigments such as particle size and particle surface
are of great influence in the dispersion process. Primary dispersions
for ink production demand that the pigment particles are thoroughly
wetted by the liquid phase and that the particles in the finished
ink are in a size range of 1 micron to 5 microns maximum. If this
dispersion level is not achieved, printing problems will arise.
Pigments
such as those mostly used for printing inks typically are crystalline
solids. They usually feature primary particle sizes of 0.5 micron
or providing for specific surface areas of 30 to 100 square meters
per gram.
Pigments
are generally precipitated from aqueous solutions. At the time of
chemical reaction causing the precipitate, these particles are molecular
in size. The molecules of the pigment are strongly attracted to
each other by physical forces and immediately from larger pigment
particles, the size of which will depend on the nature of the material
and the physical conditions existing at the time reaction. The primary
particles cluster together during processing to form agglomerates
/ aggregates. The particles in agglomerate / aggregate form are
strongly bound together and high energy is required in the dispersion
process to break them down. A dried press cake will contain a mixture
of primary particles, aggregates and agglomerates. The presscake
is normally crushed to reduce the size of the largest agglomerates,
providing what appears to be a fine powder. It is the most important
part of the dispersion process to break down these large particles
exposing a greater surface area of pigment to the wetting medium
in order to produce a finished, evenly wetted product. There are
several routes by which ink dispersions can be produced. While there
are similarities in the way the individual types on inks are made,
and since much of the machinery involved is also similar in concept,
there are distinct differences between them. The primary purpose
of the dispersion process is to break down pigment aggregates and
agglomerates to their optimum pigmentary particulate size and distribute
these pigment particles evenly throughout the similar medium i.e.
the carrier. To achieve the optimum benefits of a pigment, it is
necessary to obtain as full a reduction as possible to the primary
particle size. The color strength of a pigment depends on its' exposed
surface area, and the smaller the particle size, the higher the
surface area and thus the stronger the color. Also, the pigment
is generally the most expensive constituent of any printing ink;
therefore, one would normally want to obtain optimum performance
with the least amount of pigment. Ideal pigment dispersion consists
mainly of primary particles with only a minimum of loose aggregates
and agglomerates.
In practice,
reduction to the primary particle size is largely determined by
the nature of the pigment, the dispersion system and processing
equipment and by the end use requirement of the printing ink. As
pigment agglomerates are broken down, larger and larger pigment
surfaces are created. At this point, relatively powerful short range
surface energy to re-form pigment particle agglomerates or aggregates.
To prevent this re-agglomeration, it is imperative to neutralize
the surface energies through a suitable stabilization process. Dispersions
of pigment in organic solvents are stabilized by a mechanism known
as steric stabilization. This effect occurs when a suitable dispersion
is absorbed onto the particle surface by the "anchor group" portion
of the dispersed molecule, while the remainder of the dispersed
molecule remains in solution in the solvent.
DISPERSION
PROCEDURE
The dispersion
procedure is the most important part in the field of wet grinding.
Normally, this process is divided into four distinct stages, namely:
a) Separation
b) Wetting
c) Distribution
d) Stabilization Separation
Separation
Separation
means not only commutation of large primary pigment particle agglomerates
or aggregates under mechanical stress, but also the dispersion of
agglomerates and aggregates into the single constituents of primary
particles and aggregates. This process is also referred to as dispersion/grinding.
Wetting
Wetting
means that portion of the process in which a liquid spreads over
the surface of a solid particle or the penetration of agglomerates
through a liquid. This involves the removal of absorbed molecules
of gas (air) liquid or other materials from the surface of the pigment
particle and their replacement with molecules of the vehicle system.
Therefore, wetting efficiency depends upon the comparative surface
tension properties of the pigment and the vehicle system.
Distribution
Distribution
is the process of balancing the concentration of the separated pigment
particles within the carrier liquid. Homogenous distribution of
the pigment particles throughout the vehicle system is usually achieved
by mechanical action, mostly in small media mills, such as Perl
mills, so called because the grinding media are spherical beads
made of glass, ceramic or metal.
Stabilization
Stabilization
is the process responsible to retain the quality of separation and
the grade of wetting achieved within the vehicle system. If the
pigment dispersion has not been stabilized, flocculation can occur
from powerful short-range forces. A properly designed dispersing
process combined with an adequate formulation will prevent flocculation.
Since an understanding of the mechanism of steric stabilization
has developed, new dispersants have been designed providing for
far superior performance, compared to previous systems.
Simultaneous
Process
The four
stages of the dispersion process occurs simultaneously rather in
sequence. Again, the primary purpose of the dispersion process is
to break down pigment agglomerates and aggregates to their primary
particle size and distributes these pigment particles evenly throughout
the vehicle system.
There are
two main types of formulation for liquid inks, water based and solvent
based. The volatile nature of the liquid phase of both solvent and
water-based inks requires similar manufacturing techniques, but
they are often produced in separate units to avoid contamination.
The flammable nature of a large number of solvents used requires
special precautions to prevent the risk of fire and explosion. Generally,
the optimum manufacturing path for manufacturing of liquid inks
consists of high speed mixing, followed by small media milling and
filtration. Also, liquid inks can be made by utilizing conventional
ball mill technology.
Wet grinding
and/or dispersing of pigments in liquid ink vehicles can be achieved
in a large variety of machines. However, a very economical solution
is to employ an equipment combination consisting of a high-speed
disperser and a small media mill. This typically is a three-stage
process, consisting of:
a) Pre-mixing
b) Wet grinding/dispersing
c) Let down adjustment
While the ball mill may be considered as an original totally enclosed
system for manufacturing liquid inks, the introduction of small
media mills gave opportunities for introducing faster and continuous
production methods. Bulk amounts of concentrates and inks can be
manufactured from dry pigment and vehicle systems using a combination
of mixers and media mills. The typical process entails:
a) Weigh
out pigment and vehicle system and pre-mix on a high speed disperser,
b) Disperse the pre-mix on a small media mill,
c) Add additives and solvents in a high speed mixer,
d) Filter and pump to the storage tank after quality control procedures
are completed.
Small
Media Mills (PERL MILLS)
Agitated
bead mills are mostly used in modern wet grinding and dispersing
processes. This mill system is firmly established in the making
industry. In most industries it has prevailed over other grinding
and dispersing systems, such as ball mills, roller mills, rod mills
and similar machines long employed in the past for the wet grinding
and dispersion of solids in liquid vehicles. Modern agitated bead
mill are widely used in different industries for demanding grinding
and/or dispersing applications. The basic principles of small media
mills have been known for almost 60 years.
Industrial
breakthrough of high-speed media mills occurred in 1948 with the
introduction of Dupont' s sand mill, which has been used within
the paint and coatings industry primarily as a pigment grinder.
NEW
DEVELOPMENTS
In recent
years remarkable developments have taken place to favorably adapt
small media mills for the fine grinding needs of many industries.
As a result, there are many different types of small media mills
available today. Specific design features allow for milling processes
not conceivable some years ago. In recent years, the applicability
of small mills has been extended to coarser feedstock and to finer
product particle sizes. This development has been made possible
by design and process innovations, such as the invention of new
agitating and media separating systems and a device for continuous
grinding processes that avoids separate premix preparation completely.
In the past,
primary particles, which were considered indivisible by media milling,
have successfully been ground to primary pigment particle size via
special new mill designs. Spectacular results can be achieved with
a specially designed bead mill when it is properly operated with
250 micron grinding media. The conversion of crude pigments to finished
pigment dispersions is an example.
ENERGY
CONVERSION
From general
point of view, fine grinding, as well as dispersing, must be viewed
as an energy converting procedure. Typical applications require
that internal mill conditions be created in which the local energy
density is above the minimum required for grinding process. Since
the energy introduced into the system is mostly converted into heat,
special consideration must be given to efficient heat removal/exchange.
This is particularly important since practically all processes require
product temperatures that can be confined to predetermined limits.
HIGH
SPEED MILLS
The introduction
of high-speed agitated media mills represented a great advance in
standard manufacturing methods. The essential features of these
mills are high agitator speed and the use of small attritive elements
for particular purposes. One can increase grinding performance by
reducing the diameter of the balls, thereby increasing the number
of points contact. Modern high-speed units use this finding to the
ultimate extent.
The Perl
Mill is characterized by very small grinding particles, which are
largely spherical in shape. These perls or beads are made of glass,
ceramic or metal and are accelerated to approximately up to 200
times gravity.
REDUCED
MEDIA SIZE
With a reduction
in the size of grinding media in a media mill, the number of contact
points is increased exponentially resulting in improved grinding
and dispersing action. Furthermore, when grinding media in the 250-micron
range is used, processing of crude pigments into directly highly
loaded pigment dispersions can be accomplished in a single step
process, which may eliminate intermediate pigment preparation stages.
IMPROVED
COST EFFICIENCY
With an
improved grinding procedure manufacturers of high quality printing
inks can realize substantial cost savings by using less costly raw
materials (pigments). Also, improved dispersion can be achieved
resulting in higher pigment yields.
HORIZONTAL
vs. VERTICAL
Small media
mills can be operated either horizontally or vertically. The preferred
orientation depends upon product and process related parameters
such as viscosities, feed rates, size and density of grinding media.
As a basic rule, the most advantageous grinding chamber orientation
is the one that results in an equal media distribution within the
grinding chamber. Opinions vary considerably as to whether the grinding
chamber should be vertical or horizontal arrangement. There are
no hard and fast rules, but the following comments apply generally.
In spite off the differences in designs, both vertical and horizontal
grinding chamber arrangements provide equal grinding efficiency
in wide fields of applications.
Vertical
Mill
When a structurally
viscous product, flush base printing ink for example, is to be processed,
experience has shown the vertical mill to be advantageous because
the force of gravity counters the accumulation of grinding beads
at discharge point. It thereby makes for more uniform distribution
of the grinding media within the mill chamber.
Horizontal
Mill
The benefit
of the horizontal arrangement, on the other hand, is the ease with
which the filled bead mill can be restarted after stoppage. For
applications where the product has a medium to low viscosity, the
horizontal mill definitely provides an advantage since gravity is
basically eliminated and the grinding media is more uniformly distributed
throughout the grinding chamber. Therefore, the grinding media is
being totally activated without densification on either end of the
mill chamber. Naturally, there are other considerations for giving
preference to one or other design.
DIRECT
DISPERSION SYSTEM
For standard
machines, it is necessary to prepare premixed slurry in order to
feed the agitated media mill. Since the development of the Direct
Dispersion System, it is possible to operate agitated media mills
continuously, without premixing or pre-dispersing solids and liquids.
The DDA
system features a specially designed feeding screw, which is flanged
on directly to the grinding chamber. This can produce superior product
quality at reduced operating costs, because of the constantly maintained
processing parameters. Such systems are successfully employed in
the printing ink, magnetic media and chemical industries.
The grinding
chamber can be positioned either in vertical or horizontal design.
The system applied to the entire line of DRAIS Perl Mills. The output
rate and fineness of finished product is controlled mainly by the
residence time of the material in the grinding chamber.
Control
functions of the Direct Dispersion System are performed steplessly.
The solid and liquid constituents of a formulation meet for the
first time at the right formulation ratio under intense mixing,
grinding and shear forces. This prevents the forming of any so-called
"secondary agglomerates". For example, the Direct Dispersion System
can be applied to disperse, fully continuously pigments such as
carbon black pellets in highly viscous polymers. Today Perl Mills
of the Direst Dispersion Design are also in operation for the production
of adhesives and sealants, successfully replacing batch type kneaders.
The system
processes, with equal efficiency, materials that are not readily
flowable, inadequately wetted or completely dry. The Direct Dispersion
System also proved to be highly advantageous for large scale processing
of materials not readily wettable or containing components that
tend to settle out rapidly.
Because
only small amounts of product are being introduced into the mill
at any given time, large tanks for mixing, dispersing or material
handling are not required. The system lends itself to total automation
and computerization and therefore allows for precise process controls.
SPECIAL
CONSIDERATIONS
The different
stages of liquid manufacturing have to be addressed separately.
For the first stage the formulation of the printing ink has to be
such that the amount of vehicle system required wetting out the
pigment properly has to be assured. Also, very important, is the
proper pigment / vehicle ratio for optimum dispersion and the next
state in the small media mill. Lately, the increased availability
of easily dispersible pigments provides fro much less problems in
the media mill dispersion step. The next step of adding the remainder
of any vehicle portion and solvents to adjust viscosity together
with other additives not suitable for the intense grinding process
should also include final quality control check. The last step of
filtering the ink should prevent any chance of contaminating the
final product. Therefore, the ink is filtered through a fine mesh
filter. This could be sometimes a multistage process, especially
if the printing ink is held in stock for any length of time.
Finally,
we would like to add the two latest developments in processing of
liquid printing inks, namely the new DRAIS DCP Mill, and totally
automated ink-manufacturing process by the DRAIS SOM Computer System.
While the newly developed DCP mill system is usable for the entire
range of printing inks, special considerations have been given for
liquid inks, and also to liquid inks by replacing the conventional
pigment chip process.
For the
achievement of outstanding quality characteristics of liquid inks,
particularly special Gravure and Flexographic inks, it is state
of the art to use high quality pigment chips. For the following
reasons, however, the chip technology is getting more and more problematic:
a) Stock
keeping
b) Availability
c) Cost situation
d) Danger potential (in chip production)
This is
why attempts have been made for a long time to achieve the gloss
and transparency values, which are characteristics of chips, by
direct wet dispersion of powdered pigments.
DRAISWERKE
has achieved the decisive break through in solving this problem.
The advantageous process technology is made possible by the use
of the newly developed DRAIS agitated media mill series PM-DCP.
Typical
Constructional Features
- Energy input by a
large number of turbulence pegs (rotor-stator principle)
- Grinding media separation
by centrifuging
- Defined product transport
by internal series connection of two grinding chambers
- Small mill volume,
easy to clean
- Large surface area
for heat exchange
These features
enable the effective use of extremely small grinding beads at highest
volumetric energy density in the system of up to 6 kW per liter
product to be dispersed. In spite of this, remaining below the dispersing
temperatures, which are critical for NC inks, is no problem at all.
Even pigments
considered very difficult to disperse can, in a highly economical
process, be refined in liquid inks in such a way that the quality
standards of chip-based inks are matched, if not even exceeded.
The new DRAIS agitated media mill generation PM-DCP has additionally
proved its' outstanding performance in raising the quality level
of standard inks drastically. For water-based inks, the same excellent
results are achieved as for inks on the basis of organic solvents.
The better development of desired coloristic characteristic, especially
the color strength, enable interesting savings of raw materials.
In connection with unusually high throughput rates in relatively
small mill units, which are easy to clean, the innovative dispersing
technology of DRAIS introduces a system in the manufacture of liquid
inks, which is unequalled in economical respects.
Increasing
demands on quality printing inks regarding the development of coloristic
characteristics such as gloss, transparency or color strength require
the use of more effective dispersing techniques.
For securing
the quality level as it has been achieved by newly developed dispersing
machines and techniques, the use of an intelligent measuring, control
and regulating technology is indispensable.
Moreover,
there is an increasing desire to use production plants in night
operation without supervision.
To solve
this problem in an economical way, DRAISWERKE has developed a modular
control and regulating system for Perl Mills. The compact process
computer SOM 10. With keypad and LED display enables the functions:
- Operation
- Indication
- Supervision
- Control
- Regulation
- Communication with
central computer
At the most
sophisticated stage of expansion, the mill regulation is done according
to a patented process. As essential measured values, the power consumption
of the rotor, the product flow rate as well as the product discharge
temperature are taken into account. Regulated values are the pump
speed, the rotor speed and the cooling agent flow rate. The system
works in a self optimizing way in so far as a maximum throughput
rate is automatically set while at the same time an even distribution
of the grinding media is secured and the product outlet temperature
as well as the mass specific energy input are regulated to pre-selectable
parameters. Thus, a constant, reproducible product quality is guaranteed
at any time.
All operational
data, limit and alarm values, which are relevant for the dispersion
of a product, are filed in the data store of the computer. By selecting
a particular product code, the corresponding data record is loaded
in the working store. The fully automatic mode of operation comprises
the starting cycle, the optimized production as well as the stopping
and rinsing cycles.
All the
parallel working dispersing lines are operated from a central control
room. All information on the operating states of a production are
indicated and filed by a superset visualization and recording system.
The concept is most suitable for both the automation of the batch
size manufacture of e.g. Flexo / Gravure inks and the fully continuous
dispersing of e.g. web offset inks.
The elimination
of undesired states, found in manual operation, guarantees an absolutely
constant, reproducible product quality at maximum utilization of
the plant capacity, which makes this system highly economical.
Modern
Production Trends Also Include the Computerization of the Processing
Systems
The computer
is already an established tool in ink manufacture. The routine procedures
of preparing manufacturing instructions, processing of orders, stock
control, etc. are carried out at high speed and high efficiency.
The latest advances in computer and microchip technology are automating
ink manufacturing as a whole. Quality ink producers are adapting
more automated and computer controlled manufacturing methods. While
production costs are ultimately greatly reduced, one of the major
reasons to employ new technologies is achievable consistent high
quality of the printing inks. With DRAISWERKE's SOM System, greatly
enhanced product qualities and consistencies can be achieved.
SUMMARY
An attempt
has been made to describe the dispersion of pigments in vehicles
and the process equipment mostly utilized especially in view of
liquid ink manufacturing. All discussion of dispersion stabilization,
in view of hyper dispersants, has been avoided since this is a field
onto itself. There is no question as to the desirability and effectiveness
of a fully dispersed and stabilized pigmented system. Such dispersion
brings out the optimum color properties of the pigment in terms
of color strength, gloss, transparency and rheology. When a pigment
is completely dispersed it contains a large number of primary particles
and therefore, a lesser amount is required to produce the necessary
coverage and color strength than one which is not as well dispersed
and contains a larger number of aggregates/agglomerates and flocculates.
The trend today is toward production of more easily dispersed pigments.
Pigment manufacturers always are improving pigment dispersability
through the use of surface treatments. There has been increase in
the use of plastic films and foils for packaging. Thin films of
ink, if they are to provide greatest gloss and clarity of color
for these applications, require very small particle sizes and complete
wetting of the pigment by the vehicle. As the requirements of inks
increase, efforts also will increase to use of the entire pigment
surface. This becomes more and more important as the price per pound
of pigment rises. More costly pigments, with greater stability,
can be used when this newly developed dispersion processes, as discussed
before, has released all of the color and prepared the pigment surface
correctly for its' ultimate application. Surely, the future will
bring more efficient dispersion equipment as well. From the process
equipment side, the main target is the constant mass specific energy
input into a dispersion system under optimized conditions. This
will allow full utilization of dispersion equipment capacity. Such
processing systems allow for attaining the highest product quality
and minimum operating costs. Recent successes and ongoing development
work in the field grinding/dispersing technology (equipment and
process related) are essential pre-requisites in order to convert
any possible progress in raw materials or formulations into technical/economical
benefits.
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