JPS59182863A - Apparatus for purification of dye - Google Patents

Apparatus for purification of dye

Info

Publication number
JPS59182863A
JPS59182863A JP5529983A JP5529983A JPS59182863A JP S59182863 A JPS59182863 A JP S59182863A JP 5529983 A JP5529983 A JP 5529983A JP 5529983 A JP5529983 A JP 5529983A JP S59182863 A JPS59182863 A JP S59182863A
Authority
JP
Japan
Prior art keywords
dye
concentration
salt
tank
solution
Prior art date
Legal status (The legal status 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 status listed.)
Pending
Application number
JP5529983A
Other languages
Japanese (ja)
Inventor
Masahiro Haruta
春田 昌宏
Kunitaka Ozawa
小澤 邦貴
Takashi Hamamoto
浜本 敬
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Canon Inc
Original Assignee
Canon Inc
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 Canon Inc filed Critical Canon Inc
Priority to JP5529983A priority Critical patent/JPS59182863A/en
Publication of JPS59182863A publication Critical patent/JPS59182863A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To carry out the continuous and automatic mass-production of purified dye having high quality and suitable as the ink for writing utensils, etc., by using a means for the preparation of a dye solution in combination with a means for detecting the concentration of inorganic salt in said solution, and a means to control the salt concentration according to the output signal of the detecting means. CONSTITUTION:Dye powder 22 is fed from the dye reservoir 21 to the mixing tank 24, and the prepared dye solution is supplied through the supply tank 31 to the purification zone 41 furnished with a detector 46 to detect the concentration of inorganic salt by ion chromatography, etc. When the concentration of the salt detected by the detector 46 is higher than a preset level (preferably <=5wt%), the solution is passed through the salt-rejection filter 43 by operating the circulation pump 48 to obtain the purified dye. The excess salt is discharged to the waste tank 44.

Description

【発明の詳細な説明】 [技術分野] 本発明は染料精製装置に関し、特にインクシェフ 1−
記録や筆記具等に適した記録液(一般にインクと呼ぶ)
の調製に好適な精製染料を連続供給する染料精製装置に
関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field] The present invention relates to a dye purification device, and particularly to an ink chef 1-
Recording fluid (generally called ink) suitable for recording and writing instruments, etc.
This invention relates to a dye purification device that continuously supplies purified dye suitable for the preparation of dyes.

[従来技術] 従来、ピエゾ振動子による振動等により記録ヘンド内の
インクを吐出オリフィスから吐出させて記録を行うイン
クジェy l・記録方式に使用するインクとしては、各
種の染料、顔料を水またはその他の有機溶剤からなる液
媒体中に溶解あるいは分散させたものが知られている6
また、フェル)・メン、万年筆等の筆記具においても同
様なインクが使用されることが知られている。
[Prior Art] Conventionally, inkjet recording methods in which recording is performed by ejecting ink in a recording head from an ejection orifice using vibrations caused by a piezoelectric vibrator, etc. Ink used in the recording method include various dyes and pigments mixed with water or other materials. It is known to be dissolved or dispersed in a liquid medium consisting of an organic solvent6.
It is also known that similar inks are used in writing instruments such as pens and fountain pens.

このようなインクの一般的な基本構成例としては、水溶
性染料、その溶媒であろ水および乾燥防止剤であるグリ
コール類の三者を主成分として成るものをあげることが
できる。
An example of a general basic composition of such an ink is one consisting of three main components: a water-soluble dye, water as its solvent, and glycols as an anti-drying agent.

ここで、水溶性染料には、塩化ナトリウムや値酸ナトリ
ウムなどの無機塩類が多量に含まれているのが普通であ
る。これらのS機塩類は、染料合成反応の過程で副生じ
たものの他に、塩析剤、希釈剤あるいは均染剤として積
極的に添加されたものである。
Here, the water-soluble dye usually contains a large amount of inorganic salts such as sodium chloride and sodium chloride. These S machine 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.

このような無機塩類を含む染料で記録用インクを調製す
ると、次のような不都合な事態を招来する。すなわち、
無機塩類はインク中の染料溶解安定性を低化せしめ、染
料の凝集、沈殿をもたらす。また、インクジェット記録
ヘンドや筆記具においては、吐出オリフィス付近でイン
クが蒸発して液組成が変化すると、無機塩類の析出をひ
き起す。これらはいずれも、最も、8避すべき吐出オリ
フィスの目詰まりの原因となる。
When recording ink is prepared using dyes containing such inorganic salts, the following disadvantages occur. That is,
Inorganic salts reduce the stability of dye dissolution in the ink, leading to aggregation and precipitation of the dye. In addition, in inkjet recording heads and writing instruments, if the ink evaporates near the ejection orifice and the liquid composition changes, this causes precipitation of inorganic salts. All of these are the most likely causes of clogging of the discharge orifice, which should be avoided.

