JPS609753A - Ink manufacturing device - Google Patents

Abstract

PURPOSE:To make it possible to mass produce a kind of ink which is suitable for ink jet recording and writing pens by such an arrangement wherein plural processing units for refining dye solution by the execution of chromatography are provided and the preparation of a kind of ink is performed by using such refined dye solution. CONSTITUTION:A refining unit 41 which excludes inorganic salts from dye aqueous solution is composed of plural number of hypochlorization processing unit 42. A supply valve open/close unit 43 controls whether supplied dye aqueous solution, pure water and the secondary solution are to be supplied to a hypochlorization filter unit 44 or not. The hypochlorization filter unit 44 excludes inorganic salts from dye aqueous solution and the secondary solution supplied from the supply valve open/close unit 43 by chromatography. By the control of a discharge valve open/close unit 45, the dye aqueous solution of which inorganic salt density has been lowered less than a specified value by refining is discharged into a storing tank 56 through a discharge pipe 55. The aqueous solution discharged from the filter unit 44 is discharged into an inorganic salt solution discharging unit 58 or into a discharge pipe 59 through a discharge pipe 57 according to the density of its ingredient.

Description

DETAILED DESCRIPTION OF THE INVENTION (Technical Field) The present invention relates to an ink manufacturing apparatus, and more particularly to an ink manufacturing apparatus suitable for preparing recording axes (generally referred to as ink) suitable for inkjet recording, writing instruments, and the like.

(Prior Art) Conventionally, the ink used in the inkjet recording method, in which recording is performed by ejecting ink in a recording head from an ejection orifice using vibrations caused by a piezo vibrator, has been made by mixing various dyes and pigments with water or other organic solvents. It is known to be dissolved or dispersed in a liquid medium consisting of: It is also known that similar inks are used in writing instruments such as felt pens and fountain pens.

An example of a general basic composition of such an ink is one in which the main components are a water-soluble dye, water as its solvent, and the king of glycols as an anti-drying agent.

Here, the water-soluble dye usually contains a large amount of inorganic salts such as sodium chloride and sodium sulfate. These inorganic salts are not only those produced as by-products during the dye synthesis reaction process, but also those that are actively added as salting-out agents, diluents, or leveling agents.

When recording inks are prepared using dyes containing such inorganic salts, the following disadvantages arise. In other words, inorganic salts reduce the stability of dye dissolution in ink.
Causes dye aggregation and precipitation. Furthermore, in inkjet recording heads and writing instruments, if the ink evaporates near the ejection orifice and the composition changes, inorganic salts will precipitate. All of these causes clogging of the discharge orifice, which is most avoided.

Therefore, in order to eliminate such adverse effects, it is necessary to control the concentration of inorganic salts within a predetermined range (generally 0.5% by weight or less in the ink) during ink production. This is essential when a commercially available dye containing inorganic salts as an impurity is used to prepare an inkjet recording ink or a writing instrument ink.

(Objective) In view of these points, the object of the present invention is to eliminate inorganic salts contained in dye solutions when preparing ink, and thereby mass-produce ink suitable for inkjet recording, writing instruments, etc. An object of the present invention is to provide an ink manufacturing apparatus that can obtain the following effects.

To this end, the present invention is provided with a plurality of processing sections that purify (salt-reduced) dye solutions by performing chromatography, and ink is prepared using the dye solutions purified by these processing sections.

(Example) The present invention will be described in detail below with reference to the drawings.

FIG. 1 shows an embodiment of an ink manufacturing apparatus according to the present invention. Here, 1 is an ink preparation tank, and an aqueous dye solution purified as described below is supplied from a dye purification device 2 via a valve 3. In addition, from the storage section 4 and the storage section 5,
The water-soluble organic solvent and additives are fed into the formulation tank l via valves 6 and 7, respectively. Furthermore, pure water is also supplied via valve 8. Each of these supplied materials is stirred by a stirrer 9 to prepare ink.

