WO1999041003A1 - Production of automotive and other paints - Google Patents

Production of automotive and other paints Download PDF

Info

Publication number
WO1999041003A1
WO1999041003A1 PCT/BR1998/000099 BR9800099W WO9941003A1 WO 1999041003 A1 WO1999041003 A1 WO 1999041003A1 BR 9800099 W BR9800099 W BR 9800099W WO 9941003 A1 WO9941003 A1 WO 9941003A1
Authority
WO
WIPO (PCT)
Prior art keywords
tank
pipe
production
paints
paint
Prior art date
Application number
PCT/BR1998/000099
Other languages
French (fr)
Inventor
Antonio Retamal
Rogério Batista AUAD
Original Assignee
Renner Du Pont Tintas Automotivas E Industriais S/A.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Renner Du Pont Tintas Automotivas E Industriais S/A. filed Critical Renner Du Pont Tintas Automotivas E Industriais S/A.
Priority to DE69831063T priority Critical patent/DE69831063T2/en
Priority to EP98960943A priority patent/EP0975419B1/en
Priority to US09/402,437 priority patent/US6494608B1/en
Priority to KR10-1999-7009415A priority patent/KR100520500B1/en
Priority to CA002283730A priority patent/CA2283730C/en
Priority to JP54084199A priority patent/JP3882148B2/en
Publication of WO1999041003A1 publication Critical patent/WO1999041003A1/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/71Feed mechanisms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying
    • B01F23/49Mixing systems, i.e. flow charts or diagrams
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/82Forming a predetermined ratio of the substances to be mixed by adding a material to be mixed to a mixture in response to a detected feature, e.g. density, radioactivity, consumed power or colour
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F35/00Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/80Forming a predetermined ratio of the substances to be mixed
    • B01F35/83Forming a predetermined ratio of the substances to be mixed by controlling the ratio of two or more flows, e.g. using flow sensing or flow controlling devices
    • B01F35/833Flow control by valves, e.g. opening intermittently
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2101/00Mixing characterised by the nature of the mixed materials or by the application field
    • B01F2101/30Mixing paints or paint ingredients, e.g. pigments, dyes, colours, lacquers or enamel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/40Mixing liquids with liquids; Emulsifying

Definitions

  • This descriptive report for patent of invention relates to a Continuous and Automatic Process for the Production of Automotive and other Paints, the development of which has as purpose to obtain a process which assures color unifo ⁇ nity, texture and viscosity in the production of paints specially destined to the painting of metal objects, specially car bodies.
  • the manufacture of paint by the conventional method involves a quite complex process and is formed by the following phases: weighing of the raw material, preparation, adjustment of color, coverage, adjustment of viscosity, quality control, canning and packaging.
  • the raw materials which are necessary to produce a given color of paint are weighed in the quantities mentioned in a formula, placed on a pallet and taken, by the lifting truck, to the plaint manufacturing plant which is awaiting the starring of the production.
  • the raw materials either solid or liquid, are weighed in different places, far from the production line, and we should point out that the accuracy of such weighed quantities depends upon the scales used which, on their turn, should constantly gauged so that precise results may be achieved in the weighing operations.
  • Some raw material, which are added in large quantities (such as rosins and solvents), are taken at the plant preparation area.
  • Each tank has its own pump which is driven by the respective feeding valve for raw materials and which is located in the piping which reach the plant, and in said piping system there is coupled a single flow meter which controls the quantity of the raw materials which have to be added to the mixing tank.
  • the mixing tank located at the plant and, in this manner, as soon as the quantity
  • the preparation phase consists of the addition, one by
  • drum tumbler that if the rosin is stored in drums, the operator should use a drum tumbler, which is
  • additives are added also by hand and under stirring.
  • drum tumbler equipment should be used, which is kept in an appropriate
  • Color is the determination of differences in shade between a film and
  • liquid paints, solutions and dispersions the result of which is expressed in g/cm'.
  • Solids is the percentage of solid material existing in a paint.
  • content of non volatile material in a product is not an absolute quantity, but depends uponthe temperature and time of heating used; the recommended temperature
  • time 120°C + 2°C for 1 hour of stove, and, in this method a fixed quantity of
  • the product is weighed, spread in a container and taken to a stove for 1 hour, after
  • Viscosity in a quite empirical way, it is possible to say that viscosity
  • Ford 4 glass if the solvent is added in large quantities, it is also
  • Said test takes approximately 30 minutes to be performed.
  • paint is placed in cans and then packaged, by had.
  • the filling of containers may be
  • the packaging may be made with any volume, depending of the machine to
  • additives and dyes shall be simultaneously pumped within the mixing head in order
  • the paint after ready, passes through a probe which reads the color
  • the whole manufacture process for paint is performed by the PLC (Programmable
  • the system has a flexibility to produce from
  • the system is possible to monitored, for all stages of the process and
  • the system does not require the same number of operators for
  • Figure 1 shows a diagram of the simplified flowchart for the process of loading the
  • FIG. 2 is a diagram of the simplified flowchart for the process of addition of rosins
  • Figure 3 shows a diagram of a simplified flowchart of the addition process for
  • additives in the mixing tank identified by "B";
  • Figure 4 shows a diagram of a simplified flowchart of the addition process for dyes
  • Figure 5 shows a diagram of a simplified flowchart of the addition process for
  • Figure 6 shows a diagram of a simplified flowchart of the addition process for small
  • FIG. 7 shows a diagram of a simplified flowchart of the addition control system
  • Figure 8 shows a diagram of a simplified flowchart of the reception process for raw
  • Figure 9 shows a diagram of a simplified flowchart of the whole set. from the mixer to the later stor;
  • Figure 10 shows a diagram of a simplified flowchart of the reception of nitrogen in
  • Figure 1 1 shows a diagram of a simplified flowchart for the reception of clean
  • Figure 12 shows a diagram of a simplified flowchart for the taking out of dirty-
  • rosin is started, namely, the rosin exists from one of the tanks ( 12a) with a stirrer (2a) and through the pipe (8a) passes by a dosing pump (9a) which is automatically
  • the recirculation of the rosin is started in the second ring, which is formed by
  • said dosing pump (15a) has a
  • variable rotation allowing a variable flow to reach the specified quantity of rosin as
  • control valve (12b) in order to return to the tank (lb), with the pressure of this first
  • dosing pump ( 15c) has variable rotation allowing the variable flow in order to reach
  • valve ( 19d) to open or close and, in this way, to control the viscosity specified in the
  • the balanced mixture of raw materials may be divided into two feeding lines (F and
  • a semi-loading system may be placed in the two feeding lines (F and
  • the mixer (21) is a compact equipment and is provided with several
  • the inner mixing chamber which has a defined minimum volume, necessary for a
  • the system is cleaned with solvent and dried with
  • rosin tanks (la), of all dye tanks (lb), of all additive tanks (lc) and of all tanks of solvents ( 1 d) are pumped and remain recirculating in the pipe systems until the
  • tank or lung tank 941 is gradually pumped into the mixer head (21) until the volume

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Paints Or Removers (AREA)
  • Accessories For Mixers (AREA)
  • Coating Apparatus (AREA)
  • Processes Of Treating Macromolecular Substances (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)

Abstract

Continuous and automatic process for the production of paint including tanks of raw materials, for the addition of rosins (A), of concentrates (B), of additives (C) and of solvents (D). For the production of paints, the process of balanced mixture of raw materials may be divided into two feeding lines (F, G) which receive the introduction of raw materials automatically dosed, by valves and pumps, in mixing tanks (32a, 32b), with a lower outlet pipe which directs the mixture toward the main mixer (21). The paint is taken to a storage tank (41), with a portion of the paint going to a control cell, and with the data being compared with the data of the standard paint for adjustment of color, coverage, and viscosity. An internal cleaning system uses nitrogen to push the paint out from the pipes which are then cleaned with pumped solvent.

Description

PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS
This descriptive report for patent of invention relates to a Continuous and Automatic Process for the Production of Automotive and other Paints, the development of which has as purpose to obtain a process which assures color unifoπnity, texture and viscosity in the production of paints specially destined to the painting of metal objects, specially car bodies.
Presently, the manufacture of paint by the conventional method involves a quite complex process and is formed by the following phases: weighing of the raw material, preparation, adjustment of color, coverage, adjustment of viscosity, quality control, canning and packaging. The raw materials which are necessary to produce a given color of paint are weighed in the quantities mentioned in a formula, placed on a pallet and taken, by the lifting truck, to the plaint manufacturing plant which is awaiting the starring of the production. As it is noticed, the raw materials, either solid or liquid, are weighed in different places, far from the production line, and we should point out that the accuracy of such weighed quantities depends upon the scales used which, on their turn, should constantly gauged so that precise results may be achieved in the weighing operations. Some raw material, which are added in large quantities (such as rosins and solvents), are taken at the plant preparation area.
All raw materials which arrive at the preparation area are kept in tanks located in dikes. Each tank has its own pump which is driven by the respective feeding valve for raw materials and which is located in the piping which reach the plant, and in said piping system there is coupled a single flow meter which controls the quantity of the raw materials which have to be added to the mixing tank. Initially, the operator connects one end of a hose to
the pipe of the product which is to be added while the other end of the hose is placed
against the mouth of the mixing tank, in such a way that in order to unload the raw
material, the operator marks in the meter the quantity in weight (Kg) of the product
and open the feeding valve; said valve send an electric signal to the pump (located in
the dike) turning it on and transferring the product from the outside storage tank to
the mixing tank, located at the plant and, in this manner, as soon as the quantity
marked in the flow meter is reached the pump is automatically turned off.
The preparation phase consists of the addition, one by
one. of the raw materials, following a given order and starting always with the
products of large quantity, followed by those of small quantity, with the rosin being
the first product to be added in the mixing tan, without stirring. It should be noted
that if the rosin is stored in drums, the operator should use a drum tumbler, which is
kept in an appropriate place, taking it next to the mixing tank in order to proceed
with the unloading of the rosin and, if said rosin is taken directly from the pipe
system existing in the plant, the procedure is practically the same for the weighing or.
if there is a pipe system feeding the plant, the addition process is through the flow
meter, as mentioned above.
Other products (additives) are added also by hand and under stirring.
using pails and cans. The whole addition work described above takes approximately 4
hours.
ϊfic dying or color adjustment process is performed by the manual
addition, wilh use of pails, of the dying additives, with the color technician weighing
first the empty pails where the dyes are placed and weighing the pails again when
full, in order to identify the volume of concentrate materials which are placed in the
tank under stirring, until reaching the appropriate color, with the pails being weighted
once again in order to define the exact quantity which was added.
Then a small sample of the paint is taken to the quality control
laboratory, which paints a small plate at the painting cabin, with said plate being
dried, in open air, for 5 to 30 minutes, and than in a stove, under 60 to 180° C
temperature for 10 to 30 minutes, waiting the cooling down of the plate and
comparing it with a standard sample, either visually or through instruments. If the
color is not within the required standards, the color technician makes the necessary
adjustments and repeats the procedure in order to adjust the color until the paint is
within the referred standards. Normally, in order to adjust the color, the color
technician repeats from 3 to 4 times the above mentioned process an this takes, in the
average, 4 hours. It should be pointed out that if the color technician adds the wrong
dye or in an exaggerated amount, it is impossible to adjust the color and. therefore.
the whole lot is lost. After the adjustment of the color a sample is taken and sent to the
quality control department for the adjustment of viscosity and tests. The viscosity
adjustment is made on the sample and performed through the identification of the
volume of solvent contained in said sample, when the total volume of solvent to be
added to the mixing tank is computed.
In this phase, the operator should bring the solvent to adjust the
viscosity, weighing the solvent in pails, cans or drums (depending upon the quantity
of solvent to be added) and pouring it into the mixing tank. If the use of drums is
necessary, a drum tumbler equipment should be used, which is kept in an appropriate
place, taking it next to the mixing tank in order to proceed with the unloading of the
solvent.
In order to wash the tank or bowl, the operator fills a can with cleaning
solvent, taken from the closest solvent pipe, pour it by hand and cleans the walls with
a brush. After this starting work, the operator pours more solvent in order to rinse.
and this dirty solvent, which comes from the tank or bowl, is drained through a
draining cock into a drum, which is taken to the shipping platform of the plant in
order to be removed to the so called "solvent recuperating" plant, which distillates
and recovers the solvent, which will be returned to the plant through a pipe system, to
be used again. When the paint is ready, a sample is taken and sent to the quality control
department, where the following tests are performed: color, coverage, solids, specific
weight and viscosity.
Presently, these tests are performed as follows:
Color: is the determination of differences in shade between a film and
its respective standard, when looked under natural light and in which a sample is
taken out. the viscosity is adjusted and the pain is applied on a steel plate, awaiting
for 15 minutes to evaporate the light solvents and, after said period of time, the
sample is placed on a stove under 60°C for 30 minutes. The average time for the test
is of 1 (one) hour, but in the case of white synthetic enamel, the color technician
needs 16 hours for the drying of the paint in open air, and it may take up to 5 days in
order to adjust the color and to finish the tests.
Specific weigh: used for the determination of the specific mass of
liquid paints, solutions and dispersions, the result of which is expressed in g/cm'.
being traditionally referred to as density; the method is based upon the relationship
between mass of a substance and its volume. For this, a container, the volume of
which is known, is filled with a sample at 25°C, the container is weighed obtaining
the specific weight, with the average time spent to perform the test being
approximately 10 minutes.
Solids: is the percentage of solid material existing in a paint. The
content of non volatile material in a product is not an absolute quantity, but depends uponthe temperature and time of heating used; the recommended temperature
and time is 120°C + 2°C for 1 hour of stove, and, in this method a fixed quantity of
the product is weighed, spread in a container and taken to a stove for 1 hour, after
said period, the sample goes to the drying oven for 30 minutes and then is weighed in
a laboratory scale in order to obtain the percentage of solid material: the average time
for said tests is 2 hours. If the percentile value of solids is out of the specified
standards, the adjustment is made with the addition of rosin or dyes and if during said
addition a larger quantity is used, the whole lot is rejected.
Viscosity: in a quite empirical way, it is possible to say that viscosity
is the difficulty a liquid offers against its flowing; the method is based upon the
flowing time of a continuous flow of a liquid at 25°C, through a given diameter hole
called Ford 4 glass, and if the solvent is added in large quantities, it is also
impossible to adjust the viscosity, therefore losing the whole lot.
Said test takes approximately 30 minutes to be performed.
After the liberation by the Quality Control department, the approved
paint is placed in cans and then packaged, by had. The filling of containers may be
performed in any quantity, depending on the machine to be used.
The average time needed to achieve the analysis for color, viscosity, solids
and specific weight, considering the total rime from the moment taken from the production sector, time awaiting for the tests in the laboratory, until the final answer
from the Quality Control Laboratory to the production department is of
approximately 4 hours.
We should point out further that if the addition of dyes, solvents or
rosins for the adjustment of color, viscosity and solids are performed in non
appropriate quantities by the operator or color technician, it is possible to lose the
whole lot. which will be totally eliminated.
made by different persons and. considering that there are the aspects of training.
capacity, interpretation of results, the analysis depend also of the gouging of the
instruments and quality of the laboratory equipment. Finally, there is a series of
factors which may affect significantly the results, with implications in quality and in
the cost of production.
In the patent nor applied for, the continuous and automatic process for
the production of automotive paints and others is constituted by a process which
produces automatically any type of paint, strictly within the standards specified in the
formulae, complying with the requirements of color, coverage, solids and viscosity.
allowing also the automatic change of color or type of paint in approximately 3
minutes. The packaging may be made with any volume, depending of the machine to
be used for such a work.
For the manufacture of certain types of paint, the mixture of materials
is taken into one of the two mixing tanks; while a mixing tank is loaded and mixing. the mixture of the other tank is being continuously pumped into the head of the
mixer, which has high speed stirring. Other materials required for the final paint
(additives and dyes) shall be simultaneously pumped within the mixing head in order
to be mixed with products of different tanks of raw material. We call raw materials
the rosins, the concentrates, solvents and additives which are used for the production
of paints.
The paint, after ready, passes through a probe which reads the color
and viscosity and then is loaded into cans or drums (0.9. 1.0. 3.6 and 4.0 litters or
other volumes) ready for delivery.
The whole manufacture process for paint is performed by the PLC (Programmable
Logic Controller) and the system is controlled by the supervisor systems through the
FIX- DM ACS software, where all necessary information are stored and then used and
with said system monitoring the following parameters: Color. Coverage. Viscosity.
Specific weight. Pressure. Flow. Dying power of the concentrated.
I summary, this process as the following characteristics: produces
automatically the pain in the specified color and makes the automatic cleaning in
approximately 3 minutes, in other words, all pipes, tanks, valves and equipment are
totally clean in this short period of time and, with this, allows a fast changing of paint
(changing the color and/or type of rosin) in respect to conventional methods used up to now. with great flexibility in the production of paints, namely, it is possible to
produce any color of paint in any rosin contained in the tanks of raw materials,
without the smallest possibility of contamination of one paint with the other, with the
whole color, coverage and viscosity control being perfoπned on line.
For being continuous, the system has a flexibility to produce from
small lots up to large ones.
It performs instantaneously the tests of color, solids, viscosity, specific
weight along the whole manufacture process, with the tests being performed as the
paint is produced. The time for the preparation of the system in order to produce a
new lot is extraordinarily small in respect to the conventional process, due to the fact
that the system performs the automatic cleaning.
With this system it is possible to achieve perfect reproductions of the
paints, namely, the process produces always the same paint, as per the standards
specified in the formulation.
Considering that this process is made in a continuous and automatic
way. the adjustments are perfoπned with the addition in the exact proportion,
continuously, therefore eliminating the addition in larger quantities than the necessary-
ones and eliminating also eventual problems with the quality of the paint.
Due to the fact that the process is continuous and automatic, there is no
need to obtain samples for the laboratory in a manual way. with all inconvenient
mentioned above. Another important benefit of being a continuous and automatic
process is that it is possible to use the automation available resources, such as alarms.
indication of instant reading, graphs of the parameters, reports, accrued values along
the time, history, trends, etc.. with the power to speed up and optimize the
maintenance of the system providing events based in historic facts, filing problems or
changes occurred in the system etc.
Great reliability of the measuring system, for this being a continuous
and automatic system independent of outside variables, such as the waiting time to
perfoπn the tests, contamination, etc.
The system is possible to monitored, for all stages of the process and
all parameters are duly known and controlled.
The system does not require the same number of operators for
maintenance, nor the need of maintaining a laboratory with sophisticated equipment.
for the controls are performed on line.
With this process, a great loss of time is avoided in the movement of
raw materials for the addition of the products, as it is done in the conventional
processes.
Due to the fact that the process is fully automatic, the personnel used
in the operation of the plant becomes more specialized and therefore qualified to
perform any repair in the plant. For a better understanding of the object of this patent, we refer to
the following drawings, where:
Figure 1 shows a diagram of the simplified flowchart for the process of loading the
tanks with raw materials:
Figure 2 is a diagram of the simplified flowchart for the process of addition of rosins
to the mixing tank identified by "A";
Figure 3 shows a diagram of a simplified flowchart of the addition process for
additives in the mixing tank, identified by "B";
Figure 4 shows a diagram of a simplified flowchart of the addition process for dyes
in the mixing tank, identified by "C";
Figure 5 shows a diagram of a simplified flowchart of the addition process for
solvents in the mixing tank, identified by "D";
Figure 6 shows a diagram of a simplified flowchart of the addition process for small
quantities of raw materials taken from the mixing tank, identified by "E";
Figure 7 shows a diagram of a simplified flowchart of the addition control system
for several raw materials in to two mixing tanks, before being placed in the mixer,
the system needed to obtain certain types of paints;
Figure 8 shows a diagram of a simplified flowchart of the reception process for raw
materials in seveτal tanks of the mixer, for the mixing, analysis of their characteristics
and following to the packaging station;
Figure 9 shows a diagram of a simplified flowchart of the whole set. from the mixer to the later stor; Figure 10 shows a diagram of a simplified flowchart of the reception of nitrogen in
the cleaning system, which pushes the paint present within the pipes and in the mixer:
Figure 1 1 shows a diagram of a simplified flowchart for the reception of clean
solvent of the cleaning system; and
Figure 12 shows a diagram of a simplified flowchart for the taking out of dirty-
solvent from the cleaning system.
This Patent of Invention for a CONTINUOUS AND AUTOMATIC
P OCFSS FOR THE PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS
constituted by several feeding lines of raw material, with such lines being basically
formed by tanks ( 1 ) for the loading of raw materials which have the necessary stirrer
motor (2) to homogenize said raw materials and the high level control (3) which,
when the tank ( 1 ) reaches the required filling level, connects the high level transmitter
which disconnects, automatically (through a software), the feeding pump (4) in order
to stop the transfer of the raw material through the pipe (5) from the tank, bowl or
other container (6) and controls the low level (7) which, when the tank is in its low
level, connects the transmitter in order to turn the pump (4) on. which transfers
through said pipe (5) the raw material from the tank (6) into the tank (1). pointing out
that under noπnal conditions of operation, all raw materials connected to the
production of a given paint are simultaneously and automatically added.
In the process for the addition of rosins (A), the recirculation of the
rosin is started, namely, the rosin exists from one of the tanks ( 12a) with a stirrer (2a) and through the pipe (8a) passes by a dosing pump (9a) which is automatically
turned on when the system reaches a previously determined pressure, and by a duct
( l OaO) in order to communicate with the duct (1 1a) with a control valve ( 12a) and
returning into the tank ( 1 a) with the pressure of this first recirculation ring being
controlled through the opening or closing of said control valve (12a) and in this
phase, the recirculation of the rosin is started in the second ring, which is formed by
the pipe (13a), filter ( 14a), dosing pump (15a), flow meter (16a), diversive valve
(17a) which returns the rosin by a pipe (18a) which, on its turn, is connected to the
pipe (1 la) and which, passing through the control valve (12a), returns to the tank (la)
or through the pipe (20a) going to the mixer (21); said dosing pump (15a) has a
variable rotation allowing a variable flow to reach the specified quantity of rosin as
per the respective paint formulas, with the quantity of rosin to be added in the mixer
(21) being controlled by a flow meter (16a) which controls the rotation of the dosing
pump (15a) which, as the total quantity of rosin determined for the production of the
lot is introduced into the system, the adding pumps (9a and 16a) of the rosin tank will
be turned off automatically.
In the process for the addition of dyes (B) which are stored on another
tank ( l b) with 20. 1.000 and 2,500 litters capacity and with a stirrer (2b). after being
taken from the bowl (6b) by the feeding pump (4b) enters first into recirculation.
co ing out from the tank (lb), passing by the pipe (8b) and through the dosing pump
(9b) which is automatically turned on when the system reaches a previously defined 14
pressure and by the pipe (10b) in order to connect widi the pipe (l ib) with the
control valve (12b) in order to return to the tank (lb), with the pressure of this first
ring being controlled through the opening or closing of the control valve (12b) and
in this phase, the recirculation of the concentrated in the second ring starts, which is
formed by the pipe (13b), basket filter (14b), dosing pump (15b), flow meter (16b)
and diversive valve (17b), which returns the concentrate by a duct (18b) which, on its
turn, is connected with the pipe (l ib) and which, passing by the control valve (12b)
returns to the tank (lb) or through the pipe (20) goes to the mixer (21); said dosing
pump (15b) has variable rotation allowing the variable flow in order to reach the
quantity of concentrate specified in the respective formulas of paints, with the