そこで、かかる弊害を除去するために、インクの製造に
際して無機塩類濃度が所定の範囲内(−nシには、イン
ク中に0.5重蓋%以下とする)になるように制御する
8閥がある。このことは、無機塩Mを不純物として含む
一般の市販染料を、インクジェット記録用インクや筆記
具用インクの調製に用いる場合に、不可欠である。
Therefore, in order to eliminate such adverse effects, eight methods are used to control the concentration of inorganic salts within a predetermined range (for -n, the concentration of inorganic salts in the ink should be 0.5% or less). There is. This is essential when a general commercially available dye containing the inorganic salt M as an impurity is used for preparing an inkjet recording ink or a writing instrument ink.

[目的] 未発ul]の目的は、このような点に鑑みて、インクの
調製を行うにあたり、インク中に含まれるフ11)、機
塩類を制御し、以てインクジェット記録用イ7りやJs
p記具用具用インク調製に好適な精製した染オ′I溶液
をX!l!続供給し得るようにした染料精製装置を提供
することにある。
[Purpose] In view of these points, the purpose of the unreleased UL is to control the fu11) and mechanical salts contained in the ink when preparing the ink, thereby improving the quality of inkjet recording materials and Js.
A purified dye O'I solution suitable for preparing ink for marking utensils was prepared using X! l! An object of the present invention is to provide a dye purification device that can be continuously supplied.

[実施例] 以十′、図面に従って本発明の詳細な説明する。[Example] The present invention will now be described in detail with reference to the drawings.

第1図は本発明装置の一実施例を示す。FIG. 1 shows an embodiment of the apparatus of the present invention.

ここで、2Iは染料粉末22を貯留した染料供給部であ
り、染料/ヘルプ23を介してその染料粉末22を調合
槽24に供給する。また、調合4pJ24には、純水バ
ルブ25を介挿した純水供給パイプ28を介して純水を
供給する。
Here, 2I is a dye supply unit that stores the dye powder 22, and supplies the dye powder 22 to the mixing tank 24 via the dye/help 23. Further, pure water is supplied to the mixture 4pJ24 through a pure water supply pipe 28 in which a pure water valve 25 is inserted.

この調合槽24では、供給された染料粉末22および純
水を調合槽撹拌機27により混合、溶解して、染料水溶
液をつくるものである。調合槽24内に貯留している染
料水溶液の液量は、調合槽液部検出器28により検出す
る。調合槽内に得られた染料水溶液には、純水に溶解し
なかった染料粉末の粒子等が残存しており、これをろ過
フィルタ29により除去する。このフィルタ29には、
通常のろ紙またはフロロボア(商品名)等を用いること
かできる。フィルタ29を通過させて粒子等を除去した
染料水溶液を、供給槽31に供給する。
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 portion 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 Fluorobor (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 .

供給槽31に供給された染料水溶液は、供給バルブ32
が閉状態にある限り、供給槽31内に貯留される。ここ
で、この供給槽31には、液面高さ制御用の3’7−3
3を配設し、供給槽内に貯留される染料水溶液の敬を一
定策以下に抑える。
The aqueous dye solution supplied to the supply tank 31 is passed through the supply valve 32.
is stored in the supply tank 31 as long as it is in the closed state. Here, this supply tank 31 has a 3'7-3 for controlling the liquid level height.
3 is installed to suppress the temperature of the dye aqueous solution stored in the supply tank to below a certain level.