The amount of ink produced in the mixing tank 1 is detected by a liquid amount detector 10.
Detected by. Further, the dye concentration and inorganic salt concentration in the ink prepared in the mixing tank 1 are detected by a dye concentration detector 11 and an inorganic salt concentration detector 12, respectively. Based on the outputs of these rain detectors, final property management (lot management) of the prepared ink is performed. The ink whose components have been adjusted to desired values is discharged via the discharge valve 13 as necessary.

14 is a control unit that controls the drive of each part; 15
is an operation section equipped with various display sections, drive switches, etc.

FIG. 2 shows the structure of the dye purification apparatus in the apparatus shown in FIG.

Here, 21 is a dye supply section that stores dye powder 22, and supplies the dye powder 22 to a mixing tank 24 via a dye valve 23. In addition, a pure water valve 2 is provided in the mixing tank 24.
Pure water is supplied through a pure water supply pipe 28 in which a pipe 5 is inserted.

In this mixing tank 24, the supplied dye powder 22 and pure water are mixed and dissolved by a mixing tank agitator 27 to produce an aqueous dye solution. The amount of the aqueous dye solution stored in the mixing tank 24 is detected by a mixing tank liquid amount detector 28 . The aqueous dye solution obtained in the mixing tank contains particles of dye powder that were not dissolved in the pure water, and these are removed by the filter 29. This filter 29 has
Ordinary filter paper or Fluoropore (trade name) can be used. The aqueous dye solution from which particles and the like have been removed by passing through the filter 29 is supplied to the supply tank 31 .

The aqueous dye solution supplied to the supply tank 31 is supplied to the purification section described below via the supply pipe 32. Here, this supply tank 31 is provided with a valve 33 for controlling the liquid level to suppress the amount of the aqueous dye solution stored in the supply tank to a certain amount or less.

Next, 41 is a purification section that removes S base salts from the dye aqueous solution, and includes a plurality of salt reduction treatment units 42 (42-1 to 42-1).
2-N). In the salt reduction processing unit 42, 4
3 (43-1 to 43-N) are supply valve opening/closing parts, 44 (
44-1 to 44-N) are salt reduction filter parts, and 45 (
45-1 to 45-N) are discharge valve opening/closing parts.

The supply valve opening/closing section 43 includes a dye aqueous solution supply pipe 47 (m
7-t~47-N), pure water supply pipe 4B (46-1~4
B-N) and secondary solution supply pipe 48 (4B-1 to 48-
N) are communicated with each other. The aqueous dye solution is supplied from the supply tank 31 to the opening/closing section 43 via the supply pipes 32 and 47 sequentially, and the pure water is supplied sequentially via the supply pipes 26 and 4B.

Further, a secondary solution, which will be described later, is supplied to the supply valve opening/closing section 4 via the secondary solution storage tank section 51 and supply pipes 52 and 48 in sequence.
Supply to 3.

The supply valve opening/closing section 43 controls whether or not the supplied aqueous dye solution, pure water, and secondary solution are supplied to the salt reduction filter section 44 .

; In the salt-reducing filter section 44, by chromatography,
Inorganic salts are removed from the aqueous dye solution and secondary solution supplied from the supply valve opening/closing section 43.

By controlling the discharge valve opening/closing section 45, the concentration of inorganic salts is reduced to a predetermined value (for example, 5% for the dye) through such (salt reduction) purification.
Discharge the dye aqueous solution that has become less than (% by weight). '55 (
55-1 to 55-N) to the storage tank 5B.

Further, the aqueous solution discharged from the filter section 44 is transferred to the discharge pipe 5 depending on its component concentration. (57-1 to 57-N) to the inorganic salt solution discharge part 5, or the discharge pipe 5!3 (
59-1 to 59-N).