quantity of concentrate to be added in the mixer (21 ) being controlled by a flow
meter (16b) which controls the rotation of the dosing pump (15b) and the quantity of
concentrates which have to be introduced into the system controlled by the control
loop which reads the color on-line and corrects instantaneously with the addition of
concentrates inherent to the respective formula and, as the whole quantity of
concentrate determined for the production of the lot is introduced into the system, the
addition pumps (9b and 15b) of the dye tanks will be automatically turned off.
In the addition process for additives (C) which are stored in another
tank (lc) of 20, 1,000 and 2,500 litters capacity and with motor stirrer (2c) which.
after being taken from the bowl (6c) using a feeding pump (4c) enters initially in
recirculation, namely, it exits the tank (lc), passes by the pipe (8c), by the dosing pump (9c) which is automatically turned on when the system reaches a
previously defined pressure and by a pipe (10c) in order to connect with the pipe
(l ie) with the control valve (12c) in order to return to the tank (lc), with the pressure
of this first ring being controlled through the opening or closing of the control valve
(12c) and, in this phase, the recirculation of the concentrated in the second ring starts,
which is formed by the pipe (13c), basket filter (14c), dosing pump (15c), flow meter
(16c) and diversive valve (17c), which returns the additives by a duct (18c) which, on
its turn, is connected with the pipe (l ie) and which, passing by the control valve
(12c) returns to the tank (lc) or through the pipe (20) goes to the mixer (21); said
dosing pump ( 15c) has variable rotation allowing the variable flow in order to reach
the quantity of additives specified in the respective formulas of paints, with the
quantity of additives to be added in the mixer (21) being controlled by a flow meter
(16c) which controls the rotation of the dosing pump (15c) and the quantity of
additives which have to be introduced into the system controlled by the control loop
which reads the color on-line and corrects instantaneously with the addition of
additives inherent to the respective formula and, as the whole quantity of additives
determined for the production of the lot is introduced into the system, all addition
pumps (9c and 15c) of the dye tanks will be automatically turned off.
In the addition process for additives (D) which are stored in another
tank ( 1 d) which is automatically loaded by PLC with the solvent coming out from the
pipe (8d) being pumped, by the centrifuge dosing pump (9d), passing through the 16
basket filter (14d), by the flow meter (16d) and control valve (19d), until the
pressure reaches a previously established value, with said pressure being adjusted
until reaching a value programmed by the valve (12d) and then the valve (17d) which
sends the flow through the pipe (18d) by the valve (12d) back to the tank (Id) and,
upon changing the position (from ac to ab) and the solvent starts entering the mixer
(21) and in this stage, a fine adjustment of the flow will be made with the quantity of
solvent being controlled by another flow meter (22) which sends instantaneously the
viscosity value of the solvent to the program and this sends a signal to the control
valve ( 19d) to open or close and, in this way, to control the viscosity specified in the
formulation, in such a way that when the raw materials are finally introduced in said
mixer (21), the whole lot of paint already established was produced with the system
turning off automatically.
For the feeding of small quantities of raw materials (E) and for the
adjustments of the mixer (21), a dispersion tank (2e) receives, through the pipe (5e)
and the pump (4e) the raw material taken from the drum or bowl (6e).
Optionally, for the preparation of some types of paints, the process of
the balanced mixture of raw materials may be divided into two feeding lines (F and
G) which receive, alternately and independently, the introduction of the raw materials
(221, 22b, 22c, 22d, 22e, 22f, ...), processed by pumps controlled by the PLC,
through the on-off valves (23a, 23b, 23c, 23d, 23e, 23f, ...) and of rosin (24)
through the valves (25a) and (25b), which shall be automatically dosed by the flow meter (26) which are self adherent and the drains of which (27a), (27b),
(28a) and (28b) serve to calibrate said meters (26) and filters (29a) and (29b) and
through the pipes (30a) and (30b) and 3 way valves (31a) and (31b) which feed
the mixing tanks (32a and 32b), not dedicated, each one with a motor stirrer (2),
with said tanks having a lower outlet pipe through the gear pump (33a) and (33b)
and flow meters (34a) and (34b) and two basket filters assembly in parallel (35a)
and (35b) and connected in a 3 way valve (36a) and (36b) (which send the mixture
to the main mixer (21) or which direct the mixture to 3 way valves (37a) and (37b)
and to the pressure control valves (38a) and (38b) and bringing the mixture back to
the mixing tanks (32a) and (32b) or, when the cleaning process, takes the dirty
cleaning solvent to the outlet (39).
A semi-loading system may be placed in the two feeding lines (F and
G) of the mixing tanks (32a and 32b), with such system being formed by drums,
gear pumps and basket filter, where the quantity of raw materials manually measured
through the weighing in scale with the raw materials being added in the mixing
tanks (32a and 32b), through the pumping or manual unloading through the funnel
installed in the mouth of the tanks.
The mixer (21) is a compact equipment and is provided with several
independent inlet nozzles through which several raw materials are introduced within
the inner mixing chamber, which has a defined minimum volume, necessary for a
perfect homogenization of the raw materials, forming therefore the paint, with the lo
paint produced coming out through the pipe (40) and enters the storage tank
(41 ), with part of the paint being formed in said mixer (21 ) going to the control cell,
composed by diversive valves (42) and (43) by a small tank (44), a pump (45) and a
colorimeter (46), where the color and coverage is analyzed, with the paint returning
to the storage tank 941 ) through the pipe (47) and the data so obtained being then
sent to the program which compares with the standard paint in order to add the
necessary raw materials to adapt the color and coverage, until reaching the specified
standards, with said program adding the flow meter (22) which reads the viscosity
and sends the data to the program which, on its turn, compares with the viscosity
specified and orders the addition or restriction of the quantity of solvent in order to
adjust the viscosity which, if is out of the standards, will return to the tank (41) or if
it has the standard viscosity and ready to be canned, the content of the storage tank
(41 ) is unloaded through pipes by a pump (48) and valve (49) returning to the mixer
(21 ) and from there through the flow meter (22) and, through pipes and the valve
(50) and the discharge pipe (51) and discharging nozzles (52 and 53) may be packed
in 0.9, 1.0, 3.6, 4.0, 200 litters or any other type of volume; after the end of the
production of a given paint, the system is cleaned with solvent and dried with
nitrogen automatically in 3 minutes, with the system remaining capable of producing
a new lot of paint of any color or with any rosin.
In the start up process, the materials from all tanks (32a), (32b) of all
rosin tanks (la), of all dye tanks (lb), of all additive tanks (lc) and of all tanks of solvents ( 1 d) are pumped and remain recirculating in the pipe systems until the
pressure reaching a stable value being, then, the dosing system and feeding system
using the adjustment of the last lot produced; the first paint in the mixer (21) is taken
to the storage tank (41 ) (called also lung tank) and when the paint becomes stable
within the technical specification, the flow is turned to the discharging of the ready
paint (52 and 53) in drums or cans and, during the process, the material of the storage
tank or lung tank 941 ) is gradually pumped into the mixer head (21) until the volume
of said tank reaches the zero level, before the end of the "production run", totally
controlled.
The feeding of new colors requires a 20 liter sample of the product,
which is sent through the colorimeter (46) analyzers) using the small tank (44) and
the pump (45) with the system registering the new color, with the product being men
produced through the normal sequence using the percentile value of the inlet formula
as a starting point and the color registrations and viscosity which intend to reach.
After the discharge being completed, a portion of nitrogen from the
storage tank and distributed by the pipes passes through the diversive valve (54), is
inserted through individual valves (55), (56), (57) and (58) in the points (59), (60).
(61 ) and (62) of the system to push the product of the pipes in the outlet of the mixer
(21 ) and in the pipes, the clean solvent is then introduced from the storage tank which
passes through the pump (63), filter (64), and diversive valve (65) and is inserted 20
through the individual valves (66), (67), (68) and (69) in the points (70), (71 ), (72),
(73) and (74), this last one passing through the pipe with the diversive valve (75) and
passing into the mixing tanks (32a) and (32b), with the dirty solvent being taken out
in the points (39) and (76) being placed within the storage tank (77) through the
pump (78) taken for recuperation.
Periodically, the adjustment of the dosing pumps (15a), (15b), (15c),
(9d), (33a) and (33b) in order to compensate the natural wear through a deviation of
the outlets, using an hydraulic cylinder against a constant simulated pressures in the
normal process; the time which the cylinder takes to run a given volume is measured
and the flow x rotation curve stored in the control system are updated and, if the flow
goes below a given value (maximum wear), the system informs the operator in order
to process the change of said pumps (15a), (15b), (15c), (9d), (33a) and (33b).