次に、41は染料水溶液から無機塩類を排除する精製部
である。この精製部41において、42は減塩槽、43
は減塩フィルタであり、44は排塩槽である。減塩槽4
2には、供給バルブ32を介して染料水1容滴を供給す
る。この供給された染料水溶液を、il& JM槽撹拌
機45により撹拌して、その水溶液を均一化し、無機塩
類濃度検出器46によりその水溶液中の無機塩類の濃度
を検出する。この濃度検出は、例えばイオンクロマトグ
ラフィー法に−より行う。また、染料濃度検出器47に
より、その水溶液中の染料濃度を検出する。この濃度検
出は、例えは分光光度法により行うものである。後述の
ように、無機塩類の濃度が所定値(例えば、染料に対し
て5IT(量%)以−J−であることが検出されると、
循環ポンプ48を作動させて、減塩槽内の染料水溶lt
4をi斌1j4 フィルタ43を介して循環させる。こ
の減小フィルタとしては、例えば限外ろ過フィルタ。
Next, 41 is a purification section that removes inorganic salts from the aqueous dye solution. In this purification section 41, 42 is a salt reduction tank, 43
is a salt reduction filter, and 44 is a salt removal tank. Salt reduction tank 4
2, one volume drop of dye water is supplied via the supply valve 32. The supplied aqueous dye solution is stirred by an IL&JM tank stirrer 45 to homogenize the aqueous solution, and an inorganic salt concentration detector 46 detects the concentration of inorganic salts in the aqueous solution. This concentration detection is performed, for example, by ion chromatography. Further, a dye concentration detector 47 detects the dye concentration in the aqueous solution. This concentration detection is performed, for example, by spectrophotometry. As described below, when it is detected that the concentration of inorganic salts is a predetermined value (for example, 5IT (volume %) or more with respect to the dye),
The circulation pump 48 is operated to remove the dye aqueous solution in the salt reduction tank.
4 is circulated through the ibin1j4 filter 43. This reduction filter is, for example, an ultrafiltration filter.

i!!4 fsL透フィルタ等を用いる。かかる減塩フ
ィルタ43を通過させることにより、染料水溶液に含ま
れ′する塩化ナトリウムや硫酸ナトリウム等の無a塩が
水溶液として染料水溶液中からろ過されて、排塩槽44
に排出される。このように、υト塩槽44には、染料の
溶媒である水の一部が無機塩類と共にり1出されてしま
う。そこで、この排出された分の水を染料水溶液に補充
すると共に、減塩槽42内において所望濃度の染料水溶
液が得られるように、純水バルブ48を介して減塩槽4
2に純水を供給する。
i! ! 4 Use an fsL transparent filter, etc. By passing through the salt-reducing filter 43, aqueous salts such as sodium chloride and sodium sulfate contained in the aqueous dye solution are filtered out from the aqueous dye solution, and the salt is removed from the salt removal tank 44.
is discharged. In this way, a portion of the water, which is a solvent for the dye, is discharged into the salt tank 44 along with the inorganic salts. Therefore, in addition to replenishing the dye aqueous solution with this discharged water, the salt-reducing tank 42 is connected to the salt-reducing tank 42 via a pure water valve 48 so that a dye aqueous solution with a desired concentration is obtained in the salt-reducing tank 42.
Supply pure water to 2.

このようにして、減塩槽42内に、無機塩類濃度および
染料濃度が所定範囲内のイ16である染料水溶液を得る
。なお、減塩槽42内の染料水溶液の量を、減塩槽液量
検出器50により検出する。
In this way, an aqueous dye solution having an inorganic salt concentration and a dye concentration within a predetermined range is obtained in the salt reduction tank 42. Note that the amount of dye aqueous solution in the salt reduction tank 42 is detected by a salt reduction tank liquid amount detector 50.

上述のように(減塩)精製した後の染料水溶液を、貯蔵
バルブ51を介して貯蔵槽52に排出し、その貯蔵槽内
に貯蔵する。
The aqueous dye solution purified as described above (salt reduction) is discharged into the storage tank 52 via the storage valve 51 and stored in the storage tank.

第2図は第1図に示す装置の制御系を示す。ここで、6
1は制御器であり、各部の駆動制御をつかざどる。62
はリードオンリメモリ(ROM)であり、第3図に示す
動作手順等の制御プログラムが記憶されている。83は
ランタムア゛クセスメモリ(RAM)であり、各種テー
クの一時記憶等がなされる。
FIG. 2 shows the control system of the apparatus shown in FIG. Here, 6
Reference numeral 1 denotes a controller, which controls the drive of each part. 62
is a read-only memory (ROM) in which a control program such as the operating procedure shown in FIG. 3 is stored. 83 is a random access memory (RAM) in which various takes are temporarily stored.