One end of this discharge pipe 59 is communicated with a suction boat of a circulation pump 6o, and the aqueous dye solution discharged to the discharge pipe 59 is passed through a discharge pipe 61 communicated with the discharge boat by this pump 60 to two. The next solution is fed under pressure to the solution storage tank 51.

In this way, the refluxed dye aqueous solution is supplied to the purification unit 41 again as a secondary solution from the discharge side of the purification unit 41, and (
Salt reduction) purification.

In addition, 74 is a discharge valve arranged in the discharge tank 58,
The inorganic salt solution is discharged through this valve 74.

FIG. 3 shows the configuration of the salt reduction processing unit 42 shown in FIG. 2.

In the figure, the first supply valve 431 in the supply valve opening/closing section 43 is controlled to open and close to control the supply of pure water to the salt reduction filter section 44 via the supply pipe 46.

Similarly, the second supply valve 432 and the third supply valve 43
2 to the salt-reducing filter section 44 by controlling the opening and closing of 3.
Control the supply of the next solution and the aqueous dye solution.

Next, the salt-reducing filter section 44 separates inorganic salts from the dye aqueous solution by chromatography. That is, the dye static aqueous solution is supplied to the upper end of the chromatography column 441 from the supply valve opening/closing 8843. While the supplied aqueous dye solution descends within the column 441, each component in the aqueous solution is separated. Through such a developing operation (chromatography),
The components with the weakest adsorption properties flow out first. Therefore,
By detecting the component concentration of the effluent solution, based on the detection result, it is possible to extract only the aqueous dye solution in which the concentration of inorganic salts is below a predetermined concentration from the effluent melt.

Inorganic salt concentration detector 442 and dye concentration detector 443
is for detecting the concentration of inorganic salts and dye in the solution flowing out from the column 441, and is disposed in the flowing liquid passage 444 at the lower end of the chromatography column 441. As a method of detecting each component, the concentration of inorganic salts is determined by measuring conductivity.

There are methods using ionic current, and methods for measuring dye concentration by spectrophotometry.

A dye solution is supplied to the chromatography column 441 in fixed amounts for purification (salt reduction).For this purpose, a liquid level position detector 445 is installed at the upper end of the column to detect the dye solution. Based on the result, the supply of the aqueous solution from the supply valve opening/closing section 43 is controlled.

Here, the stationary phase filled in the column 441 generally includes ion exchange resins, chelate resins, etc.
In this example, an ion retardation resin, such as Retardion IIA, is used.
-8 (trade name: manufactured by Dow Chemical Company) is used. Ion retardation resins do not require regeneration agents, can be regenerated with pure water, and are nearly neutral, so they are advantageous for desalting substances that are unstable to acids and alkalis.

FIG. 4 shows an outflow curve in which the concentration of each component of the outflow solution from the chromatography column 441 is plotted against the time axis, that is, the fractionation characteristics. As shown, the dye concentration (curve I) peaks between time Tl and T2, and the inorganic salt concentration (curve I) peaks between time Tl and T2.
Line ■) reaches its peak between time 73 and time 74. In this example,
Based on such classification characteristics, the inorganic salt concentration detector 44
2 and the detection value of the dye concentration detector 443, the effluent solution from the chromatography column 441 is fractionated and extracted as follows.

That is, when the dye concentration of the effluent solution is equal to or higher than the predetermined value C2 (effective dye concentration) and the inorganic salt concentration is less than the predetermined value C3 (allowable inorganic salt concentration) (between times 11 and 72), the effluent solution is transferred to the storage tank. Leads to 56. However, after the inorganic salt concentration exceeds the value C3 and the dye concentration falls below the value C2, the effluent solution is directed to the inorganic salt solution discharge tank 58. Also,
The effluent solution is refluxed to the secondary solution storage tank 51 during the period from when the inorganic salt concentration reaches the value C3 or higher until the dye concentration becomes the value C2 or lower (between times 72 and 73).