Claims

21
1. CONTINUOUS AND AUTOMATIC PROCESS FOR THE
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS, characterized by
several feeding lines of raw material, with such lines being formed basically by tanks
(1) for the loading of raw materials, which have, if necessary, a motor stirrer (2) to
homogenize said raw materials and high level control (3) which, when the tank (1 )
reaches the required filling level, turns the high level transmitter on which
disconnects automatically (by software) the feeding pump (4) in order to stop the transfer,
through the duct (5), the raw material of the tank, bowl or other (6) and a low level control (7)
which, when the tank is with a low level turns said transmitter on to connect the pump (4)
which transfer through said pipe (5) the raw material from the tank (6) into the tank (l),m
pointing out that under normal conditions of operation, all raw materials inherent
to the production of a given paint are added simultaneously and automatically.
2. CONTINUOUS AND AUTOMATIC PROCESS FOR THE
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS as per the claim 1.
characterized by the fact that in the process for addition of rosins (A) the
recirculation of the rosin, namely, the rosin coming our of one of the tanks (la)
with motor stirrer (2) and through the duct (8a) passes by the dosing pump (a) which
is automatically turned on when the system reaches a given pressure and by the pipe
(10a) to connect the pipe (11a) with the control valve (12a) and returning to the tank
(la), with the pressure of this first recirculation ring being controlled through the opening or closing of said control valve (12a) and, in this phase, the
recirculation of the rosin begins in the second ring, which is formed by the pipe
(13a), filter (14a), dosing pump (15a), flow meter (16a), diversive valve (17a), which
returns the rosin through the pipe (18a) which is connected to the pipe (1 1a) and
which, passing by the control valve (12a) returns to the tank (la) or through the pipe
(20a) going to the mixer (21 ); said dosing pump (15a) has variable rotation
allowing a variable flow to reach the quantity or rosin specified in the respective
formulas of the paints, with the quantity of rosin to be added in the mixer 921)
controlled by a flow meter 916a) which commands the rotation of the dosing pump
(15a) which as soon as all quantity of rosin determined for the production of the lot is
introduced in the system, the addition pumps (9a and 16a) of the rosin tank will torn
automatically off.
3. CONTINUOUS AND AUTOMATIC PROCESS FOR THE
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS as per the claim 1,
characterized by the fact that in the process for the addition of dyes (B) which are
stored on another tank (lb) with 20, 1,000 and 2,500 litters capacity and with a stirrer
(2b). after being taken from the bowl (6b) by the feeding pump (4b) enters first into
recirculation, coming out from the tank (lb), passing by the pipe (8b) and through the
dosing pump (9b) which is automatically turned on when the system reaches a
previously defined pressure and by the pipe (10b) in order to connect with the pipe
(l ib) with the control valve (12b) in order to return to the tank (lb), with the pressure 23
of this first ring being controlled through the opening or closing of the control valve
(12b) and, in this phase, the recirculation of the concentrated in the second ring starts,
which is formed by the pipe ( 13b). basket filter ( 14b). dosing pump ( 15b). flow
meter ( 16b) and diversive valve ( 17b). which returns the concentrate by a duct ( 18b)
which, on its turn, is connected with the pipe ( l ib) and which, passing by the control
valve ( 12b) returns to the tank ( lb) or through the pipe (20) goes to the mixer (21 );
said dosing pump ( 15b) has variable rotation allowing the variable flow in order to
reach he quantity of concentrate specified in the respective formulas of paints, with
the quantity of concentrate to be added in the mixer (21 ) being controlled by a flow
meter ( 16b) which controls the rotation of the dosing pump ( 15b) and the quantity of
concentrates which have to be introduced into the system controlled by the control
oop which reads the color on-line and corrects instantaneously with the addition of
concentrates inherent to the respective formula and, as the whole quantity of
concentrate determined for the production of the lot is introduced into the system, the
addition pumps (9b and 15b) of the dye tanks will be automatically turned off
4. C ONTINUOUS AND AUTOMATIC PROCESS FOR THE
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS as per the claim I.
characterized by the fact that in the process for the addition of additives (C) which
are stored in another tank ( lc) of 20, 1,000 and 2,500 litters capacity and with motor
stirrer (2c) which, after being taken from the bowl (6c) using a feeding pump (4c)
enters initially in recirculation, namely, it exits the tank (lc), passes by the pipe (8c). by the dosing pump (9c) which is automatically turned on when the system reaches a
previously defined pressure and by a pipe (10c) in order to connect with the pipe
(l ie) with the control valve (12c) in order to return to the tank (lc), with the pressure
of this first ring being controlled through the opening or closing of the control valve
(12c) and, in this phase, the recirculation of the concentrated in the second ring
starts, which is formed by the pipe (13c), basket filter (14c), dosing pump (15c),
flow meter (16c) and diversive valve (17c), which returns the additives by a duct
(18c) which, on its turn, is connected with the pipe (He) and which, passing by the
control valve (12c) returns to the tank (lc) or through the pipe (20) goes to the mixer
(21 ); said dosing pump (15c) has variable rotation allowing the variable flow in
order to reach the quantity of additives specified in the respective formulas of
paints, with the quantity of additives to be added in the mixer (21) being controlled
by a flow meter (16c) which controls the rotation of the dosing pump (15c)
and the quantity of additives which have to be introduced into the system controlled
by the control loop which reads the color on-line and corrects instantaneously with
the addition of additives inherent to the respective formula and, as the whole quantity
of additives determined for the production of the lot is introduced into the system, all
addition pumps (9c and 15c) of the dye tanks will be automatically turned off.
5. CONTINUOUS AND AUTOMATIC PROCESS FOR THE
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS as per the claim 1,
characterized by the fact that in the process for the addition of solvents (D) used to adjust the viscosity, the solvent, which comes from the tanks (Id) which is
automatically loaded by PLC with the solvent coming out from the pipe (8d) being
pumped, by the centrifuge dosing pump (9d), passing through the basket filter (14d).
by the flow meter ( 16d) and control valve (19d), until the pressure reaches a
previously established value, with said pressure being adjusted until reaching a value
programmed by the valve (12d) and then the valve (17d) which sends the flow
through the pipe (18d) by the valve ( 12d) back to the tank ( 1 d) and, upon changing
the position (from ac to ab) and the solvent starts entering the mixer (21) and in this
stage, a fine adjustment of the flow will be made with the quantity of solvent being
controlled by another flow meter (22) which sends instantaneously the viscosity value
of the solvent to the program and this sends a signal to the control valve (19d) to
open or close and, in this way, to control the viscosity specified in the formulation, in
such a way that when the raw materials are finally introduced in said mixer (21),
the whole lot of paint already established was produced with the system turning off
automatically.
6. CONTINUOUS AND AUTOMATIC PROCESS FOR THE
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS as per the claim 1,
characterized by the fact for the feeding of small quantities of raw material (E) and
for die adjustment of the mixer (21), a dispersion tank (le) receives, through the pipe
(5e) and pump (4e) the raw material taken from the bowl or container (6e).
7. CONTINUOUS AND AUTOMATIC PROCESS FOR THE 26
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS as per the claim 1.
characterized by the fact that, optionally, for the preparation of some types of paints.
the process of the balanced mixture of raw materials may be divided into two feeding
lines (F and G) which receive, alternately and independently, the introduction of the
raΛV materials (221. 22b. 22c. 22d. 22e. 22f ...), processed by pumps controlled by
the PLC. through the on-off valves (23a, 23b, 23c, 23d, 23e, 23f. ...) and of rosin
(24) through the valves (25a) and (25b), which shall be automatically dosed by the
flow meter (26) which are self adherent and the drains of which (27a). (27b). (28a)
and (28b) serve to calibrate said meters (26) and filters (29a) and (29b) and through
the pipes (30a) and (30b) and 3 way valves (31 a) and (31b) which feed the mixing
tanks (32a and 32b). not dedicated, each one with a motor stirrer (2). with said tanks
having a lower outlet pipe through the gear pump (33a) and (33b) and flow meters
(34a) and (34b) and two basket filters assembly in parallel (35a) and (35b) and
connected in a 3 way valve (36a) and (36b) (which send the mixture to the main
mixer (21 ) or which direct the mixture to 3 way valves (37a) and (37b) and to the
pressure control valves (38a) and (38b) and bringing the mixture back to the mixing
tanks (32a) and (32b) or, when the cleaning process, takes the dirty cleaning solvent
to the outlet (39).
8. C ONTINUOUS AND AUTOMATIC PROCESS FOR THE
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS as per the claim 7.
characterized by a semi-loading system that may be placed on the two feeding lines (F and G) of the mixing tanks (32a and 32b). with such system being foπned by
drums, gear pump and basket filter, where the quantity of raw material is measured
manually through the weighing in scale, with the raw materials being added in the
mixing tanks (32a and 32b) through the pumping or manual discharge, through a
funnel installed in the nozzle of the tanks.
9. CONTINUOUS AND AUTOMATIC: PROCESS FOR THE
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS as per the claims
2. 3. 4. 5. 6, and 7, characterized by the fact that said mixer (21 ) is a mixer compact
with several independent inlet nozzles through which the raw materials are introduced
in the inner mixing chamber, which has a defined minimum volume, necessary for a
perfect homogenization of the raw materials, forming the paint, with the produced
paint coming out from the pipe (40) and entering into the storing tank (41 ). with part
of the paint being formed in said mixer (21) going to the control cell, composed
by diversive valves (42) and (43) by a small tank (44), a pump (45) and a colorimeter
(46). where the color and coverage is analyzed, with the paint returning to the storage
tank 941 ) through the pipe (47) and the data so obtained being then sent to the
program which compares with the standard paint in order to add the necessary raw
materials to adapt the color and coverage, until reaching the specified standards,
with said program adding the flow meter (22) which reads the viscosity and sends the
data to the program which, on its tum, compares with the viscosity specified and
orders the addition or restriction of the quantity of solvent in order to adjust the 28
viscosity which, if is out of the standards, will return to the tank (41 ) or if it has the
standard viscosity and ready to be canned, the content of the storage tank ( 1 ) is
unloaded through pipes by a pump (48) and valve (49) returning to the mixer (21 )
and from there through the flow meter (22) and, through pipes and the valve (50) and
the discharge pipe (51 ) and discharging nozzles (52 and 53) may be packed in 0.9.
1.0, 3.6. 4.0, 200 litters or any other type of volume: after the end of the
production of a given paint, the system is cleaned with solvent and dried
with nitrogen automatically in 3 minutes, with the system remaining capable of
producing a new lot of paint of any color or with any rosin.
10. CONTINUOUS AND AUTOMATIC PROCESS FOR THE
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS characterized by
the fact that in the start up process, the materials from all tanks (32a), (32b) of all
rosin tanks ( l a), of all dye tanks (lb), of all additive tanks (l c) and of all tanks
of solvents ( 1 d) are pumped and remain recirculating in the pipe systems until the
pressure reaching a stable value being, then, the dosing system and feeding system
using the adjustment of the last lot produced; the first paint in the mixer (21 ) is taken
to the storage tank (41 ) (called also lung tank) and. when the paint becomes stable
within the technical specification, the flow is turned to the discharging of the ready
paint (52 and 53) in drums or cans and. during the process, the material of the storage
tank or lung tank 941 ) is gradually pumped into the mixer head (21 ) until the volume
of said tank reaches the zero level, before the end of the "production run", totallv 29
controlle
1 1. C ONTINUOUS AND AUTOMATIC: PROCESS FOR THE
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS characterized by
the alignment of new colors requiring a 20 litter sample of the product, which is sent
through the colorimeter (46) analyzers) using the small tank (44) and the pump (45).
with the system registering the new color, with the product being then produced by a
normal sequence using the percentile value of the inlet formula as the starring point
and the registration of color and viscosity which we intend to reach.
12. CONTINUOUS AND AUTOMATIC PROCESS FOR THE
PRODUCTION OF AUTOMOTIVE AND OTHER PAINTS characterized by
the fact that after the discharge being completed, a portion of nitrogen from the
storage tank and distributed by the pipes passes through the diversive valve (54). is
inserted through individual valves (55), (56), (57) and (58) in the points (59). (60).
61 ) and (62) of the system to push the product of the pipes in the outlet of the mixer
(21 ) and in the pipes, the clean solvent is then introduced from the storage tank which
passes through the pump (63), filter (64), and diversive valve (65) and is inserted
through the individual valves (66), (67), (68) and (69) in the points (70). (71 ). (72).
(73) and (74). this last one passing through the pipe with the diversive valve (75) and
passing into the mixing tanks (32a) and (32b), with the dirty solvent being taken out
in the points (39) and (76) being placed within the storage tank (77) through the pump
(78) taken for recuperation.
13. CONTINUOUS AND AUTOMATIC PROCESS FOR THE
PRODUC TION OF AUTOMOTIVE AND OTHER PAINTS characterized by
the fact that it is necessary to adjust, periodically, the dosing pumps ( 15a). ( 15b).
(15c). (9d), (33a) and (33b) in order to compensate the natural wear through a
deviation of the outlets, using an hydraulic cylinder against a constant simulated
pressures in the noπnal process; the time which the cylinder takes to run a given
volume is measured and the flow x rotation curve stored in the control system arc
updated and, if the flow goes below a given value (maximum wear), the system
informs the operator in order to process the change of said pumps ( 15a). ( 15b). ( 15c).
(9d). (33a) and (33b).
PCT/BR1998/000099 1998-02-13 1998-12-10 Production of automotive and other paints WO1999041003A1 (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
DE69831063T DE69831063T2 (en) 1998-02-13 1998-12-10 MANUFACTURE OF AUTOMOTIVE AND OTHER COLORS
EP98960943A EP0975419B1 (en) 1998-02-13 1998-12-10 Production of automotive and other paints
US09/402,437 US6494608B1 (en) 1998-02-13 1998-12-10 System for the continuous and automatic production of automotive and other paints capable of handling a plurality of different paints
KR10-1999-7009415A KR100520500B1 (en) 1998-02-13 1998-12-10 Production of automotive and other paints
CA002283730A CA2283730C (en) 1998-02-13 1998-12-10 Continuous and automatic process for the production of automotive and other paints
JP54084199A JP3882148B2 (en) 1998-02-13 1998-12-10 Continuous automatic manufacturing system for automobiles and other paints

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
BR9800361-5A BR9800361A (en) 1998-02-13 1998-02-13 Continuous and automatic process for the production of automotive paints and others
BRPI9800361 1998-02-13

Publications (1)

Publication Number Publication Date
WO1999041003A1 true WO1999041003A1 (en) 1999-08-19

Family

ID=38871689

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/BR1998/000099 WO1999041003A1 (en) 1998-02-13 1998-12-10 Production of automotive and other paints

Country Status (11)

Country Link
US (1) US6494608B1 (en)
EP (1) EP0975419B1 (en)
JP (1) JP3882148B2 (en)
KR (1) KR100520500B1 (en)
CN (2) CN100344359C (en)
AR (1) AR006736A1 (en)
BR (1) BR9800361A (en)
CA (1) CA2283730C (en)
DE (1) DE69831063T2 (en)
ES (1) ES2244102T3 (en)
WO (1) WO1999041003A1 (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001279188A (en) * 2000-02-18 2001-10-10 John Michael Friel System for manufacturing dispersion type coating material
US6533449B1 (en) * 1998-03-26 2003-03-18 Renner Herrmann S.A. Apparatus and process for the continuous preparation of a fluid, utilizing a fluid recycling means including a buffer
JP2003340257A (en) * 2002-05-01 2003-12-02 Hewlett Packard Co <Hp> Mixer and mixing method
US7423755B2 (en) 2005-12-05 2008-09-09 E.I. Du Pont De Nemours And Company Liquid measurement cell having a transparent partition therein
US7477394B2 (en) 2005-12-05 2009-01-13 E.I Du Pont De Nemours & Company Method for measuring a color property of a liquid using a liquid measurement cell having a transparent partition therein
US7542143B2 (en) 2005-12-05 2009-06-02 E.I. Du Pont De Nemours And Company Liquid measurement cell having a pressurized air cavity therein
US7684045B2 (en) 2005-12-05 2010-03-23 E.I. Du Pont De Nemours And Company Probe apparatus for measuring a color property of a liquid
US7719686B2 (en) 2005-12-05 2010-05-18 E.I. Du Pont De Nemours And Company System for measuring a color property of a liquid
EP2719406A4 (en) * 2011-06-08 2015-03-11 Nikkiso Co Ltd Mixing device
WO2018210559A1 (en) 2017-05-19 2018-11-22 Basf Coatings Gmbh Modular production system and method for producing formulations
CN110141983A (en) * 2019-05-27 2019-08-20 北京半导体专用设备研究所(中国电子科技集团公司第四十五研究所) Photoresist dilution automatically configures device and photoresist dilution automatically configures component
RU2776169C2 (en) * 2017-05-19 2022-07-14 БАСФ Коатингс ГмбХ Modular production system and method for compositions

Families Citing this family (56)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7339000B1 (en) 1998-12-23 2008-03-04 Coatings Management Systems Inc. Method and apparatus for producing an aqueous paint composition from a plurality of premixed compositions
US7445816B2 (en) * 1999-11-15 2008-11-04 Ppg Industries Ohio, Inc. Method and apparatus for coating a substrate
WO2002000335A1 (en) * 2000-06-16 2002-01-03 Chroma Injecta Color Systems, Inc. Process and dispensing system for preparing liquid concentrates for plastics
US6867861B2 (en) 2001-03-19 2005-03-15 E. I. Du Pont De Nemours And Company Method and apparatus for characterizing the color properties of fluids
US6719452B2 (en) * 2001-03-19 2004-04-13 E. I. Du Pont De Nemours And Company Process for manufacturing transparent tints
US6917424B2 (en) 2001-03-19 2005-07-12 E. I. Du Pont De Nemours And Company Process for manufacturing pigment dispersions
US6888636B2 (en) 2001-03-19 2005-05-03 E. I. Du Pont De Nemours And Company Method and apparatus for measuring the color properties of fluids
US7027147B2 (en) 2001-03-19 2006-04-11 E. I. Dupont De Nemours And Company Method and apparatus for measuring the color properties of fluids
TWI240763B (en) * 2001-05-16 2005-10-01 Ind Tech Res Inst Liquid phase deposition production method and device
DE10239189A1 (en) * 2002-08-21 2004-03-04 Endress + Hauser Flowtec Ag, Reinach Device and method for mixing two fluids
JP4512913B2 (en) * 2003-04-07 2010-07-28 旭有機材工業株式会社 Fluid mixing device
DE102004005080A1 (en) * 2004-02-02 2005-08-18 Voith Paper Patent Gmbh Continuous controlled coating color preparation
EP1799552A2 (en) * 2004-10-13 2007-06-27 Ultrablend LLC Tinting method and apparatus
ES2344988T3 (en) * 2004-11-18 2010-09-13 Kansai Paint Co., Ltd. PAINT ELABORATION SYSTEM AND PROCEDURE.
FR2883080A1 (en) * 2005-03-11 2006-09-15 Volumatic And Blending Systems Fluid feed system for chemical/lubricant mixer includes degassing and recirculating ducts, and recirculation valve with control unit
US7628529B2 (en) * 2005-07-29 2009-12-08 Toyota Motor Engineering & Manufacturing North America, Inc. Systems and methods for mixing paint
DE102006026254A1 (en) * 2006-06-02 2007-12-06 Schmidt & Heinzmann Gmbh & Co. Kg Mixing equipment for molding compound used to produce polymer sheet for further processing, is designed with recirculating pumping line
DE102007058412A1 (en) * 2007-12-03 2009-06-04 Bartec Dispensing Technology Gmbh Viscous material e.g. adhesive, conditioning device for use in processing device, has agitator driven by motor and feed pump that is connected to downstream of container, where pump is driven by motor
JP5043696B2 (en) * 2008-01-21 2012-10-10 東京エレクトロン株式会社 Processing liquid mixing apparatus, substrate processing apparatus, processing liquid mixing method, and storage medium
US20090228367A1 (en) * 2008-03-05 2009-09-10 Microblend Technologies, Inc. Method and apparatus for producing and selling paint remotely
KR100950560B1 (en) * 2008-07-01 2010-04-01 현대삼호중공업 주식회사 Painter mixer
WO2011106022A1 (en) * 2010-02-26 2011-09-01 Conagra Foods Rdm, Inc. Fiber particle size reduction in fiber-containing food slurries
TWI447249B (en) * 2010-05-17 2014-08-01 Hon Hai Prec Ind Co Ltd System for supplying mixed gases, sputtering apparatus and sputtering method
CN102251220A (en) * 2010-05-19 2011-11-23 鸿富锦精密工业(深圳)有限公司 Mixed gas supply system, sputtering device and sputtering method
CL2010000832A1 (en) * 2010-08-04 2011-03-18 Parga Edmundo Ganter Sbr sewage treatment system of limited volume, uses two concentric ponds a pulmonary pond and an sbr reactor, both trunks, the reactor is located inside the volume of the pulmonary pond, and with an aeration zone with a duct that extends until before the minimum reactor level, process.
EP2671637A4 (en) 2011-01-31 2014-01-22 Asahi Kasei Chemicals Corp Mixed solution production device and mixed solution preparation method
US10289127B2 (en) * 2011-04-13 2019-05-14 Autoquip, Inc. Mixed fluid delivery system
ES2451694T3 (en) * 2011-06-29 2014-03-28 Alfa Laval Corporate Ab System to eject liquid into a container
CN102371131A (en) * 2011-11-17 2012-03-14 安徽索维机电设备制造有限公司 Automatized material mixing production equipment of automobile paint
CN103143482B (en) * 2011-12-07 2015-08-12 李因国 High accuracy paint mixing color matching double purpose device
US8936390B2 (en) * 2011-12-16 2015-01-20 Microblend Technologies, Inc. Method and apparatus for producing paint
CN103691338B (en) * 2013-12-25 2015-11-25 昆明昆船物流信息产业有限公司 A kind of prepared slices of Chinese crude drugs automatic blending method and system
RU2578314C2 (en) * 2014-07-14 2016-03-27 Общество с ограниченной ответственностью "Нефтяные и Газовые Измерительные Технологии" Method of creation of uniform two-component mixture of liquids with set ratio of mutually insoluble components of different density
CA2958294C (en) * 2014-08-19 2019-02-19 Atlas James RUSSELL System, method and apparatus for recycling asphalt shingles and producing asphalt mix
CN104376408A (en) * 2014-11-07 2015-02-25 珠海市长陆工业自动控制系统有限公司 Data acquisition and management system used in paint producing process
US10697833B2 (en) * 2014-11-13 2020-06-30 Basf Coatings Gmbh Index for determining a quality of a color
CN104857887B (en) * 2015-04-29 2018-01-30 江苏优珀斯材料科技有限公司 A kind of auto feed of high viscosity coating fluid, dispensing, feeding system
CN105676813A (en) * 2016-01-06 2016-06-15 惠州东方雨虹建筑材料有限责任公司 Pipeline monitoring system for water-based pigment make-up system in pigment coating workshop
JP7306608B2 (en) * 2016-03-11 2023-07-11 フジフイルム エレクトロニック マテリアルズ ユー.エス.エー., インコーポレイテッド Advanced fluid handling methods and systems
US9643134B1 (en) * 2016-07-12 2017-05-09 Mazzei Injector Company, Llc Proportionate automated blending system for aqueous mixtures
CN106422938A (en) * 2016-11-01 2017-02-22 重庆瑞恩涂料有限公司 Multi-stirring-mode paint production system powered by adjustable stabilized voltage source
RU2731588C1 (en) * 2017-05-19 2020-09-04 БАСФ Коатингс ГмбХ Method and a mixing plant for dosed batch-based preparation of a fluid cover material
CN107703126A (en) * 2017-08-10 2018-02-16 中科图灵视控(北京)智能科技有限公司 A kind of Concentration Testing and automatic feeding system
CN107837746A (en) * 2017-11-23 2018-03-27 安徽枫雅轩科技信息服务有限公司 Automatic mixture production equipment for automotive paint
DE102018004663B4 (en) * 2018-06-12 2020-11-26 Psa Automobiles Sa Vehicle painting device and method
CN108905862B (en) * 2018-08-27 2023-11-07 天津金牛电源材料有限责任公司 Automatic electrolyte preparation system and preparation method thereof
BR102019005047B1 (en) 2019-03-15 2021-04-13 Rogério Baptista Auad INK PRODUCTION SYSTEM WITH AUTOMATIC SELF-ADJUSTMENT OF FINAL PRODUCT PROPERTIES AND RESPECTIVE METHOD
CN110548474A (en) * 2019-09-29 2019-12-10 深圳市亚仕德新材料有限公司 Coating production system
IT202000009547A1 (en) * 2020-04-30 2021-10-30 Dromont S P A AUTOMATIC PLANT FOR THE PREPARATION OF PAINTS AND SIMILAR
CN112316766A (en) * 2020-11-14 2021-02-05 全方位(菏泽)生物科技有限公司 Stirring mechanism of liquid mixing device
CN112473043B (en) * 2020-11-30 2022-05-03 中国民用航空总局第二研究所 Fire extinguishing agent filling system for aviation forest fire control and using method
CN112742274A (en) * 2021-01-04 2021-05-04 深圳市科润光电股份有限公司 Proportioning equipment for LED packaging adhesive
US20220243573A1 (en) * 2021-01-29 2022-08-04 Downhole Chemical Solutions, Llc Systems and methods for subdividing chemical flow for well completion operations
CN115121400B (en) * 2021-03-29 2023-06-09 华晨宝马汽车有限公司 Liquid viscosity regulating method
US20220362688A1 (en) * 2021-05-12 2022-11-17 Eddy Pump Corporation Slurry removal system
CN114082333A (en) * 2021-12-28 2022-02-25 随州市文峰涂料有限责任公司 A high-efficient mixing arrangement for water paint mixing of colors

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3425667A (en) * 1967-03-31 1969-02-04 Inst Lacke & Farben Method and apparatus for making paints
US3830473A (en) * 1973-02-22 1974-08-20 Standard Brands Inc Starch paste apparatus
US4403866A (en) * 1982-05-07 1983-09-13 E. I. Du Pont De Nemours And Company Process for making paints
US5590960A (en) * 1993-11-04 1997-01-07 E. I. Du Pont De Nemours And Company One tank paint makeup process using a recirculation loop with liquid injection

Family Cites Families (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1781435A (en) * 1928-07-06 1930-11-11 Joseph B Carper Process for the production of paints
US3208829A (en) * 1960-09-28 1965-09-28 American Cyanamid Co Apparatus for the segmentation of polymer solutions
US3067987A (en) * 1959-06-19 1962-12-11 Grace W R & Co Two-component mixer
US3244407A (en) * 1964-01-09 1966-04-05 Piazza Engineering Corp Apparatus for feeding and mixing powdered filter aid
US3769232A (en) * 1971-04-26 1973-10-30 Olin Corp Polyurethane foam generating apparatus
US4096586A (en) * 1976-03-04 1978-06-20 Societe D'assistance Technique Pour Produits Nestle S.A. Solubilization of casein
GB1591608A (en) * 1976-09-14 1981-06-24 Agfa Gevaert Method and apparatus suitable for the preparation of silver halide emulsions
DE2659273C2 (en) * 1976-12-29 1985-08-29 Daimler-Benz Ag, 7000 Stuttgart Process for the continuous processing of two-component paints
US4299501A (en) * 1979-08-10 1981-11-10 Ortho Pharmaceutical Corporation Continuous process for the preparation of semisolid dispersions
US4407431A (en) * 1981-03-04 1983-10-04 Hutter Iii Charles G System for dispensing curable compositions
JPS59213469A (en) * 1983-05-16 1984-12-03 Nippon Ranzubaagu Kk Painting method of reaction curing type paint
FR2564333A1 (en) * 1984-05-15 1985-11-22 Ripolin Sa DEVICE FOR DISPENSING LIQUID OR PASTY INGREDIENTS
IT1199500B (en) * 1984-10-12 1988-12-30 Corob Srl METHOD FOR VOLUME DOSING OF DYES IN PAINT PRODUCTS AND RELATED MACHINE
FR2587738B1 (en) * 1985-09-25 1988-02-19 Saint Gobain Isover REPAIR OF BONDING COMPOSITIONS FOR MINERAL FIBERS
US4857355A (en) * 1987-02-10 1989-08-15 Pepsico Inc. Syrup batching loop
DE4135648C1 (en) * 1991-10-29 1993-05-13 Erich Netzsch Gmbh & Co Holding Kg, 8672 Selb, De Mixing powdered solid into liq. phase e.g. for paint mfr.
EP0671203B1 (en) * 1994-03-08 1997-11-26 Agfa-Gevaert N.V. Photographic preparation device
AUPM634794A0 (en) * 1994-06-21 1994-07-14 Pacific Inks (Australia) Pty Ltd System for mixing liquids
US5568266A (en) * 1994-09-28 1996-10-22 Mts Colorimetrie Colorimeter and colorimetrical control device
US5522660A (en) * 1994-12-14 1996-06-04 Fsi International, Inc. Apparatus for blending and controlling the concentration of a liquid chemical in a diluent liquid
JPH0933538A (en) * 1995-07-19 1997-02-07 Toa Medical Electronics Co Ltd Method and unit for preparing reagent
US5632960A (en) * 1995-11-07 1997-05-27 Applied Chemical Solutions, Inc. Two-stage chemical mixing system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3425667A (en) * 1967-03-31 1969-02-04 Inst Lacke & Farben Method and apparatus for making paints
US3830473A (en) * 1973-02-22 1974-08-20 Standard Brands Inc Starch paste apparatus
US4403866A (en) * 1982-05-07 1983-09-13 E. I. Du Pont De Nemours And Company Process for making paints
US5590960A (en) * 1993-11-04 1997-01-07 E. I. Du Pont De Nemours And Company One tank paint makeup process using a recirculation loop with liquid injection

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP0975419A4 *

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6533449B1 (en) * 1998-03-26 2003-03-18 Renner Herrmann S.A. Apparatus and process for the continuous preparation of a fluid, utilizing a fluid recycling means including a buffer
JP2001279188A (en) * 2000-02-18 2001-10-10 John Michael Friel System for manufacturing dispersion type coating material
JP2003340257A (en) * 2002-05-01 2003-12-02 Hewlett Packard Co <Hp> Mixer and mixing method
JP4610864B2 (en) * 2002-05-01 2011-01-12 ヒューレット・パッカード・カンパニー Mixing apparatus and mixing method
US7684045B2 (en) 2005-12-05 2010-03-23 E.I. Du Pont De Nemours And Company Probe apparatus for measuring a color property of a liquid
US7542143B2 (en) 2005-12-05 2009-06-02 E.I. Du Pont De Nemours And Company Liquid measurement cell having a pressurized air cavity therein
US7477394B2 (en) 2005-12-05 2009-01-13 E.I Du Pont De Nemours & Company Method for measuring a color property of a liquid using a liquid measurement cell having a transparent partition therein
US7719686B2 (en) 2005-12-05 2010-05-18 E.I. Du Pont De Nemours And Company System for measuring a color property of a liquid
US7423755B2 (en) 2005-12-05 2008-09-09 E.I. Du Pont De Nemours And Company Liquid measurement cell having a transparent partition therein
EP2719406A4 (en) * 2011-06-08 2015-03-11 Nikkiso Co Ltd Mixing device
US9623166B2 (en) 2011-06-08 2017-04-18 Nikkiso Company Limited Mixing apparatus
WO2018210559A1 (en) 2017-05-19 2018-11-22 Basf Coatings Gmbh Modular production system and method for producing formulations
US11344856B2 (en) 2017-05-19 2022-05-31 Basf Coatings Gmbh Modular production system and method for producing formulations
RU2776169C2 (en) * 2017-05-19 2022-07-14 БАСФ Коатингс ГмбХ Modular production system and method for compositions
CN110141983A (en) * 2019-05-27 2019-08-20 北京半导体专用设备研究所(中国电子科技集团公司第四十五研究所) Photoresist dilution automatically configures device and photoresist dilution automatically configures component

Also Published As

Publication number Publication date
EP0975419A1 (en) 2000-02-02
KR20010006330A (en) 2001-01-26
BR9800361A (en) 2000-09-26
KR100520500B1 (en) 2005-10-11
CA2283730A1 (en) 1999-08-19
CA2283730C (en) 2004-07-13
AR006736A1 (en) 1999-09-29
DE69831063T2 (en) 2006-04-06
JP2002514971A (en) 2002-05-21
CN1560143A (en) 2005-01-05
EP0975419A4 (en) 2001-08-29
DE69831063D1 (en) 2005-09-08
CN1150056C (en) 2004-05-19
ES2244102T3 (en) 2005-12-01
JP3882148B2 (en) 2007-02-14
CN1252011A (en) 2000-05-03
EP0975419B1 (en) 2005-08-03
US6494608B1 (en) 2002-12-17
CN100344359C (en) 2007-10-24

Similar Documents

Publication Publication Date Title
WO1999041003A1 (en) Production of automotive and other paints
US3670785A (en) Method and apparatus for tinting paint
US4345628A (en) Gravimetric diluter
RU2731588C1 (en) Method and a mixing plant for dosed batch-based preparation of a fluid cover material
US3306495A (en) Dispensing apparatus with calibrating means
CA1290744C (en) Process and an apparatus for mixing substances
CA2386433A1 (en) System and method for accurately blending fluids
EP0421742B1 (en) An apparatus for automatically preparing a dyeing solution
EP3940480A1 (en) Paint-production system with automatic self-adjustment of properties of the end product, and related method
JP3267529B2 (en) Paint mixing apparatus and method
US3939005A (en) Method for automatic preparation of solutions of liquid and dry materials
JPH0698879B2 (en) Liquid colorant automatic toning device and toning method
JPS60241923A (en) Automatic blender of liquid fluid such as dyeing solution and pigment solution
WO1996023580A1 (en) Method and apparatus for dosing and mixing liquid substances
JPS631434A (en) Dye liquid preparing apparatus
JPH06106039A (en) Method and device for mixing toning raw material
JP2001239189A (en) Coating line system for shop primer
Turner The Automated Drug Room.
CN116492890A (en) Automatic batching system for water-based paint
JPH0226533B2 (en)
JP2001198448A (en) Mobile liquid agent mixer
JPH0798142B2 (en) Grain mixing equipment
JPS63274439A (en) Liquid and powder weighing and mixing apparatus
JPS6230919A (en) Automatic apparatus for injection and weighing
JPS60161735A (en) Fluid dividing and taking-out apparatus

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 98804129.4

Country of ref document: CN

AK Designated states

Kind code of ref document: A1

Designated state(s): CA CN JP KP KR MX US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE

ENP Entry into the national phase

Ref document number: 2283730

Country of ref document: CA

Ref document number: 2283730

Country of ref document: CA

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: 1998960943

Country of ref document: EP

Ref document number: 09402437

Country of ref document: US

ENP Entry into the national phase

Ref document number: 1999 540841

Country of ref document: JP

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: PA/a/1999/009333

Country of ref document: MX

WWE Wipo information: entry into national phase

Ref document number: 1019997009415

Country of ref document: KR

121 Ep: the epo has been informed by wipo that ep was designated in this application
WWP Wipo information: published in national office

Ref document number: 1998960943

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1019997009415

Country of ref document: KR

WWG Wipo information: grant in national office

Ref document number: 1998960943

Country of ref document: EP

WWG Wipo information: grant in national office

Ref document number: 1019997009415

Country of ref document: KR