本例では、無機塩類濃度検出器46および染料濃度検出
器47からは、アナログ信号が出力され、それぞれA/
D変換器64および65を介してデジタル1ご号に変換
された後、大力4フファ回路66を介して制御器61に
供給される。一方、調合槽液量検出器28およびイ戊塩
槽液量検出器50からはそれぞれデジタル信号が出力さ
れ、入カパッファ回路66を介して制御器61に供給さ
れる。
In this example, analog signals are output from the inorganic salt concentration detector 46 and the dye concentration detector 47, and each A/
After being converted into a digital number 1 via the D converters 64 and 65, it is supplied to the controller 61 via a large-power 4-FF circuit 66. On the other hand, digital signals are output from the mixing tank liquid level detector 28 and the salt tank liquid level detector 50, respectively, and are supplied to the controller 61 via the input buffer circuit 66.

67〜74は前述した各バルブ23.2’5,48.3
2および51、撹拌機27および45、ならびに循環ポ
ンプ48をそれぞれ1ス動するためのドライブ回路であ
り、制御器61から出力バッファ回路75を介して供給
される駆動信号によりオンオフ制御される。
67 to 74 are the aforementioned valves 23.2'5, 48.3
2 and 51, the stirrers 27 and 45, and the circulation pump 48 by one stroke, and are controlled to be turned on and off by a drive signal supplied from the controller 61 via the output buffer circuit 75.

81および82は、それぞれ染料濃度範囲設定スイフチ
および無機塩類濃度範囲設定スイッチであり、jJ定さ
れたJ震度範囲に対応する信号がコンソール入出力42
27回路83を介17て制御器に供給される。84およ
び85は、それぞれ染料濃度表示器および無機塩類濃度
表示器であり、精製中にある染料水溶液中の染料濃度値
および無a塩類濃度仙が表示される。従って、この装置
の操作者は製造中の染料水溶液の品質を容易に知見する
ことができる。
81 and 82 are a dye concentration range setting switch and an inorganic salt concentration range setting switch, respectively, and a signal corresponding to the J seismic intensity range determined by JJ is sent to the console input/output 42.
The signal is supplied to the controller via the 27 circuit 83. Reference numerals 84 and 85 are a dye concentration indicator and an inorganic salts concentration indicator, respectively, which display the dye concentration value and a salt-free concentration value in the aqueous dye solution being purified. Therefore, the operator of this apparatus can easily know the quality of the aqueous dye solution being produced.

スイッチ81および82による染料濃度範囲および無機
塩類濃度範囲の設定値はRAM 83内しこ一時記憶さ
れる。無機塩類濃度検出器46および染料濃度検出器4
7により検出された精製中にある染料水溶液の無機塩類
および染料の各検出濃度値は、制御器の比較部1311
において設定値と比較され、その比較結果に基づき、後
述のように循環ポンプ48′4の各負荷の駆動が制御さ
れる。
The values set for the dye concentration range and inorganic salt concentration range by switches 81 and 82 are temporarily stored in RAM 83. Inorganic salt concentration detector 46 and dye concentration detector 4
The detected concentration values of inorganic salts and dyes in the aqueous dye solution being purified by 7 are determined by the comparison unit 1311 of the controller.
is compared with a set value, and based on the comparison result, the drive of each load of the circulation pump 48'4 is controlled as described later.

第3図は第1図1こ示す装置の動作フローを示す。図に
おいて、手順5TI−9T4は調合槽24内の染料水溶
液を一定量に保持する手順である。すなわち手順STI
では、調合槽液量検出器2日の出力から、調合槽24内
の染料水溶液の液面高さが予め定められた設定範囲を規
定する低位置に対して1−1&こあるか否かを検出する
。その低位置よりも下の場合にはf、 llTl S 
T 2に進み、そうでない場合には手順ST3に進む。
FIG. 3 shows the operation flow of the apparatus shown in FIG. 1. In the figure, step 5TI-9T4 is a step for maintaining the dye aqueous solution in the mixing tank 24 at a constant amount. That is, the procedure STI
Now, from the output of the mixing tank liquid level detector on the 2nd day, it is determined whether the liquid level of the dye aqueous solution in the mixing tank 24 is 1-1 & higher than the low position that defines the predetermined setting range. To detect. If it is below that low position, f, llTl S
Proceed to T2, and if not, proceed to step ST3.