Referring again to FIG. 3, the discharge valve opening/closing section 45 separates the outflow solution as described above, and the outflow passage 444
is branched into three prongs, and each branch pipe and discharge pipe 57, 59 and 55 are connected to the first pipe. Second and third discharge valve 4
51, 452 and 453. With this configuration, by opening the first discharge valve 451, the effluent solution can be discharged to the inorganic salt solution discharge tank 58, and similarly, by opening the second and third discharge valves 452 and 453, the effluent solution can be discharged into the inorganic salt solution discharge tank 58. Next solution storage tank 51
and can be led to storage tank 56.

FIG. 5 shows the control system of the apparatus shown in FIG. here 10
Reference numeral 1 denotes a controller, which controls the drive of each part. 10
A read-only memory (ROM) 2 stores a control program such as the operating procedure shown in FIG. A random access memory (RAM) 103 temporarily stores various data.

Reference numeral 104 denotes various switches arranged in the operation unit 15, which send various command signals to the controller 101 via the input/output buffer circuit 105. Reference numeral 106 designates a display device similarly disposed on the operation unit 72, and reference numeral 107 designates a drive circuit that controls the display of the display device 108 based on a drive signal from the controller 101.

In this example, analog signals are output from the inorganic salt concentration detector 442 and the dye concentration detector 443, and are converted into digital signals via A/D converters 111 and 112, respectively, and then sent to the input buffer circuit +13. The signal is supplied to the controller 101 via the controller 101. On the other hand, the liquid level position detector 445 outputs a digital signal, and the input buffer circuit 113
1 is integrated into the controller 101 via the controller 101.

121 to 126 are the aforementioned valves 431, 432, 4.
33.

This is a drive circuit for opening and closing 451, 452, and 453, respectively, and is ON/OFF controlled by a drive signal supplied from the controller 101 via the output buffer circuit 127.

In addition, since the configurations of the g salt processing units 42-1 to 42-N are the same, only the unit h 42-1 is shown in the figure, and the other units 42-2 to 42-N are omitted. be.

The eighth quotient shows the operation of each processing unit in this embodiment configured as described above.

In the figure, when a start command is received from the operation unit 15 in step STI, the program switch is set to OFF in step ST2. Next, in step ST3, the second and third supply valves 432 and 433 are opened to start supplying the dye aqueous solution in the supply tank 31 and the secondary solution in the secondary solution storage tank 51 into the chromatography column 441. This supply operation continues until the liquid level in the column 441 reaches the highest position H (see FIG. 3) according to the output of the liquid level position detector 445 in step ST4. When the liquid level height H reaches the maximum position, that is, when a predetermined amount of aqueous solution has been supplied to the column, step ST
5, both valves 432 and 433 are closed.

Next, in step ST8, the first exhaust valve 451
is opened, and the effluent solution from the chromatography column 441 begins to be discharged to the inorganic salt solution discharge tank 58.

Step ST? In this step, it is determined whether the liquid level in the column is at the lowest position (see FIG. 3). Immediately after supplying the dye aqueous solution and secondary solution,
Since the liquid level is above the lowest position, the determination is "NO" and the process proceeds to step S78. In step ST8, the first supply valve 431 is closed, and the process proceeds to step 5TIO. Here, as mentioned above, immediately after the dye aqueous solution and the secondary solution are supplied and the developing operation is started in the column 441, the concentration of each component of the effluent solution is shown between time 0 and T1 in FIG. in a state. Therefore, in step 5TIQ, the dye concentration detector 443
The determination as to whether the detected density value is equal to or greater than the effective dye density value 02 is "NO", and the process proceeds to step 5TII. Furthermore, in step 5TII, the determination as to whether the concentration value detected by the inorganic 1J7 type concentration detector 442 is equal to or higher than the cleaning S base salt concentration value C1 is determined as "NO", and the process proceeds to step 5T12. In step 5TI2, it is determined whether the program switch is in the on state. In the first loop, since it is in the off state, the determination is "NO" and the process returns to step ST7. Like this, step ST7→ST8→5TIO→
The loop of 5TII→S12 is repeated until rYESJ is determined in step 5TIO.

