Title of Invention

A MIXER AND A METHOD FOR MIXING LIQUID COLORANTS, AND A METHOD FOR COLORING PLASTICS

Abstract The invention relates to a mixer and a method for mixing liquid colorants and a method for coloring plastics comprising a) a mixing pipe (1) having an outlet opening (2) at an end of the mixing pipe (1); b) a mixing unit (3), positioned in the mixing pipe (1) so it is rotatable around a longitudinal axis of the mixing pipe (1), and having at least two mixing elements (3a, 3b) wherein, when in operation, a portion of said mixing elements (3a, 3b) move a content of the mixer in a direction towards the outlet opening (2) and a portion of the mixing elements (3a, 3b) move a content of the mixer in an opposite direction with identical rotational direction of the mixing unit (3), and c) at least two inlet openings (4,5) for liquid colorants (6,7) which are positioned in a wall of the mixing pipe (1) between ends of the mixing pipe (1) in an area of the mixing unit (3) and wherein the inlet openings (4,5) for liquid colorants in the mixing unit (3) are positioned so that during a movement of the mixing unit (3), at least one mixing element (3a,3b) of the mixing unit (3) is moved past each of the inlet openings (4,5) at least than 1 mm distance.
Full Text The present invention relates to a mixer for liquid
colorants and a method for mixing liquid colorants
performed using this mixer, which is suitable for on-demand
dosing of liquid colorants in plastic processing machines.
In the processing of plastics via plastic melts, the
plastic is typically colored by masterbatches.
Masterbatches are plastic granulates having a high content
of coloring agent, which are added to the plastic during
the processing via the melt in order to color the plastic.
The use of masterbatches has the disadvantage that a
separate masterbatch must be manufactured for every type of
plastic and every color and must be stored ready for the
plastic processing. Rapid changes to new colors or changes
of the color tone are not possible, since a new masterbatch
must be produced in each case.
Instead of masterbatches, liquid colorants may also be used
for coloring plastics, the liquid colorant either being
supplied with the, noncolored plastic granulate to the
machine which processes the plastic or being mixed with the
already melted plastic in the machine. In this method, a
liquid colorant mixed for the desired color tone is used,
so that a corresponding liquid colorant must be produced
and stored for every desired color. Rapid changes to new
colors or a change of the color tone are also not possible
here, since a new liquid colorant must be manufactured in
each case.

Supplying multiple liquid colorants separately to a plastic
processing machine and manufacturing plastics having
different color tones via recipe-controlled dosing of the
quantities of the individual liquid colorants has been
suggested in WO 02/087849. This method has the
disadvantage, however, that in the event of recipes having
greatly differing mixing ratios of the individual liquid
colorants, the mixing of the liquid colorants with the
plastic is not sufficiently homogeneous on many plastic
processing machines, so that unevenly colored products are
obtained.
Therefore, there is a need for a mixer and a mixing method,
by which homogeneously mixed liquid colorants for coloring
plastics may be manufactured from individual liquid
colorants according to a recipe, even with greatly
differing proportions of the individual liquid colorants,
the manufacture of the mixture being performed directly
before the processing of the plastic in accordance with the
demand of the plastic processing machine. The mixer must be
capable of reliably mixing even thixotropic liquid
colorants, which only flow at a specific shear load.
WO 99/3-4905 discloses a mixer for manufacturing paints, in
which individual liquid colorants and one or more lacquer
base materials are dosed into a shared chamber of the mixer
and mixed in a downstream turbine mixer, before the mixture
leaves the mixer. However, this mixer is less suitable for
mixing liquid colorants of differing viscosity and density
without adding larger quantities of a lacquer base
material, as is necessary for coloring plastics, since the
mixing of the liquid colorants then remains incomplete.

US 3,664,638 discloses static mixers for mixing liquids, in
which multiple helical mixing elements, each having an
alternating rotational direction, are positioned in a pipe
one after another. Static mixers of this construction are
known to those skilled in the art under the names helical
mixers or Kenics mixers and are typically used for mixing
reactive components during the manufacture of two-component
plastics or two-component adhesives.
Dynamic mixers, in which the mixing elements known from the
helical mixers rotate in a mixing pipe, are also used for
manufacturing two-component plastics. In these mixers, the
two components are axially supplied to the mixing pipe at
one end as in the static mixers.
The known static helical mixers and the mixers having
rotating helical mixing elements using axial supply of the
components are not suitable for mixing liquid colorants
having different flow behaviors, however, as are used for
coloring plastics, in the event of greatly differing mixing
conditions. In the event of different viscosities of the
liquid colorants to be mixed, there is uneven mixing of the
more viscous components, for example, so that mixtures
having varying color tone are obtained. Similar problems
also arise if the liquid colorants have different densities
or one or more of the liquid colorants has thixotropic flow
behavior.
JP-A 3-60727 discloses a static mixer in the construction
of helical mixers, in which nozzles are positioned in the
wall of the mixing pipe in order to mix a fluid with a
fluid flowing through the pipe. The mixer is reported to
have a high mixing action if small quantities of a fluid

are mixed, via the nozzles in the wall of the mixing pipe, into a large fluid stream which
flows through the mixing pipe.
EP-A 0 90 257 discloses a mixer for multiple component plastics, which has a mixing
chamber having a piston rotating in the mixing chamber, a shear gap forming between
the piston and the mixing chamber. The individual components are dosed radially into
the shear gap and leave the mixer via an outlet opening opposite the piston. The mixer
causes laminar flow in the shear gap and has no devices which move the content of the
shear gap in the direction opposite to the outlet opening.
The object of uniform mixing of liquid colorants, even in the event of greatly differing
proportions of the individual liquid colorants and different flow behaviors of the liquid
colorants, may be achieved by the mixer according to the present invention and the
method for mixing liquid colorants performed using the mixer.
SUMMARY OF THE INVENTION
Accordingly, in a first aspect of the invention, there is provided a mixer for liquid
colorants, comprising a) a mixing pipe (1) having an outlet opening (2) at an end of
the mixing pipe (1); b) a mixing unit (3), positioned in the mixing pipe (1) so it is
rotatable around a longitudinal axis of the mixing pipe (1), and having at two mixing
elements (3a, 3b) wherein, when in operation, a portion of said mixing elements (3a,
3b) move a content of the mixer in a direction towards the outlet opening (2) and a
portion of the mixing elements (3a, 3b) move a content of the mixer in an opposite
direction with identical rotational direction of the mixing unit (3), and c) at least two
inlet openings (4, 5) for liquid colorants (6, 7) which are positioned in a wall of the
mixing pipe (1)


between ends of the mixing pipe (1) in an area of the mixing unit (3) and wherein the
inlet openings (4, 5) for liquid colorants in the mixing unit (3) are positioned so that
during a movement of the mixing unit(3), at least one mixing element (3a, 3b) of the
mixing unit (3) is moved past each of the inlet openings (4, 5) at least than 1 mm
distance.
Furthermore, the subject matter of the present invention is a method for mixing liquid
colorants, in which at least two liquid colorants are mixed in the mixer according to the
present invention, the liquid colorants being supplied to the mixer via the inlet openings
for liquid colorants, while the mixing unit is moved around the longitudinal axis of the
mixing pipe and the mixed liquid colorant leaves the mixer, via the outlet opening at the
end of the mixing pipe.
In addition, the subject matter of the present invention is a method for coloring plastics,
in which at least two liquid colorants are mixed using the method according to the
present invention for mixing liquid colorants with volumetric dosing and the mixed liquid
colorant is supplied directly to a plastic processing machine.
Liquid colorants as defined in the present invention are compositions capable of flowing
which contain one or more pigments in dispersed form and/or one or more dyes in
dissolved form. The liquid colorants may be liquid or pasty and may even comprise
thixotropic compositions, which only flow when a shear force which is higher than their
yield point acts on them. The liquid colorants preferably contain up to 10 wt-%,
particularly up to 5 wt-% pigments.
The mixer according to the present invention has a mixing pipe, at whose end an outlet
opening for the mixed liquid colorant is located. The mixing pipe is preferably

implemented so it may be closed during the mixing procedure
at the end opposite the outlet opening, so that the liquid
colorant mixed in the mixing pipe may only leave the mixing
pipe through the outlet opening. A pressure retention valve
may possibly also be positioned on the outlet opening in
order to ensure that no mixed liquid colorant exits from
the outlet opening as long as no liquid colorants are
supplied to the mixer. The mixing pipe preferably has a
circular cross-section and may have a cylindrical or
conical shape, a cylindrical shape being especially
preferred.
A mixing unit is positioned in the mixing pipe so that it
is rotatable around the longitudinal axis of the mixing
pipe. The mixing unit thereby has at least two mixing
elements, a portion of the mixing elements moving the
contents of the mixer in the direction of the outlet
opening and a portion of the mixing elements moving the
contents of the mixer in the opposite direction with
identical rotational direction of the mixing unit. Through
this differing effect of the mixing elements on the
contents of the mixer, back-mixing of the contents is
caused via vortex formation in the mixer. The mixing
elements are preferably dimensioned so that during one
rotation of the mixing unit, the mixing elements are moved
through at least 80 % of the cross-sectional area,
especially preferably at least 90 % of the cross-sectional
area of the mixing pipe. Through such dimensioning, mixing
is caused over the entire cross-section of the mixing pipe.
The mixing unit is preferably implemented so that it is
replaceable, particularly so that it may be pulled out of
the mixing pipe still assembled.

The mixing elements of the mixing unit preferably have the
form of helical coils having alternating opposite
rotational directions, as are known to those skilled in the
art from the mixing elements of the helical mixers.
However, other forms of mixing elements may also be used,
such as stirrers having stirring blades with opposing
pitch. The mixing unit preferably has at least 5,
especially preferably at least 9 mixing elements, each
having a different action on the contents of the mixer.
The actuation of the mixing unit, which sets the mixing
unit in motion, may be produced arbitrarily. Preferably,
the mixing unit is driven via a motor. The mixing unit is
especially preferably driven from the end of the mixing
pipe opposite the outlet opening via a shaft lying in the
longitudinal axis of the mixing pipe. The mixing unit may
be set into an oscillating or rotating movement by the
drive, a rotating movement being preferred. If multiple
mixing elements extend up to near the wall of the mixing
pipe, in the event of a drive via a shaft lying in the
longitudinal axis of the mixing pipe, no additional
mounting of the mixing element in the mixing pipe is
necessary.
The mixer according to the present invention additionally
has at least two inlet openings for liquid colorants, which
are positioned in the wall of the mixing pipe lying between
the ends of the mixing pipe in the area of the mixing unit.
The liquid colorants are accordingly supplied to the mixing
pipe radially through the wall of the mixing pipe and not
axially at the end of the mixing pipe. The inlet openings
for liquid colorants are thereby preferably positioned so
that at least 60 % and especially preferably more than 80 %
of the length of the mixing unit lies between the inlet

openings and the outlet opening at the end of the mixing
pipe. The inlet openings for liquid colorants preferably
lie in one to three planes and especially preferably in
only one plane transverse to the longitudinal axis of the
mixing pipe. The inlet openings may additionally be
provided with shutoff valves or non-return valves, in order
to prevent mixed liquid colorant from flowing back from the
mixer into the lines leading to the inlet openings.
The inlet openings for liquid colorants and the mixing unit
are preferably positioned so that during the movement of
the mixing unit, at least one mixing element of the mixing
unit is moved past each of the inlet openings at a small
distance, preferably less than 1 mm distance, particularly
preferably less than 0.5 mm distance. A high shear force is
thus attained at the inlet openings for liquid colorants
and improved mixing is achieved.
The mixer according to the present invention may
additionally have one or more additional inlet openings for
flushing liquid and/or compressed air, preferably both for
flushing liquid and for compressed air, in order to be able
to empty and clean the mixer in the event of a color
change. In addition, the mixer may also have one or more
outlet openings which allow emptying independently from the
outlet opening at the end of the mixing pipe. The inlet
openings for flushing liquid and/or compressed air and
possibly additional outlet openings are preferably
positioned radially near one end of the mixing pipe or
axially at one end of the mixing pipe.
The method according to the present invention for mixing
liquid colorants is performed in the mixer according to the

present invention. Thereby, the liquid colorants are
supplied to the mixer via the inlet openings for liquid
colorants, while the mixing unit is moved around the
longitudinal axis of the mixing pipe and the mixed liquid
colorant leaves the mixer via the outlet opening at the end
of the mixing pipe. Preferably, all openings besides the
inlet openings for liquid colorants and the outlet opening
at the end of the mixing pipe remain closed during the
mixing procedure, so that the liquid colorants supplied via
the inlet openings may only leave the mixing pipe via the
outlet opening at the end of the mixing pipe after the
mixing. In particular, the end of the mixing pipe opposite
the outlet opening remains closed during the mixing.
The movement of the mixing unit during the supply of the
liquid colorants may be oscillating or rotating, a rotating
movement being preferred. A rotating movement at
essentially constant speed is especially preferred. The
velocity of the movement of the mixing unit may be selected
by those skilled in the art within wide limits in
accordance with the properties of the liquid colorants to
be mixed. The velocity of the movement is selected so that
it is at least sufficiently high for uniform mixing to be
achieved. The velocity of the movement has an upward limit
only by the occurrence of cavitation at the mixing
elements. As long as gas, such as air, is still contained
in the mixer, the velocity of the movement is preferably
selected low, in order to avoid mixing in gas bubbles and
to obtain a bubble-free mixture.
The method according to the present invention for mixing
liquid colorants is preferably performed continuously or
intermittently. If it is performed continuously, the liquid
colorants are supplied in predefined volume ratios, so that

a continuous flow of the mixed liquid colorant leaves the
mixer. If the method is performed intermittently, the
liquid colorants are supplied in predefined volume ratios
alternately in each case in a first time interval, while,
in a following second time interval, the liquid colorants
are not supplied. In intermittent operation, mixed liquid
colorant only leaves the mixer during the first time
interval, but not during the second time interval.
The liquid colorants are preferably supplied to the inlet
openings for liquid colorants by volumetric dosing. In this
case, the liquid colorants are supplied using predefined
volume flows in predefined volume ratios, which result from
the recipe for the desired color. The volumetric dosing is
preferably performed through forced-delivery pumps, in
which the delivered volume results inevitably from the
mechanical movement of the pump. Suitable forced-delivery
pumps are, for example, piston pumps, rotary piston pumps,
and gear pumps. Double-piston pumps are preferably used for
dosing the liquid colorants, in which liquid colorant is
dosed alternately by one of two pistons, while the other
piston is filled, so that a constant volume flow is dosed.
Through volumetric dosing using forced-delivery pumps, a
uniform composition of the mixed liquid colorant may be
achieved reproducibly, without variations in the control of
the dosing resulting in color variations. In addition,
through the volumetric dosing, the quantity flow of mixed
liquid colorant which leaves the mixer may be set
precisely, so that using the method according to the
present invention, the liquid colorant may be dosed
directly into a plastic processing machine. In this case,
the dosing may be performed continuously into a
continuously operating plastic processing machine, for
example, into an extruder. Similarly, dosing may also be
performed intermittently into a discontinuously operating

plastic processing machine, such as an injection molding
machine.
The volumetric dosing of the liquid colorants into the
mixer according to the present invention is preferably
controlled by the plastic processing machine, so that
dosing may be performed directly into the plastic
processing machine without an intermediate container. The
control of the dosing of the liquid colorants into the
mixer according to the present invention by the plastic
processing machine is especially advantageously used for
dosing into discontinuously operating plastic processing
machines, such as injection molding machines.
The direct dosing from the method according to the present
invention into a plastic processing machine allows rapid
color change or an alteration of the color tone during the
plastic processing, without a colorant mixture having to be
prepared beforehand for this purpose or a colorant
container having to be changed on the plastic processing
machine.
Forced-delivery pumps which are driven by stepping motors
are especially preferably used for dosing the liquid
colorants. These pumps have the advantage of a
significantly broader range of precisely and uniformly
adjustable dosing rates compared to continuously driven
pumps having variable-speed drive. While with variable-
speed drive, the range from minimum to maximum dosing rate
is typically not more than 1:100, by using a drive having
stepping motors, ranges of more than 1:1000 may be
implemented. Therefore, a larger range of mixing ratios may
be set without replacing pumps and therefore a larger

number of color tones may be produced. Motorized piston
burettes which are driven by stepping motors are especially
suitable for dosing the liquid colorants.
In the method according to the present invention the supply
of the liquid colorants to the inlet openings for liquid
colorants may be performed continuously or in fixed cycles
in each case. Through the back-mixing occurring in the
mixing pipe, even with fixed-cycle supply of one or more
liquid colorants, uniform mixing without variations of the
composition over time may be achieved using the mixer
according to the present invention if the ratio between the
average hold-up time of the mixed liquid colorant and the
duration of a fixed cycle in the mixer is more than 5:1,
preferably more than 10:1. The duration of a fixed cycle
according to the present invention is the sum of the
duration of an individual step of the colorant supply into
the mixer and the duration of a pause between two such
steps of the colorant supply. Through the possibility of
fixed-cycle supply, even mixtures having greatly differing
ratios of the liquid colorants used may be manufactured
reproducibly without color variations using the method
according to the present invention.
In the method according to the present invention, the
mixing procedure is preferably interrupted for a color
change and the mixer is cleaned using- a flushing liquid in
order to obtain a mixed liquid colorant having altered and
uniform composition as rapidly as possible and keep the
quantities of waste arising from a color change low. For
this purpose, the supply of the liquid colorants is first
interrupted and the mixing pipe is emptied by supplying
compressed air. Subsequently, the mixing pipe is filled at
least once with flushing liquid and the mixing unit is

moved in order to remove the liquid colorant adhering to
the mixing pipe and to the mixing unit with the flushing
liquid. The mixing pipe is then emptied once again by
supplying compressed air and subsequently the supply of the
liquid colorants is continued in another ratio. If, in the
- method according to the present invention, the liquid
colorant is dosed directly into a plastic processing
machine, the contents of the mixing pipe emptied using
compressed air and a first part of the liquid colorant
mixed using an altered ratio are expediently conveyed to a
separate collection container during the cleaning
procedure, before the direct dosing into the plastic
processing machine is continued. In principle, any liquid
which is capable of dissolving or dispersing the components
of the liquid colorant is suitable as the flushing liquid.
The flushing procedure is preferably performed so that at
the end of the flushing procedure, all lines connected to
the mixing pipe are filled with liquid. By avoiding gas
cushions in supply lines, a more 'uniform flow of the mixed
liquid colorant out of the mixer may be obtained during the
following mixing procedure.
If an inlet opening is not needed for manufacturing the
currently needed mixture of liquid colorants, the supply
line for liquid colorant leading to this inlet opening is
preferably at least partially filled with mixed liquid
colorant from the mixing pipe after beginning the supply of
the liquid colorants. This is preferably performed by
briefly operating a pump used for supplying the liquid
colorant in the reverse delivery direction. By at least
partially filling the supply line with already mixed liquid
colorant, contamination of the currently mixed liquid
colorant by an undesired liquid colorant from a currently

unneeded inlet opening may be avoided. In an alternative
embodiment, the supply lines to unneeded inlet openings may
also be at least partially filled with flushing liquid
during the flushing procedure.
In the method according to the present invention for mixing
liquid colorants, in addition to the at least two liquid
colorants, still further free-flowing components or
compositions may also be supplied via the inlet openings
positioned in the wall of the mixing pipe. During the
manufacturing of liquid colorants for coloring plastics,
for example, UV stabilizers, antioxidants, flame
retardants, plasticizers, or additives which improve the
impact strength may also be admixed in order to add them to
the plastic with the mixed liquid colorant.
Figure 1 shows a preferred embodiment of the mixer
according to the present invention having mixing elements
in the form of. helical co_jls, additional inlet openings for
flushing liquid and compressed air, and dosing of the
liquid colorants by volumetrically dosing double-piston
pumps.
Figure 2 shows the flow of liquid colorants plotted against
time t for continuous operation of the mixer with
continuous dosing of the first liquid colorant at a flow
rate Fx and fixed-cycle dosing of the second liquid
colorant at a flow rate F2 and a duration of a fixed cycle
of ti.

Figure 3 shows the flow of liquid colorants plotted against
time t for intermittent operation of the mixer with
continuous dosing of the first liquid colorant at a flow
rate Fi and fixed-cycle dosing of the second liquid
colorant at a flow rate F2. During the intermittent
operation, both liquid colorants are each dosed for a first
time interval t2 and the dosing of both liquid colorants is
interrupted for a second time interval t-$.
Figure 4 shows a preferred embodiment of the mixer
according to the present invention having two mixing pipes.
In the embodiment of Figure 1, the mixer comprises a
cylindrical mixing pipe (1) having an outlet opening (2) at
the lower end of the mixing pipe (1). In the mixing pipe
(1), a mixing unit (3), which is driven by a motor via a
shaft (8), is positioned so it is rotatable around the
longitudinal axis of the mixing pipe (1). The mixing unit
(3) has a total of 5 mixing elements (3a, 3b) in the form
of helical coils having alternating opposite rotational
directions, which are moved through more than 80 % of the
cross-sectional area of the mixing pipe (1) during a
rotation of the mixing unit (3). With identical rotational
direction of the mixing unit (3), a first portion of the
mixing elements (3a) moves the contents of the mixer in the
direction of the outlet opening and a second portion of the
mixing elements (3b) moves the contents of the mixer in the
opposite direction. The mixer additionally has two inlet
openings (4, 5) for liquid colorants (6, 7), which are
positioned in the wall of the mixing pipe lying between the
ends of the mixing pipe (1) in the area of the mixing unit
(3) in a plane transverse to the longitudinal axis of the
mixing pipe (1), so that more than 60 % of the length of
the mixing unit (3) lies between the inlet openings (4, 5)

and the outlet opening (2) at the end of the mixing pipe
(1). The inlet openings (4, 5) for liquid colorants (6, 7)
and the mixing unit (3) are positioned in this case so that
during the movement of the mixing unit, a mixing element
(3b) is moved past the inlet openings (4, 5) at less than
0.5 mm distance. The mixer also has an additional inlet
opening (9) for flushing liquid (10) and compressed air
(11) •
In an especially preferred embodiment of the method
according to the present invention, two liquid colorants
(6, 7) are supplied by double-piston pumps (13, 14) to the
mixing pipe (1) via the inlet openings (4, 5) for liquid
colorants (6, 7), while the mixing unit (3) rotates around
the longitudinal axis of the mixing pipe (1). The end of
the mixing pipe (1) opposite the outlet opening (2) and the
additional inlet opening (9) remain closed in this case, so
that all of the quantity of liquid colorants (6, 7)
supplied via the inlet openings (4, 5) leaves the mixer as
mixed liquid colorant (12) via the outlet opening (2) and a
valve (15). The double-piston pumps (13, 14) are driven via
stepping motors in this case, so that the liquid colorants
(6, 7) may be supplied to the mixer in fixed cycles, the
ratio between the duration of a cycle and the average hold-
up time of the mixed liquid colorant in the mixer being
selected as less than 1: 10. The mixed liquid colorant (12)
is supplied directly to a plastic processing machine, the
volumetric dosing of the liquid colorants (6, 7) being
activated by the plastic processing machine.
For a color change, the mixer shown in Figure 1 is
especially preferably cleaned by first stopping the dosing
of the liquid colorants (6, 7) and closing the valve (15)
via which the mixed liquid colorant (12) is supplied to a

plastic processing machine. Subsequently, compressed air
(11) is supplied via the additional inlet opening (9) and
the contents of the mixing pipe (1) are emptied as a waste
stream (16) into a collection container via the valve (15).
The mixing pipe (1) is then filled completely with a
flushing liquid (10) via the additional inlet opening (9)
with valve (15) closed, the mixing unit (3) rotating and
the mixing pipe (1) being ventilated via a ventilation
opening (not shown) at the upper end of the mixing pipe
(1). After approximately 3 0 seconds, during which the
mixing unit (3) rotates further, compressed air (11) is
supplied via the additional inlet opening (9) and the
contents of the mixing pipe (1) are emptied as a waste
stream (16) into a collection container via the valve (15).
This flushing procedure is subsequently repeated again
twice. The speed of the mixing unit (3) is then reduced and
the liquid colorants (6, 7) are dosed at the new ratio, the
valve (15) initially remaining open so that the mixed
liquid colorant is supplied to a collection container as a
waste stream (16). After a quantity of liquid colorants
(6, 7) corresponding to the volume of the mixing pipe (1)
has been dosed and the air has thus been displaced out of
the mixing pipe' (1), the speed of the mixing unit (3) is
increased back to the original value. After a quantity of
liquid colorants (6, 7) which corresponds to two to three
times the volume of the mixing pipe (1) has been dosed, the
valve (15) is switched so that the mixed liquid colorant
(12) is again supplied to the plastic processing machine.
In the embodiment of Figure 4, the mixer comprises two
mixing pipes (1), each comprising an outlet opening (2), a
mixing unit (3) and inlet openings (4, 5). Liquid colorants
(6, 7) are supplied to the inlet openings (4, 5) by double-
piston pumps (13, 14), whereby in each of the double-piston
pumps the pistons may be actuated independently of each

other and liquid colorant can be dosed from either of the
two pistons independently of each other into either of the
two mixing pipes via appropriately arranged valves. The two
mixing pipes are connected by a valve (15) designed as a
four-way valve in such a manner, that alternatively one of
the mixing pipes is connected via a line with the device
into which the mixed liquid colorant (12) is dosed, while
at the same time the other mixing pipe is connected with a
collection container for the waste stream (16). In addition
to inlet openings (9) for flushing liquid (10) the mixer
preferably also comprises valves (17), whereby flushing
liquid (10) or compressed air (11) can also be passed via
the outlet opening (2) into the mixing pipe (3), as well as
additional outlet openings (18) for waste streams (19) at
the end of the mixing pipe (3) opposite to the outlet
opening (2). The additional valves (17) and outlet openings
(18) allow flushing of the mixing pipe in both directions
and thereby more effective cleaning of the mixing pipe for
a color change.
The preferred embodiment of the mixer according to Figure 4
allows a liquid colorant with a new, altered mixing ratio
to be prepared in a second mixing pipe for a color change,
while still dosing from a first mixing pipe at the old
mixing ratio. This shortens the down time for a color
change, since only the line for mixed liquid colorant (12)
leading from valve (15) to the consuming device has to be
flushed or exchanged for the color change, while the
cleaning of the mixing pipe can occur without interruption
of the dosing of liquid colorant. The second mixing pipe is
flushed and emptied with flushing liquid (10) and
compressed air (11) as described above, while liquid
colorants (6, 7) are still dosed into the first mixing pipe
at the old mixing ratio and a mixed liquid colorant is
obtained at the old mixing ratio via valve (15). Besides

the supply of flushing liquid and compressed air via inlet
opening (9) and emptying via valve (15), there is
preferably additional flushing in the opposite direction by
the supply of flushing liquid and compressed air via valve
(17) and emptying via outlet opening (18). Subsequently,
the second mixing pipe is filled with liquid colorants
(6, 7) in the new mixing ratio as described above, while
the dosing of liquid colorants into the first mixing pipe
is continued at the old mixing ratio. For that purpose, the
two pistons of a double-piston pump (13, 14) are operated
in such a manner as to dose from one of the pump pistons
into the first mixing pipe according to the old mixing
ratio, while dosing from the other pump piston into the
second mixing pipe according to the new mixing ratio. If
one of the pump pistons dosing into the first mixing pipe
has to be filled during this procedure, the filling of the
second mixing pipe is interrupted, the ongoing dosing is
switched to the second, still filled pump piston, the first
pump piston is filled and thereafter filling of the second
mixing pipe is continued, so that the ongoing dosing into
the first mixing pipe is not interrupted. Preferably, with
each of the double-piston pumps the pump piston not
actually needed for dosing into the first mixing pipe is
filled before the second mixing pipe being filled, then all
pumps are switched to dosing into the first mixing pipe
from the filled piston, thereafter the second pump piston
not currently needed for dosing into the first mixing pipe
is likewise filled and then filling of the second mixing
pipe is started. With this procedure, the filling of the
second mixing pipe can normally be completed before a
switch between the pistons of a double-piston pump becomes
necessary for the dosing into the first mixing pipe.

Examples
The experiments were performed in a mixer corresponding to
Figure 1 with a mixing pipe (1) having 8.3 mm internal
diameter and 10 cm length. The mixing pipe had two inlet
openings (4, 5), each 1.5 mm in diameter, at 8 cm distance
to the outlet opening (2). A helical mixer MR 08-12 having
8 mm diameter and 93 mm length from Mixpac, which has 12
mixing elements in the form of helical coils with opposing
directions, was used as the mixing unit (3). The mixing
unit was set in rotation by a motor at 1500 rpm. Motorized
burettes model PSD/8 from Hamilton were used as piston
pumps (13, 14) for dosing the liquid colorants.
Example 1
A red and a white Polytrend 7 00 liquid colorant from
Colortrend were supplied intermittently to the mixer
radially via two different inlet openings (4, 5) in the
volume ratio 10:9, resulting in a total volume flow of
1.8 ml/min. The time interval for supplying the liquid
colorants and the time interval for interrupting the supply
were each 10 seconds. To judge the mixing quality,
individual droplets of mixed liquid colorant obtained at
the outlet opening (2) were drawn out thinly on a
microscope slide and visually evaluated. No inhomogeneities
or variations of the color tone could be observed in the
mixed liquid colorant.
Example 2 (Comparative Example)
Example 1 was repeated, but the two liquid colorants were
not supplied radially via the inlet openings (4, 5), but

axially via inlet openings in the end of the mixing pipe
opposite to the outlet opening (2). The mixed liquid
colorant had clearly recognizable variations in the color
tone.

WE CLAIM
1. Mixer for liquid colorants, comprising
(a) a mixing pipe (1) having an outlet opening (2) at the end of the
mixing pipe,
(b)a mixing unit (3), positioned in the mixing pipe so it is rotatable
around the longitudinal axis of the mixing pipe, having at least two
mixing elements (3a, 3b), and
(c) at least two inlet openings (4, 5) for liquid colorants (6, 7),
characterized in that
the mixing elements (3a, 3b) of the mixing unit (3) have the form of
helical coils having alternating opposite rotational directions and a
portion of the mixing elements (3a) moving the contents of the mixer
in the direction of the outlet opening and a portion of the mixing
elements (3b) moving the contents of the mixer in the opposite
direction with identical rotational direction of the mixing unit, and
the inlet openings (4, 5) are positioned in the wall of the mixing pipe
between the ends of the mixing pipe in the area of the mixing unit,
and during the movement of the mixing unit, at least one mixing
element (3a, 3b) of the mixing unit (3) is moved past each of the inlet
openings at less than 1 mm distance, preferably less than 0.5 mm
distance.
2. Mixer as claimed in Claim 1, wherein the mixing pipe (1) has a cylindrical
shape.

3. Mixer as claimed in one of the preceding claims, wherein the mixing
elements (3a, 3b) of the mixing unit (3) move through at least 80 % of
the cross-sectional area of the mixing pipe (1) during one rotation of the
mixing unit.
4. Mixer as claimed in one of the preceding claims, wherein at least 60 % of
the length of the mixing unit (3) lies between the inlet openings (4, 5) for
liquid colorants (6, 7) and the outlet opening (2) at the end of the mixing
pipe (1).
5. Mixer as claimed in one of the preceding claims, wherein the inlet
openings (4, 5) for liquid colorants (6, 7) lie in one plane transverse to the
longitudinal axis of the mixing pipe (1).
6. Mixer as claimed in one of the preceding claims, wherein the mixing unit
(3) is driven from the end of the mixing pipe opposite the outlet opening
(2) via a shaft (8) lying in the longitudinal axis of the mixing pipe (1).
7. Mixer as claimed in one of the preceding claims, comprising one or more
additional inlet openings (9) for flushing liquid (10) and compressed air
(11).
8. Mixer as claimed in one of the preceding claims, comprising two mixing
pipes (1), whose outlet openings (2) are connected via a valve (15) with a
common line for mixed liquid colorant (12).


9. Mixer as claimed in Claim 8, comprising it comprises at least two double-
piston pumps (13,14), and liquid colorant can be dosed from both pistons
of a double-piston pump independently of each other into either of the
two mixing pipes.
10. Method for mixing liquid colorants, wherein at least two liquid colorants
(6, 7) are mixed in a mixer as claimed in one of Claims 1 to 9, the liquid
colorants being supplied to the mixer via the inlet openings (4, 5) for
liquid colorants, while the mixing unit (3) is moved around the longitudinal
axis of the mixing pipe (1) and the mixed liquid colorant (12) leaves the
mixer via the outlet opening (2) at the end of the mixing pipe.
11. Method as claimed in Claim 10, wherein the mixing unit (3) rotates around
the longitudinal axis of the mixing pipe (1).
12. Method as claimed in Claim 10 or 11, wherein the end of the mixing pipe
(1) opposite the outlet opening (2) remains closed during the mixing.
13. Method as claimed in one of Claims 10 to 12, wherein at least one of the
liquid colorants (6, 7) is supplied to the mixer in fixed cycles, the ratio
between the average hold-up time of the mixed liquid colorant in the
mixer and the duration of a fixed cycle being more than 10:1.
14. Method as claimed in Claim 13, wherein at least one of the liquid colorants


(6, 7) is supplied to the mixer using a pump which is driven by a stepping
motor.
15. Method as claimed in one of Claims 10 to 14, wherein the liquid colorants
(6, 7) are supplied to the mixer volumetrically dosed.
16. Method as claimed in Claim 15, wherein the volumetric dosing of the liquid
colorants (6, 7) is performed by forced delivery, preferably by double-
piston pumps (13,14).
17. Method as claimed in one of Claims 10 to 16, wherein no liquid colorant is
supplied via at least one inlet opening (5) and the supply line leading to
this inlet opening (5) is at least partially filled with mixed liquid colorant
from the mixing pipe after beginning the supply of liquid colorants.

18. Method as claimed in one of Claims 10 to 17, wherein for a color change
(a) the supply of the liquid colorants (6, 7) is interrupted,
(b) the mixing pipe (1) is emptied by supplying compressed air (11),
(c) the mixing pipe is filled with flushing liquid (10) and the mixing unit
(3) is moved,
(d) the mixing pipe (1) is emptied by supplying compressed air (11), and
(e) the supply of the liquid colorants (6, 7) is continued in another ratio.
19. Method as claimed in one of Claims 10 to 18, wherein a mixer with two

mixing pipes (1) is used and at least two liquid colorants (6, 7) are
supplied to one of the mixing pipes, while in the other mixing pipe for a
color change, a) the mixing pipe is emptied by supplying compressed air
(11), b) the mixing pipe is filled with flushing liquid (10) and the mixing
unit (3) is moved, and c) the mixing pipe is emptied by supplying
compressed air (11).


The invention relates to a mixer and a method for mixing liquid colorants and a
method for coloring plastics comprising a) a mixing pipe (1) having an outlet
opening (2) at an end of the mixing pipe (1); b) a mixing unit (3), positioned in
the mixing pipe (1) so it is rotatable around a longitudinal axis of the mixing pipe
(1), and having at least two mixing elements (3a, 3b) wherein, when in
operation, a portion of said mixing elements (3a, 3b) move a content of the
mixer in a direction towards the outlet opening (2) and a portion of the mixing
elements (3a, 3b) move a content of the mixer in an opposite direction with
identical rotational direction of the mixing unit (3), and c) at least two inlet
openings (4,5) for liquid colorants (6,7) which are positioned in a wall of the
mixing pipe (1) between ends of the mixing pipe (1) in an area of the mixing unit
(3) and wherein the inlet openings (4,5) for liquid colorants in the mixing unit (3)
are positioned so that during a movement of the mixing unit (3), at least one
mixing element (3a,3b) of the mixing unit (3) is moved past each of the inlet
openings (4,5) at least than 1 mm distance.

Documents:

01201-kolnp-2008-abstract.pdf

01201-kolnp-2008-claims.pdf

01201-kolnp-2008-correspondence others.pdf

01201-kolnp-2008-description complete.pdf

01201-kolnp-2008-drawings.pdf

01201-kolnp-2008-form 1.pdf

01201-kolnp-2008-form 2.pdf

01201-kolnp-2008-form 3.pdf

01201-kolnp-2008-form 5.pdf

01201-kolnp-2008-gpa.pdf

01201-kolnp-2008-international publication.pdf

01201-kolnp-2008-international search report.pdf

01201-kolnp-2008-pct priority document notification.pdf

01201-kolnp-2008-pct request form.pdf

01201-kolnp-2008-priority document.pdf

1201-KOLNP-2008-(29-02-2012)-CORRESPONDENCE.pdf

1201-KOLNP-2008-ABSTRACT 1.1.pdf

1201-KOLNP-2008-AMANDED CLAIMS 1.1.pdf

1201-KOLNP-2008-AMANDED CLAIMS-1.2.pdf

1201-KOLNP-2008-AMANDED CLAIMS.pdf

1201-KOLNP-2008-AMANDED PAGES OF SPECIFICATION.pdf

1201-KOLNP-2008-CORRESPONDENCE 1.2.pdf

1201-KOLNP-2008-CORRESPONDENCE 1.3.pdf

1201-KOLNP-2008-CORRESPONDENCE OTHERS 1.1.pdf

1201-KOLNP-2008-CORRESPONDENCE-1.4.pdf

1201-KOLNP-2008-CORRESPONDENCE-1.5.pdf

1201-KOLNP-2008-DESCRIPTION (COMPLETE) 1.1.pdf

1201-KOLNP-2008-DESCRIPTION (COMPLETE)-1.2.pdf

1201-KOLNP-2008-DRAWINGS 1.1.pdf

1201-KOLNP-2008-DRAWINGS-1.2.pdf

1201-KOLNP-2008-EXAMINATION REPORT REPLY RECIEVED.pdf

1201-KOLNP-2008-FORM 1-1.1.pdf

1201-KOLNP-2008-FORM 1-1.2.pdf

1201-KOLNP-2008-FORM 18-1.2.pdf

1201-kolnp-2008-form 18.pdf

1201-KOLNP-2008-FORM 2-1.1.pdf

1201-KOLNP-2008-FORM 2-1.2.pdf

1201-KOLNP-2008-FORM 3-1.1.pdf

1201-KOLNP-2008-FORM 3-1.2.pdf

1201-KOLNP-2008-FORM 3-1.3.pdf

1201-KOLNP-2008-FORM 5.pdf

1201-KOLNP-2008-GPA.pdf

1201-KOLNP-2008-GRANTED-ABSTRACT.pdf

1201-KOLNP-2008-GRANTED-CLAIMS.pdf

1201-KOLNP-2008-GRANTED-DESCRIPTION (COMPLETE).pdf

1201-KOLNP-2008-GRANTED-DRAWINGS.pdf

1201-KOLNP-2008-GRANTED-FORM 1.pdf

1201-KOLNP-2008-GRANTED-FORM 2.pdf

1201-KOLNP-2008-INTERNATIONAL PRELIMINARY REPORT.pdf

1201-KOLNP-2008-INTERNATIONAL SEARCH AUTHORITY REPORT.pdf

1201-KOLNP-2008-OTHERS 1.1.pdf

1201-KOLNP-2008-OTHERS-1.1.pdf

1201-KOLNP-2008-OTHERS-1.2.pdf

1201-KOLNP-2008-OTHERS.pdf

1201-KOLNP-2008-PETITON UNDER RULE 137.pdf

1201-KOLNP-2008-REPLY TO EXAMINATION REPORT-1.1.pdf

abstract-01201-kolnp-2008.jpg


Patent Number 251613
Indian Patent Application Number 1201/KOLNP/2008
PG Journal Number 13/2012
Publication Date 30-Mar-2012
Grant Date 26-Mar-2012
Date of Filing 24-Mar-2008
Name of Patentee ENVONIK DEGUSSA GMBH
Applicant Address RELLINGHAUSER STRASSE 1-11, 45128 ESSEN
Inventors:
# Inventor's Name Inventor's Address
1 WEELEN, MAURICE I. C. SCHLAUNSTR. 24, NL-6287 AV EYS
2 BECHT, SIMON WICKSTÄDTERSTRASSE 50 61197 FLORSTADT
3 WELP, MARTIN BILK 57, NL-48493 WETTLINGEN
4 ANDREAS KLUGE ROBERT-SCHUMANN-STRAßE 13 63179 OBERTSHAUSEN
PCT International Classification Number B01F 3/08, B01F 7/00
PCT International Application Number PCT/EP2006/066194
PCT International Filing date 2006-09-08
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 10 2005 049 926.0 2005-10-17 Germany