手111ft S T 2では、染料バルブ23および
純水バルブ25を開き、それぞれ所定量の染料粉末およ
び純水を調合槽28内に投入する。調合槽24において
は、撹拌機27が常時動作状態にあるので、投入された
染料粉末が純水に溶解されて、染料水溶静か調合される
。手順ST3では、液量検出器28の出力により、調合
槽24内の液面が設定範囲を規定する高位置よりも上か
否かを検出する。その高位1°ν1よりも」二の場合に
は手順ST4に進み、そうでない場合には手ll111
ST5に進む。手順ST4では、閉状ji、にある染料
バルブ23および純水バルブ25を閉して、染料粉末お
よび純水の供給を止める。
At hand 111ft ST 2, the dye valve 23 and pure water valve 25 are opened, and predetermined amounts of dye powder and pure water are respectively put into the mixing tank 28. In the mixing tank 24, since the stirrer 27 is always in operation, the dye powder introduced therein is dissolved in pure water and the dye is quietly mixed into water. In step ST3, it is detected based on the output of the liquid amount detector 28 whether or not the liquid level in the mixing tank 24 is above a high position that defines the setting range. If the position is higher than 1°ν1, proceed to step ST4, otherwise proceed to step ST4.
Proceed to ST5. In step ST4, the dye valve 23 and pure water valve 25 in the closed state ji are closed to stop the supply of dye powder and pure water.

r順ST5ては、染料a度検出器47により検出された
減塩槽42内の染料水溶液における染料濃度値を、表小
器84に表示する。手順ST6では、同じく無機m類濃
度検出器46により検出された無機塩類濃度値を表示器
85に表示する。
In step ST5, the dye concentration value in the aqueous dye solution in the salt reduction tank 42 detected by the dye a degree detector 47 is displayed on the table 84. In step ST6, the inorganic salt concentration value also detected by the inorganic class M concentration detector 46 is displayed on the display 85.

1″、mn S T 7では、検出器47により検出さ
れた染料濃度が、スイフチ81により設定された染料濃
度の範囲内にあるか否かを判定する。その;没定範囲内
にあると判定された場合には手順ST8に進み、そうで
ない場合には、手順ST9に進む。手順ST8では、検
出器46により検出された無機1ハ類の濃度が、スイッ
チ82により設定された値の範囲内にあるか否かを判定
する。その設定範囲内にあると判定された場合には手順
5TIOに進み、そうでない場合には手順ST9に進む
1'', mn ST 7 determines whether the dye concentration detected by the detector 47 is within the dye concentration range set by the swifter 81. It is determined that it is within the immersion range. If so, proceed to step ST8; otherwise, proceed to step ST9. In step ST8, the concentration of the inorganic class 1C detected by the detector 46 is within the range of the value set by the switch 82. If it is determined that it is within the set range, the process proceeds to step 5TIO, and if not, the process proceeds to step ST9.

手順ST9では、検出器50により検出された減塩槽4
2内の液面が設定範囲を規定する高位置よりも旧か否か
を判定する。その高位置より下の場合には、手順5T1
1へ進み、そうでない場合には手順5T12に進む。手
順5TIIでは、供給バルブ32および純水バルブ49
を開閉制御して、減塩槽42内へ染料水溶液および純水
を供給する。これによって、減塩槽42内の染料水溶液
における染料濃度を、」−述のようにスイッチ81によ
り設定された範囲内になるように調整する。この後、手
順5TI3へ進む。−・方、手順5T12では、供給バ
ルブ32および純水/ヘルプ49の閉動作を行う。
In step ST9, the salt-reducing tank 4 detected by the detector 50
It is determined whether the liquid level in 2 is older than the high position that defines the setting range. If it is below that high position, step 5T1
If not, proceed to step 5T12. In step 5TII, the supply valve 32 and the pure water valve 49
The aqueous dye solution and pure water are supplied into the salt reduction tank 42 by controlling opening and closing. As a result, the dye concentration in the aqueous dye solution in the salt reduction tank 42 is adjusted to fall within the range set by the switch 81 as described above. After this, proceed to step 5TI3. - On the other hand, in step 5T12, the supply valve 32 and the pure water/help 49 are closed.

f順5T13では、循環ポンプ48を作動させて、減I
へ4f11142内の染料水溶液を減塩フィルタ43を
介して循環させ、その染料水溶液から無機塩類の排除を
行う。
At f order 5T13, the circulation pump 48 is operated to reduce I.
The dye aqueous solution in 4f11142 is circulated through the salt-reducing filter 43 to remove inorganic salts from the dye aqueous solution.

」−述のように、染料濃度および無!!IIM類濤度が
設定範囲外の場合には、手順5TIIおよび手順5T1
3または1−順5T12および手順5T13を通るルー
チンを繰り返して、染料濃度および無機塩類濃度を設定
範囲内の値となす。画濃度が設定範囲内に納まった後は
、手順5TIOに進む。
”-as mentioned, dye concentration and no! ! If the IIM level is outside the setting range, step 5TII and step 5T1
3 or 1 - Repeat the routine through step 5T12 and step 5T13 to bring the dye concentration and inorganic salt concentration within the set range. After the image density falls within the set range, proceed to step 5TIO.

T=順5TIOでは、検出器50により検出された減塩
槽42内の液miが61ぐ定範囲を規定する低位置より
も1−か否かを判定する。その低位置よりも」−の場合
には、〔順5TI4へ進み、そうでない場合には手順5
T15へ進む。毛11[4ST14では、循環ポンプ4
8の作動を停止]二させ、貯蔵バルブ51の開動作を行
う。この結果、減Iム4P442内に得られた所定量の
精製染料水溶液が、16゛蔵槽52に供給される。
In the T=order 5TIO, it is determined whether the liquid mi in the salt reduction tank 42 detected by the detector 50 is 1- lower than the lower position defining the 61-regular range. If it is lower than that position, proceed to step 5TI4; otherwise, proceed to step 5TI4.
Proceed to T15. Hair 11 [In 4ST14, circulation pump 4
8] to open the storage valve 51. As a result, a predetermined amount of purified dye aqueous solution obtained in the reduced-Imum 4P442 is supplied to the 16° storage tank 52.

ト朧ST1’5では、貯蔵/ヘルプ51の閉動作および
供給ノヘルブ32.純水バルブ48の開動作を行い、貯
蔵槽52への供給を終了させると共に、減塩槽42内の
染料水溶液の量を増やし、その液面高さが設定範囲内と
なるようにする。
In Toboro ST1'5, the closing operation of the storage/help 51 and the supply help 32. The pure water valve 48 is opened to end the supply to the storage tank 52, and the amount of dye aqueous solution in the salt reduction tank 42 is increased so that the liquid level is within the set range.

この後、再び上述した手+1iT11,5T13または
手順5T12,5T13を通るルーチンを繰り返して、
減塩槽42内には、染料濃度および無機塩類濃度が設定
範囲内にある所定値の染料水溶液が得られる。この後は
、上述した手順5T14へ進む。
After this, repeat the routine that goes through the above-mentioned hand+1iT11, 5T13 or steps 5T12, 5T13 again,
In the salt reduction tank 42, an aqueous dye solution having a predetermined dye concentration and an inorganic salt concentration within a predetermined range is obtained. After this, the process proceeds to step 5T14 described above.

上述したように、本実施例においては、精製部41にお
いて、染料水溶液が一定量毎に精製される。
As described above, in this embodiment, the aqueous dye solution is purified in the purification section 41 in fixed amounts.

[効果] 以上説明したように本発明によれば、染料溶油を製造す
るにあたり、染料溶液中に含有される911町機塩類の
濃度検出を行い、その検出結果にノ、(つき染料の精製
、すなわち、無機塩類の濃度調整を行うようにしたので
、インクジェット記録用インクや筆記具用インク等の;
im製に好適な精製染料溶液を製造することができる。
[Effect] As explained above, according to the present invention, when producing a dye solution, the concentration of 911-choki salts contained in the dye solution is detected, and based on the detection result, That is, since the concentration of inorganic salts is adjusted, ink for inkjet recording, ink for writing instruments, etc.;
A purified dye solution suitable for im production can be produced.

更に、本発明によれば、かかる染料溶液を連続的に、し
かも自動的に%l j5mすることが可能となり、高品
賀インクの大量生lrにbf適である。
Further, according to the present invention, it is possible to continuously and automatically reduce the dye solution to %lj5m, making it suitable for large-scale production of high-quality ink.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明による装置の一実施例を示す概略構成図
、第2図は第1図に示す装置の制御部を示すブロック図
、第3図は第1図に示す装置の動作を示すフローチャー
トである。 21・・・染料供給部、 22・・・染料粉末、 23・・・染料バルブ、 24・・・調合槽、 25・・・純水バルブ、 26・・・純水供給パイプ、 27・・・調合槽撹拌機 28・・・調合槽液部:検出器、 29・・・ろ過フィルタ、 31・・・供給槽。 32・・・供給バルブ、 33・・・弁、 41・・・精製部、 42・・・減塩槽、 43・・・減塩フィルタ、 44・・・排塩槽、 45・・・減塩横撹拌機、 46・・・無機塩類濃度検出器、 47・・・染料濃度検出器、 48・・・循環ポンプ、 49・・・純水バルブ、 50・・・減塩槽液量検出器。 51・・・貯蔵バルブ、 52・・・貯蔵槽、 61・・・制御器、 62・・・リードオンリメモリ(ROM)、63・・・
ランタムアクセスメモリ(RAM) 。 64.65・・・A/D変換器、 68・・・入力4フファ回路。 67〜74・・・ドライブ回路、 75・・・出力バッファ回路、 81・・・染料濃度範囲設定スイッチ、82・・・無機
塩類濃度範囲設定スイ・ンチ、83・・・コンソール入
出力4227回路、84・・・染料濃度表示器、 85・・・無機塩類濃度表示器、 ell・・・比較部。
FIG. 1 is a schematic configuration diagram showing an embodiment of the device according to the present invention, FIG. 2 is a block diagram showing the control section of the device shown in FIG. 1, and FIG. 3 shows the operation of the device shown in FIG. 1. It is a flowchart. 21... Dye supply unit, 22... Dye powder, 23... Dye valve, 24... Mixing tank, 25... Pure water valve, 26... Pure water supply pipe, 27... Preparation tank agitator 28...Preparation tank liquid part: detector, 29...filtration filter, 31...supply tank. 32... Supply valve, 33... Valve, 41... Purification section, 42... Salt reduction tank, 43... Salt reduction filter, 44... Salt removal tank, 45... Salt reduction Horizontal stirrer, 46...Inorganic salt concentration detector, 47...Dye concentration detector, 48...Circulation pump, 49...Pure water valve, 50...Salt reduction tank liquid level detector. 51...Storage valve, 52...Storage tank, 61...Controller, 62...Read only memory (ROM), 63...
Random Access Memory (RAM). 64.65...A/D converter, 68...Input 4-fufa circuit. 67-74...Drive circuit, 75...Output buffer circuit, 81...Dye concentration range setting switch, 82...Inorganic salt concentration range setting switch, 83...Console input/output 4227 circuit, 84...Dye concentration indicator, 85...Inorganic salt concentration indicator, ell...Comparison section.

Claims (1)

【特許請求の範囲】[Claims] 染料溶液の製造手段と、前記溶液中の無!!i場類の濃
度検出手段と、この検出出力に基づいて前記塩類の濃度
を制御する無機塩類濃度制御手段とを具備したことを特
徴とする染料精製装置。
Means for producing a dye solution, and no residue in said solution! ! 1. A dye purification apparatus, comprising: a concentration detection means for the i-class concentration; and an inorganic salt concentration control means for controlling the concentration of the salts based on the detection output.
JP5529983A 1983-04-01 1983-04-01 Apparatus for purification of dye Pending JPS59182863A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5529983A JPS59182863A (en) 1983-04-01 1983-04-01 Apparatus for purification of dye

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5529983A JPS59182863A (en) 1983-04-01 1983-04-01 Apparatus for purification of dye

Publications (1)

Publication Number Publication Date
JPS59182863A true JPS59182863A (en) 1984-10-17

Family

ID=12994690

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5529983A Pending JPS59182863A (en) 1983-04-01 1983-04-01 Apparatus for purification of dye

Country Status (1)

Country Link
JP (1) JPS59182863A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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JPS5025626A (en) * 1973-03-12 1975-03-18
JPS5086532A (en) * 1973-11-30 1975-07-11
JPS5199695A (en) * 1975-01-23 1976-09-02 Aligena Ag
JPS52131978A (en) * 1976-04-28 1977-11-05 Daicel Chem Ind Ltd Circulating concentrator
JPS53115552A (en) * 1977-01-24 1978-10-09 Pure Cycle Corp Water recirculating system
JPS5488804A (en) * 1977-12-05 1979-07-14 Nefuchiyanoi Puromuishiyurenno Thermally mining and recovering method of oil and flowable bitumen
JPS54131340A (en) * 1978-03-31 1979-10-12 Mitsubishi Chem Ind Ltd Water treatment device
JPS5547505A (en) * 1978-09-27 1980-04-04 Mallory & Co Inc P R Method and apparatus for controlling liquid treatment equipment
JPS5548846A (en) * 1978-10-02 1980-04-08 Matsushita Electric Ind Co Ltd Automatic leading in reproducing unit for magnetic tape
JPS5648214A (en) * 1979-09-19 1981-05-01 Aligena Ag Membrane containing porous improved polyacrylonitril suitable for ultrafiltration* its manufacture and its use
JPS5653704A (en) * 1979-09-19 1981-05-13 Aligena Ag Ultrafiltration
SU842102A1 (en) * 1979-09-07 1981-06-30 Научно-Исследовательский И Проектныйинститут По Комплексной Автоматизациинефтяной И Химической Промышленности Method of control of oil emulsion desalinization
US4290812A (en) * 1979-07-27 1981-09-22 Olympia Werke Ag Process for the production of inks free of foreign salts
JPS56151768A (en) * 1980-04-01 1981-11-24 Ciba Geigy Ag Manufacture of solid composition of water-soluble dye
JPS56155264A (en) * 1980-05-06 1981-12-01 Canon Inc Recording liquid and production thereof
JPS5738859A (en) * 1980-06-04 1982-03-03 Ciba Geigy Ag Manufacture of concentrated liquid dye composition
JPS5781806A (en) * 1980-09-16 1982-05-22 Aligena Ag Semipermeable composite membrane containing denatured polyvinyl alcohol, its manufacture and its use
JPS57149360A (en) * 1981-03-06 1982-09-14 Ciba Geigy Ag Manufacture of concentrated aqueous composition of anionic dye
EP0061610A1 (en) * 1981-03-25 1982-10-06 Aligena Ag Semipermeable membranes from acrylonitrile-based polymers, process for their preparation and their use
JPS57174104A (en) * 1981-03-17 1982-10-26 Aligena Ag Semipermeable membrane containing modified polysulfones and its manufacture and use

Patent Citations (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3506126A (en) * 1968-05-03 1970-04-14 Milton Roy Co Closed recirculating hemodialysis system
JPS5025626A (en) * 1973-03-12 1975-03-18
JPS5086532A (en) * 1973-11-30 1975-07-11
JPS5199695A (en) * 1975-01-23 1976-09-02 Aligena Ag
JPS52131978A (en) * 1976-04-28 1977-11-05 Daicel Chem Ind Ltd Circulating concentrator
JPS53115552A (en) * 1977-01-24 1978-10-09 Pure Cycle Corp Water recirculating system
JPS5488804A (en) * 1977-12-05 1979-07-14 Nefuchiyanoi Puromuishiyurenno Thermally mining and recovering method of oil and flowable bitumen
JPS54131340A (en) * 1978-03-31 1979-10-12 Mitsubishi Chem Ind Ltd Water treatment device
JPS5547505A (en) * 1978-09-27 1980-04-04 Mallory & Co Inc P R Method and apparatus for controlling liquid treatment equipment
JPS5548846A (en) * 1978-10-02 1980-04-08 Matsushita Electric Ind Co Ltd Automatic leading in reproducing unit for magnetic tape
US4290812A (en) * 1979-07-27 1981-09-22 Olympia Werke Ag Process for the production of inks free of foreign salts
SU842102A1 (en) * 1979-09-07 1981-06-30 Научно-Исследовательский И Проектныйинститут По Комплексной Автоматизациинефтяной И Химической Промышленности Method of control of oil emulsion desalinization
JPS5648214A (en) * 1979-09-19 1981-05-01 Aligena Ag Membrane containing porous improved polyacrylonitril suitable for ultrafiltration* its manufacture and its use
JPS5653704A (en) * 1979-09-19 1981-05-13 Aligena Ag Ultrafiltration
JPS56151768A (en) * 1980-04-01 1981-11-24 Ciba Geigy Ag Manufacture of solid composition of water-soluble dye
JPS56155264A (en) * 1980-05-06 1981-12-01 Canon Inc Recording liquid and production thereof
JPS5738859A (en) * 1980-06-04 1982-03-03 Ciba Geigy Ag Manufacture of concentrated liquid dye composition
JPS5781806A (en) * 1980-09-16 1982-05-22 Aligena Ag Semipermeable composite membrane containing denatured polyvinyl alcohol, its manufacture and its use
JPS57149360A (en) * 1981-03-06 1982-09-14 Ciba Geigy Ag Manufacture of concentrated aqueous composition of anionic dye
JPS57174104A (en) * 1981-03-17 1982-10-26 Aligena Ag Semipermeable membrane containing modified polysulfones and its manufacture and use
EP0061610A1 (en) * 1981-03-25 1982-10-06 Aligena Ag Semipermeable membranes from acrylonitrile-based polymers, process for their preparation and their use

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