Note that when it is determined in steps S and T7 that it is rYEsJ, the process proceeds to step ST9, the first supply valve 431 is opened, and pure water is supplied to the column 441. Therefore, in such a case, steps ST7→ST9→
A loop of 5TIO→5TII→5T12 is executed.

In step 5 TIO, when the dye concentration value of the ejected solution from column 441 becomes equal to or greater than the effective dye concentration value 02 (
At time Tl in FIG. 4, the process proceeds to step '3T13. In step 5T13, the inorganic salt concentration value detected by the inorganic salt J agricultural level detector 442 is determined as the allowable inorganic salt concentration value C.
It is determined whether the number is 3 or more.

Here, due to the development operation of the chromatography column 441, the dye aqueous solution from which the inorganic salts have been separated flows out first (fourth column).
(Refer to time Tl-72 in the figure), and in step 5T13, "N
It is determined as "O" and the process proceeds to step 5T14. In step 5T14, the first exhaust valve 451 is closed, and in step 5TI5, the third exhaust valve 45
3 is performed, and the effluent solution from the chromatography column 441 is discharged to the storage tank 5B through the discharge pipe 55.

Next, in step 5T1B, the program switch is turned on, and the process returns to step ST7. Step ST like this? →ST8→5TIO→5T13→5T14→5T
15→5T1B or step ST? →ST9→5TI
The loop of O→5TI3→5T14-5T15→Sτ16 is repeated, and an aqueous dye solution whose inorganic salt concentration has been purified to below the allowable value C3 is obtained in the storage tank 56. This loop continues until rYEsJ is determined in step 5T13.

As shown in FIG. 4, when the inorganic salts start to flow out and the inorganic salt concentration of the effluent solution increases and becomes equal to or higher than the allowable inorganic salt concentration value C3 (time Tl in FIG. 4), steps 5T13 to The process proceeds to step 5T17, where the third exhaust valve 453 is closed, and the second exhaust valve 452 is opened at step 5T18. As a result, the outflow solution is stopped from being discharged to the storage tank 56 and is discharged to the discharge pipe 58. here,
In this example, assuming that the circulation pump 60 is driven in synchronization with the opening operation of the valve 452, the effluent solution is transferred to the discharge pipe 59.8.
1 to the secondary solution storage tank 51. This refluxing operation of the effluent solution is performed in step 5TIO by "NO
” continues until it is determined that The secondary solution recovered in this way will be purified again to reduce salt. next,
When the dye concentration of the effluent solution decreases and its value falls below the effective dye concentration value C2 (time Tl in Figure 4), step 5T
When the IO determines “NO”, the process proceeds to step 5T11.
Proceed to. Now, since the inorganic salts are continuing to flow out, it is determined as rYES J in step 5TII, and the process proceeds to step 5T19, where the second discharge valve 452 is closed, and furthermore, in step 5T20, the first discharge valve 451 is opened. It will be done. As a result, the effluent solution is 2
The rapid wave to the next solution storage tank 51 is stopped, and the solution begins to be discharged to the inorganic salt solution storage tank 58 via the discharge pipe 58. This draining operation is continued until the inorganic salt concentration of the effluent solution falls below the cleaning inorganic salt concentration value C1.

When the inorganic salt concentration falls below the value C1 (time Tl in Figure 4)
, the determination in step 5TII is "NO" and the process proceeds to Stella 7'5T12. Here, since the program switch is set to ON in step 5T1B as described above, rYES is selected in step 5T12.
If the determination is J, the process proceeds to step 5T21, where the first discharge valve 451 is closed and the discharge of the outflow solution to the discharge tank 58 is completed.

Next, in step 5T22, the supply valve 431 is closed, and the supply of pure water to the chromatography column 441 is stopped. That is, in this example, the first supply valve 431 is controlled to open and close so that the liquid level of the aqueous solution in the chromatography column 441 is always at the lowest position (see FIG. 3), and pure water is supplied (Stella 7 'Sr1, STI')
. This pure water washes the stationary phase inside the chromatography column (
regeneration) is carried out. As described above, when the inorganic salt concentration of the effluent solution falls below the cleaning inorganic salt concentration CI, it is determined that cleaning (regeneration) has been performed and the supply of pure water is stopped.

After executing step 5T22, step STI is executed again.
Return to and wait for the start command.

One (salt reduction) purification operation is completed as described above. In addition, in this embodiment, each processing unit l-42-
Although the operations 1 to 42-N are executed synchronously, they are not limited to this, and of course may be executed sequentially, for example.

Further, in this embodiment, the collected secondary solution is purified in each processing unit 42, but a separate processing unit exclusively for the secondary solution may be provided to perform the purification.

(Effects) As explained above, according to the present invention, in manufacturing ink, a plurality of processing sections are provided for purification (salt reduction) by performing chromatography, and inorganic salts are eliminated by these processing sections. Since the purified dye solution is continuously supplied, mass production of stable quality ink suitable for inkjet recording, writing instruments, etc. can be carried out continuously and automatically.

[Brief explanation of the drawing]

FIG. 1 is a schematic diagram showing an embodiment of the apparatus according to the present invention, FIG. 2 is a diagram showing the dye purification apparatus of FIG. 1, and FIG. 3 is a diagram showing the salt reduction treatment unit of FIG. 2. , Fig. 4 is a characteristic curve diagram showing the separation characteristics of the chromatographic column, Fig. 5 is a block diagram showing the control section of the apparatus shown in Fig. 1, and Fig. 6 is a diagram of the salt reduction processing unit of the apparatus shown in Fig. 1. It is a flowchart showing the operation. l...Ink mixing tank. 2...Dye refiner, 3...Valve, 4...Reservoir, 5...Reservoir, 6...Valve, ? ... Valve, 8... Valve, 9... Stirrer, IO... Liquid amount detector, 11... Dye concentration detector, 12... Inorganic salt concentration detector, I3... Discharge Valve, 14...Control unit, 15...Operation unit, 21...Dye supply unit, 22...Dye powder, 23...Dye valve, 24...Blending tank. 25... Pure water valve, 28... Pure water supply pipe, 27... Preparation tank agitator 28... Preparation tank liquid level detector, 28... Filtration filter, 31... Supply tank, 32... Supply pipe, 33... Valve, 41... Refining section, 42... Salt reduction processing unit, 43... Supply valve opening/closing section, 44... Salt reduction filter section, 45... - Discharge valve opening/closing part, 46... Dye aqueous solution supply pipe, 47... Pure water supply pipe, 48... Secondary solution supply pipe, 51... Secondary solution storage tank, 52... Supply pipe , 55... Discharge pipe, 56... Storage tank, 57... Discharge pipe, 58... Inorganic salt solution discharge tank, 59... Discharge pipe, 60... Circulation pump, 61... Discharge pipe, 74... Discharge valve, 101... Controller, 102... Read only memory, 103... Random access memory, +04... Switch. 105... Input/output buffer circuit, 106... Display device, 107... Drive circuit, 111.112... A/D converter, 113... Input 4 buffer circuit, 121-126... Drive circuit, 127... Output buffer circuit, 431.432, 433... Supply valve, 441.
...Chromato column, 442...Inorganic salt concentration detector, 443...Dye concentration detector, (23) 444...Outflow passage, 445...Liquid level position detector, 451.452,453. ...Exhaust valve. Patent applicant Canon Co., Ltd. (24)

Claims (1)

[Claims] The invention comprises a means for producing a dye solution, a plurality of purification means for performing chromatography using the solution, and an ink preparation section for preparing ink using the purified dye solution discharged from the plurality of purification means. An ink manufacturing device featuring: