JPH11262601A - Method for preparing and defoaming coating liquid - Google Patents

Method for preparing and defoaming coating liquid

Info

Publication number
JPH11262601A
JPH11262601A JP6564198A JP6564198A JPH11262601A JP H11262601 A JPH11262601 A JP H11262601A JP 6564198 A JP6564198 A JP 6564198A JP 6564198 A JP6564198 A JP 6564198A JP H11262601 A JPH11262601 A JP H11262601A
Authority
JP
Japan
Prior art keywords
liquid
defoaming
coating
mixing
dissolving
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.)
Granted
Application number
JP6564198A
Other languages
Japanese (ja)
Other versions
JP3658982B2 (en
Inventor
Nobutaka Ueno
修敬 上野
Yasuo Nishi
泰男 西
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.)
Konica Minolta Inc
Original Assignee
Konica Minolta 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 Konica Minolta Inc filed Critical Konica Minolta Inc
Priority to JP06564198A priority Critical patent/JP3658982B2/en
Publication of JPH11262601A publication Critical patent/JPH11262601A/en
Application granted granted Critical
Publication of JP3658982B2 publication Critical patent/JP3658982B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Degasification And Air Bubble Elimination (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)

Abstract

PROBLEM TO BE SOLVED: To enable coating application at a high speed while suppressing the foaming during the coating application of a coating liquid of a high viscosity and large flow rate by dissolving plural coating constitution liquids, then mixing these liquids to prepare a coating liquid and deaerating the liquid and subsequently subjecting the liquid to primary defoaming and secondary defoaming. SOLUTION: The plural constitution liquids constituting the coating liquid, for example, emulsion liquid, gelatin liquid, coupler, etc., are respectively stirred and dissolved in a prescribed amt. each by a stirring machine 11 in respective dissolving kettles 10 and thereafter, the mixture is fed into a mixing kettle 20 and while the mixture is dearated by the effect of a pressure reducing device 22, the mixture is stirred and mixed. Next, the liquid mixture is fed into, for example, a centrifugal separator 30 as the primary defoaming process by a pump 32, by which large-diameter foam is removed. After the liquid is once stored into a primary storage buffer 34, the liquid mixture is fed under pressurization to an ultrasonic defoaming device 40 as the secondary defoaming by a pump 43. The pressurized liquid is irradiated with ultrasonic waves, by which the small-diameter bubbles are dissolved. The annihilation of the foam is checked by a foam detector 50 through a pressure gauge 43, a pressurizing valve 44 and a flow meter 45 and thereafter, the liquid is sent to a coating applicator.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、支持体に塗布して
写真感光材料や感熱紙や磁気材料等を製造する際に用い
る塗布液を調整脱泡する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for preparing and defoaming a coating solution used for producing a photographic light-sensitive material, a heat-sensitive paper, a magnetic material and the like by coating the film on a support.

【0002】[0002]

【従来の技術】従来の塗布液中の泡をとる脱泡方法とし
ては、第一に超音波照射特に加圧した塗布液に超音波照
射する方法があった。これは泡をトラップする効果と泡
を溶解する効果の2つの脱泡効果を持ち、このうち泡溶
解効果が小さな泡まで完全に脱泡する効果を発揮するた
め写真感光材料に使われてきた。一方本方式は処理能力
に限界があり、特開平3−157103号では粘度30
cpで流量9リットル/分、粘度90cpで流量3リッ
トル/分、また、特開平8−318102号では流量5
リットル/分、また、特開平3−157103号では粘
度80cp等の実施例の記載があり粘度100cp、流
量3リットル/分程度が一般的な能力限界点である。更
に本方式は特に多量の泡が持ち込まれたとき超音波自体
が弱められる特徴がある。
2. Description of the Related Art As a conventional defoaming method for removing bubbles in a coating solution, there has been a method of first irradiating an ultrasonic wave, particularly a method of irradiating a pressurized coating solution with an ultrasonic wave. It has two defoaming effects, a bubble trapping effect and a bubble dissolving effect. Of these, the bubble dissolving effect has been used for photographic light-sensitive materials because it exhibits the effect of completely defoaming even small bubbles. On the other hand, this method has a limitation in processing capacity, and Japanese Patent Application Laid-Open No.
cp at a flow rate of 9 liters / minute, viscosity of 90 cp at a flow rate of 3 liters / minute, and JP-A-8-318102 discloses a flow rate of 5 liters / minute.
Examples of liters / minute, JP-A-3-157103, and a viscosity of 80 cp are described. A typical capacity limit point is a viscosity of 100 cp and a flow rate of about 3 liter / minute. Further, this method has a feature that the ultrasonic wave itself is weakened particularly when a large amount of bubbles are brought in.

【0003】第二に塗布液に対して遠心力を掛けて泡を
追い出したり、塗布液を薄膜状に流延しながら泡を上方
に追い出す方法等がある。このような方法は、実公平3
−8322号では10〜50p、特公昭60−3847
号では10000p,10リットル/分で98.5%除
去、特開昭58−101708では15000p,10
リットル/分で85%除去等の実施例の記載があり、1
0〜15000pの高粘度液に用いられ処理速度は10
リットル/分程度で完全な脱泡はしないのが一般的であ
る。本方式群は泡の多少に関係が無く能力が一定なもの
である。即ち、能力は分離できる泡の大きさで限定さ
れ、小さな泡の分離は原理上不利で理論上無限小の泡は
分離できないという欠点がある。
[0003] Second, there is a method in which centrifugal force is applied to a coating solution to expel bubbles, or a method in which foam is expelled upward while casting a coating solution in a thin film form. Such a method is actually fair 3
-8322 No. 10-50p, Japanese Patent Publication No. 60-3847
No. 10000p, 98.5% removal at 10 liters / minute, JP-A-58-101708 discloses 15,000p, 10
Examples such as 85% removal at liter / minute are described.
It is used for high viscosity liquid of 0-15000p and the processing speed is 10
Generally, complete degassing is not performed at about 1 liter / minute. This system group has a constant capacity regardless of the foam size. In other words, the capacity is limited by the size of bubbles that can be separated, and there is a disadvantage that separation of small bubbles is disadvantageous in principle, and theoretically infinitely small bubbles cannot be separated.

【0004】また、塗布中に塗布液中の溶存空気が泡と
なって出る発泡現象が存在し、これを抑制する方法とし
て塗布以前に減圧による脱気あるいは、液温降下による
溶存空気不飽和化を行うことが知られている。
[0004] In addition, there is a foaming phenomenon in which dissolved air in a coating solution is formed as bubbles during coating. As a method for suppressing this, deaeration by decompression or dissolved air desaturation by a drop in liquid temperature before coating is performed. It is known to do.

【0005】[0005]

【発明が解決しようとする課題】支持体に対する塗布で
は、特に感光材料を製造する塗布においては、塗布液中
の微小な泡でも不良故障の原因になり、塗布液は完全に
脱泡されなければならない。
In the application to a support, especially in the production of a photosensitive material, even a minute bubble in the application liquid may cause a failure and the coating liquid must be completely defoamed. No.

【0006】一方、塗布液は生産性の点より濃縮高粘度
化され大流量での高速塗布がなされる傾向にあり、これ
は脱泡には益々厳しい条件となる。
On the other hand, coating solutions tend to be concentrated and have high viscosity from the viewpoint of productivity, so that high-speed coating at a large flow rate tends to be performed, which is an increasingly severe condition for defoaming.

【0007】従来の方法では、塗布液の粘度と流速の増
大による処理時間減少、処理効果減少があり、つまり負
荷が大きくなりすぎ脱泡が不能となるか、巨大な装置を
用意することになり好ましくない。
In the conventional method, there is a reduction in processing time and a reduction in processing effect due to an increase in the viscosity and flow rate of the coating liquid. That is, the load becomes too large to be able to remove bubbles, or a huge apparatus is prepared. Not preferred.

【0008】特に脱泡能力不足はカーテン塗布方法のよ
うな高粘度大流量高速塗布の可能な塗布方法において、
塗布液供給能力から本来の塗布能力を制限することにな
り改善する産業上の効果が大きい。さらにカーテン塗布
法においては薄く引き延ばされた塗布液の流下流延膜で
あるカーテン膜を形成するため、このカーテン膜への泡
の流入や混入はカーテン膜を破壊してしまうという大ト
ラブルを引き起こす場合があり、脱泡に対する要求度が
高い。
[0008] In particular, the lack of defoaming ability is caused by a coating method capable of high-viscosity, large-flow, high-speed coating such as a curtain coating method.
The original application ability is limited from the application liquid supply ability, and the industrial effect to improve is large. Furthermore, in the curtain coating method, since a curtain film is formed, which is a downstream film of the coating solution that has been thinly stretched, the inflow or mixing of bubbles into the curtain film causes a major trouble that the curtain film is destroyed. May cause, high demand for defoaming.

【0009】本発明は、このような問題点を解決し、高
粘度大流量高速塗布にも対応できて脱泡可能であり、且
つ、塗布中の発泡現象を抑制しつつ塗布液の溶解調整混
合を可能にした塗布液調整脱泡方法を確立することを課
題目的にする。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems, is capable of coping with high-viscosity, large-flow, high-speed coating, is capable of defoaming, and dissolves, adjusts and mixes a coating solution while suppressing foaming during coating. It is an object of the present invention to establish a coating solution adjusting and defoaming method which enables the above.

【0010】[0010]

【課題を解決するための手段】この目的は、「(1)
複数の塗布液構成液を溶解する溶解プロセスと、続いて
それらを混合し塗布液に調整する混合プロセスと、液の
脱気プロセスと、前記混合した液の大径泡を分離除去す
る一次脱泡プロセスと、一次脱泡後の液を加圧した加圧
液に超音波を照射し小径泡を溶解する二次脱泡プロセス
とを持つ塗布液調整脱泡方法であって、前記二次脱泡プ
ロセスが前記混合プロセス以降より下流にあり、前記一
次脱泡プロセスと前記脱気プロセスが前記溶解プロセス
と前記混合プロセス間又は該混合プロセス中又は該混合
プロセスと前記二次脱泡プロセス間の何れかにあり、前
記一次脱泡プロセスと前記脱気プロセスはそれぞれ1つ
以上含まれることを特徴とする塗布液調整脱泡方法。」
により達成される。ただし前記一次脱泡プロセスと前記
脱気プロセスは同時に行ってもかまわない。
The object of the present invention is to achieve the object of "(1)
A dissolving process for dissolving a plurality of coating liquid constituent liquids, followed by a mixing process for mixing and adjusting them into a coating liquid, a degassing process for the liquid, and a primary defoaming for separating and removing large-diameter bubbles of the mixed liquid. A coating liquid adjustment defoaming method having a process and a secondary defoaming process of irradiating ultrasonic waves to a pressurized liquid obtained by pressurizing the liquid after the primary defoaming to dissolve small-diameter bubbles, wherein the secondary defoaming is performed. A process is downstream from the mixing process onward, wherein the primary degassing process and the degassing process are either between the dissolving process and the mixing process or during the mixing process or between the mixing process and the secondary defoaming process. Wherein the primary defoaming process and the degassing process each include one or more processes. "
Is achieved by However, the primary deaeration process and the deaeration process may be performed simultaneously.

【0011】更に、「(2) 複数の塗布液構成液を溶
解する溶解プロセスと、続いてそれらを混合し塗布液に
調整する混合プロセスと、液の脱気プロセスと、前記混
合した液の大径泡を分離除去する一次脱泡プロセスと、
一次脱泡後の液を加圧した加圧液に超音波を照射し小径
泡を溶解する二次脱泡プロセスとを持つ塗布液調整脱泡
方法であって、前記構成液を溶解後、薄膜流延減圧装置
にそれぞれ又は同時に通液して、前記脱気プロセスと前
記一次脱泡プロセスとを行わせた後、前記混合プロセス
を経て前記二次脱泡プロセスを行うことを特徴とする塗
布液調整脱泡方法。
Further, "(2) a dissolving process for dissolving a plurality of coating liquid constituent solutions, a mixing process for mixing them to prepare a coating liquid, a degassing process for the liquid, A primary defoaming process that separates and removes diameter bubbles,
A coating liquid adjustment defoaming method having a secondary defoaming process of irradiating ultrasonic waves to a pressurized liquid obtained by pressurizing the liquid after the primary defoaming and dissolving the small-diameter bubbles, wherein after dissolving the constituent liquid, a thin film The coating solution, wherein the coating solution is passed through the casting depressurization device individually or simultaneously to perform the degassing process and the primary defoaming process, and then perform the secondary defoaming process through the mixing process. Adjust defoaming method.

【0012】あるいは、(3) 複数の塗布液構成液を
溶解する溶解プロセスと、続いてそれらを混合し塗布液
に調整する混合プロセスと、液の脱気プロセスと、前記
混合した液の大径泡を分離除去する一次脱泡プロセス
と、一次脱泡後の液を加圧した加圧液に超音波を照射し
小径泡を溶解する二次脱泡プロセスとを持つ塗布液調整
脱泡方法であって、前記構成液を溶解プロセスを経て、
減圧下の混合釜に流下添加させて前記脱気プロセスと前
記混合プロセスを行わせた後、遠心分離装置又は薄膜流
延減圧処理装置で構成される前記一次脱泡プロセスを経
て前記二次脱泡プロセスを行わせることを特徴とする塗
布液調整脱泡方法。
Alternatively, (3) a dissolving process of dissolving a plurality of coating liquid constituent liquids, a mixing process of mixing them to prepare a coating liquid, a degassing process of the liquid, and a large diameter of the mixed liquid A coating liquid preparation and defoaming method that has a primary defoaming process to separate and remove bubbles and a secondary defoaming process to irradiate ultrasonic waves to the pressurized liquid pressurizing the liquid after the primary defoaming to dissolve small-diameter bubbles A, through the dissolution process of the constituent liquid,
After having been subjected to the deaeration process and the mixing process by being added to a mixing vessel under reduced pressure, the secondary deaeration is performed through the primary deaeration process including a centrifugal separator or a thin film casting and decompression treatment device. A coating solution adjustment defoaming method characterized by performing a process.

【0013】あるいは、(4) 複数の塗布液構成液を
溶解する溶解プロセスと、続いてそれらを混合し塗布液
に調整する混合プロセスと、液の脱気プロセスと、前記
混合した液の大径泡を分離除去する一次脱泡プロセス
と、一次脱泡後の液を加圧した加圧液に超音波を照射し
小径泡を溶解する二次脱泡プロセスとを持つ塗布液調整
脱泡方法であって、前記溶解プロセスと前記混合プロセ
スとを経て薄膜流延減圧処理装置で連続的に前記脱気プ
ロセスと前記一次脱泡プロセスを行わせ、その後で前記
二次脱泡プロセスを行わせることを特徴とする塗布液調
整脱泡方法。」が特に効果的な方法であり、更に、
「(5) 前記二次脱泡プロセス以降コーターまでの間
で液温を低下させるようにしたことを特徴とする(1)
〜(4)項の何れか1項に記載の塗布液調整脱泡方
法。」により、より安定な脱泡効果を得る。
[0013] Alternatively, (4) a dissolving process for dissolving a plurality of coating liquid constituent liquids, a mixing process for mixing them to prepare a coating liquid, a degassing process for the liquid, and a large diameter of the mixed liquid. A coating liquid preparation and defoaming method that has a primary defoaming process to separate and remove bubbles and a secondary defoaming process to irradiate ultrasonic waves to the pressurized liquid pressurizing the liquid after the primary defoaming to dissolve small-diameter bubbles Then, the deaeration process and the primary defoaming process are continuously performed in the thin film casting decompression treatment device through the dissolving process and the mixing process, and then the secondary defoaming process is performed. Characteristic coating solution defoaming method. Is a particularly effective method.
"(5) The liquid temperature is lowered between the secondary defoaming process and the coater (1).
(4) The method for preparing and defoaming a coating solution according to any one of (4) to (4). ", A more stable defoaming effect is obtained.

【0014】また、「(6) 前記塗布液は写真感光材
料用の塗布液であることを特徴とする(1)〜(5)項
の何れか1項に記載の塗布液調整脱泡方法。」で産業上
の利益が大きく、中でも、「(7) 前記塗布液がカー
テン塗布コーターで塗布されることを特徴とする(1)
〜(6)項の何れか1項に記載の塗布液調整脱泡方
法。」の場合が非常に有効である。
Further, "(6) The method for adjusting and defoaming a coating solution according to any one of the above (1) to (5), wherein the coating solution is a coating solution for a photographic light-sensitive material. And (3) the coating liquid is applied by a curtain coating coater (1).
The method for adjusting and defoaming a coating liquid according to any one of items (1) to (6). Is very effective.

【0015】[0015]

【発明の実施の形態】本発明者等は先ず泡の消滅のメカ
ニズムついて検討を続けて次のような知見を得た。即
ち、本明細書における脱泡とは、狭義としては液中の気
泡を分離除去あるいは溶解消滅させることをいい、広義
としては前記狭義のものに加え一旦液中に溶けた空気等
の気体が、使用段階において再び気泡となって出現する
現象を防止する操作も含む。狭義の脱泡は、前述の泡を
除去するか泡を溶解消滅させることの何れか一方又は両
方を行うことにより達成される。何れの処理において
も、液粘度の増大や液流速増大は、気泡を流出させる力
を増大させることになり、補足力も不足し、処理時間も
減少するので単純に負荷増となる。
BEST MODE FOR CARRYING OUT THE INVENTION The present inventors first studied the mechanism of disappearance of bubbles and obtained the following findings. That is, defoaming in the present specification, in a narrow sense, refers to separating and removing or dissolving bubbles in a liquid, and in a broad sense, gas such as air once dissolved in a liquid in addition to the narrow one, It also includes an operation of preventing a phenomenon that appears as bubbles again in the use stage. Degassing in a narrow sense is achieved by removing one of the aforementioned bubbles or dissolving and eliminating the bubbles. In any of the processes, an increase in the liquid viscosity or an increase in the liquid flow velocity increases the force for flowing out bubbles, the supplementary power is insufficient, and the processing time is reduced, so that the load simply increases.

【0016】上記のように脱泡には2種類のプロセスが
あるが何れか一方を選んだり、2プロセスを同時に行っ
たり、溶解消滅プロセス後に分離除去プロセスを行った
りしても、単なる組み合わせであり、大きな脱泡効果は
得られない。そのプロセスを大きな泡のみを分離除去
し、その後、分離除去できなかった小さな泡のみを溶解
消滅させるようにした場合のみ極めて効果的であること
を見いだした。
As described above, there are two types of processes for defoaming. However, even if either one is selected, two processes are performed at the same time, or the separation and removal process is performed after the dissolution and disappearance process, it is only a combination. A large defoaming effect cannot be obtained. It has been found that the process is extremely effective only when only large bubbles are separated and removed, and then only small bubbles that cannot be removed are dissolved and eliminated.

【0017】上記効果は、従来の2プロセスを同時に平
行して行う方法では得られない。なぜならば、泡溶解消
滅プロセスにおいては、消滅させ得ない大きな泡が無い
ことが重要であるからであり、特に泡の溶解消滅プロセ
スに、超音波照射に加えて液加圧を行わせる方式を取る
場合、第一に小さい泡のみで泡が破裂粉砕され速効性の
高い脱泡が行われることを新たに発見した。また、第二
に持ち込まれる泡の量が多く、特にその泡が大きいまま
のとき、超音波自体の強さが大きく減衰する特徴をもつ
ことが分かった。つまり、泡の溶解消滅のプロセスに超
音波液加圧方法を取る場合、小さな泡のみと大きな泡も
あるのとでは、両者には非常に顕著な差が現れ、前者は
飛躍的な大能力を発揮することを見いだした。尚、超音
波照射に加えて液加圧を行わせると図1のグラフにも示
すように泡消滅に有効な小さい泡の大きさの範囲が拡大
され、泡消滅効果がより効果的になる。
The above-mentioned effects cannot be obtained by the conventional method in which two processes are simultaneously performed in parallel. This is because it is important that there is no large bubble that cannot be eliminated in the foam dissolving and disappearing process. In particular, in the dissolving and disappearing process of the foam, a method of applying liquid pressure in addition to ultrasonic irradiation is adopted. In this case, it was newly discovered that the bubbles were burst and crushed with only the small bubbles, and that the defoaming with high efficiency was performed. Secondly, it was found that the amount of bubbles brought in was large, and particularly when the bubbles remained large, the strength of the ultrasonic wave itself was greatly attenuated. In other words, when the ultrasonic liquid pressurization method is used in the process of dissolving and disappearing bubbles, there is a very remarkable difference between the small bubbles and the large bubbles, and the former has a remarkable large capacity. I found it to work. In addition, when the liquid pressure is applied in addition to the ultrasonic irradiation, as shown in the graph of FIG. 1, the range of the size of the small bubble effective for the bubble disappearance is expanded, and the bubble disappearance effect becomes more effective.

【0018】一方で被脱泡液を使用する時まで脱泡され
た状態で安定に保つ為には、上記に加え、脱気プロセス
を追加したものが好ましく、高粘度で大流量の液体を高
効率に且つ強力に脱泡し、更に高い安定性を得るには、
大きな泡を分離除去して、その後、取り残した小さな泡
のみを超音波加圧方式にて溶解消滅させて、更に脱気プ
ロセスが加わった一連の脱泡プロセスが不可欠であると
の結論に達した。以上が本発明の第一のグループの発明
である。
On the other hand, in order to stably maintain the defoamed state until the time when the liquid to be defoamed is used, it is preferable to add a deaeration process in addition to the above. In order to efficiently and strongly deaerate and obtain even higher stability,
Large bubbles were separated and removed, and only the small bubbles left behind were dissolved and annihilated by an ultrasonic pressure method, and it was concluded that a series of degassing processes with an additional degassing process was essential. . The above is the invention of the first group of the present invention.

【0019】これを満足し、且つ、写真感光材料のよう
に長時間、連続的に液を調整しながら塗布を行う場合、
調整における溶解プロセス、混合プロセスの2つのプロ
セスが脱泡とは無関係に別途必要である。
In the case where the above is satisfied and the coating is performed while adjusting the solution continuously for a long time like a photographic light-sensitive material,
Two processes, a dissolving process and a mixing process, are separately required in preparation, irrespective of defoaming.

【0020】ここに至り、前述の脱泡に関する3つのプ
ロセスと合わせ合計5つのプロセスを処理することが必
要となるが、単に連続的に1つずつ処理したのでは、長
々としたスペースと高コストで運用しにくい生産方法と
なってしまう。ここで前述の第一のグループの発明に加
え、目的の効果を得る最低限のルールと各プロセスの装
置特性を考慮して効果的組み合わせを検討した結果を第
二のグループの発明として付加し、少なくとも上記5プ
ロセスを実施する際の効果的な構成及びルールを前項で
述べたように7つの手段として提供した。
At this point, it is necessary to process a total of five processes in addition to the three processes relating to the defoaming described above. It becomes a production method that is difficult to operate at cost. Here, in addition to the above-described first group invention, a result of studying an effective combination in consideration of a minimum rule for obtaining an intended effect and an apparatus characteristic of each process is added as a second group invention, Effective configurations and rules for implementing at least the above five processes are provided as seven means as described in the preceding section.

【0021】具体的には、図2〜図5の各概略構成図に
示すようになる。先ず図2に示す構成について説明す
る。例えば塗布される塗布液を構成する複数の構成液例
えば乳剤液、ゼラチン液、カプラー等は、それぞれ各溶
解釜10で所定量ずつ攪拌機11で攪拌溶解され溶解プ
ロセスを終わり、次の混合釜20に進み減圧装置22に
接続されたタンク21中で脱気されながら攪拌機23で
攪拌され、混合プロセスを終えポンプ32で一次脱泡プ
ロセスとしての例えば遠心分離装置30に送り込まれ大
径泡が脱泡されて一時貯留バッファー34に溜められポ
ンプ42で圧送され二次脱泡プロセスとしての超音波脱
泡装置40に入り、超音波を照射され、圧力計43、加
圧弁44、流量計45を経て泡検出器50でその泡の消
滅を確認されたうえで塗布装置のコーターに送液され
る。
More specifically, the configuration is as shown in FIGS. First, the configuration shown in FIG. 2 will be described. For example, a plurality of constituent liquids constituting the coating liquid to be coated, for example, an emulsion liquid, a gelatin liquid, a coupler, and the like, are stirred and dissolved by a predetermined amount in each dissolving vessel 10 by a stirrer 11 to complete the dissolving process. The mixture is stirred by the stirrer 23 while being degassed in the tank 21 connected to the decompression device 22, and the mixing process is completed. The mixture is sent to the centrifugal separator 30 as a primary defoaming process by the pump 32 to remove large-diameter bubbles. And stored in a temporary storage buffer 34 and pressure-fed by a pump 42 to enter an ultrasonic defoaming device 40 as a secondary defoaming process, irradiated with ultrasonic waves, and detected through a pressure gauge 43, a pressure valve 44 and a flow meter 45 to detect bubbles. After the disappearance of the foam is confirmed by the vessel 50, the foam is sent to the coater of the coating apparatus.

【0022】ここで、二次脱泡プロセスは混合プロセス
以降にある。そして一次脱泡プロセスと脱気プロセスが
混合プロセスと二次脱泡プロセスの間にあるが、これは
混合プロセス中で行っても良く、図3の概略構成図に示
すように溶解釜10を持つ溶解プロセスと混合釜20を
持つ混合プロセスとの間に位置させても良い。このよう
に一次脱泡プロセスと脱気プロセスはそれぞれ1つ以上
が含まれている大径泡及び後工程(塗布工程)での発泡
要素が排除される。
Here, the secondary defoaming process is after the mixing process. The primary deaeration process and the deaeration process are between the mixing process and the secondary deaeration process, but this may be performed during the mixing process, and the dissolving vessel 10 is provided as shown in the schematic configuration diagram of FIG. It may be located between the melting process and the mixing process having the mixing tank 20. As described above, the primary defoaming process and the deaeration process eliminate a large-diameter foam containing one or more bubbles and a foaming element in a subsequent step (coating step).

【0023】図3の概略構成図に示すものは、前述の通
りであるが、更に溶解釜10を持つ溶解プロセスと混合
釜20を持つ混合プロセスとの間に位置させた脱気と一
次脱泡のプロセス35は薄膜流延減圧方式のものを用い
ていて脱気、脱泡ともに効率良く行われている。しか
し、これに限ることなく遠心分離脱泡方式のものを用い
ても良い。
FIG. 3 schematically shows the structure as described above, but furthermore, degassing and primary defoaming located between the dissolving process having the dissolving pot 10 and the mixing process having the mixing pot 20. The process 35 uses a thin film casting depressurization method, and both degassing and degassing are efficiently performed. However, the present invention is not limited thereto, and a centrifugal degassing type may be used.

【0024】図4の概略構成図に示すものは、各構成液
を溶解釜10で溶解後、混合釜20に減圧下で流下添加
させながら脱気して混合のプロセスを行う。その後で薄
膜流延減圧装置30Bに送液し、一次脱泡プロセスを行
い更に貯留バッファー34を経てポンプ42で超音波脱
泡装置40に送液され、二次脱泡プロセスが行われる。
The components shown in the schematic constitutional diagram of FIG. 4 are prepared by dissolving each constituent liquid in a dissolving vessel 10 and then degassing while adding the mixture to a mixing vessel 20 under reduced pressure to perform a mixing process. Thereafter, the liquid is sent to the thin film casting and depressurizing device 30B, the primary defoaming process is performed, and the liquid is sent to the ultrasonic defoaming device 40 by the pump 42 via the storage buffer 34, and the secondary defoaming process is performed.

【0025】上記一次処理の脱泡装置としては前記薄膜
流延減圧装置30Bの代わりに遠心分離方式のものを用
いることができ、同様な効果が確認できた。尚、前記混
合釜20での減圧装置による脱気は前記一次脱泡処理の
前段として泡の発生減少に役立っているとともに塗布工
程における発泡を皆無にすることに貢献する。
As the defoaming device for the primary treatment, a centrifugal separator can be used in place of the thin film casting and depressurizing device 30B, and the same effect can be confirmed. The deaeration by the decompression device in the mixing vessel 20 is useful for reducing the generation of bubbles as a pre-stage of the primary defoaming treatment and contributes to eliminating foaming in the coating process.

【0026】図5の概略構成図に示すものは、各構成液
を溶解釜10で溶解後、混合釜20に送液し減圧下で混
合のプロセスを行う。その後で薄膜流延減圧装置30B
に送液し、そこで脱気のプロセスと一次脱泡プロセスを
行い、更に貯留バッファー34を経てポンプ42で超音
波脱泡装置40に送液され、二次脱泡プロセスが行われ
るようにしてある。
In the apparatus shown in the schematic constitutional view of FIG. 5, each constituent liquid is dissolved in a dissolving vessel 10 and then sent to a mixing vessel 20 to perform a mixing process under reduced pressure. After that, the thin film casting decompression device 30B
, Where the degassing process and the primary defoaming process are performed, and further, the liquid is sent to the ultrasonic defoaming device 40 by the pump 42 via the storage buffer 34 to perform the secondary defoaming process. .

【0027】更に、塗布時における発泡抑制効果は、前
述の脱気プロセスに加えて、二次脱泡プロセスを終了し
て塗布機のコーターに送液された間に液温が低下してい
る状態とするプロセスを付与することにより一層増進さ
れる。
Further, the effect of suppressing foaming during coating is as follows. In addition to the above-described degassing process, the liquid temperature is reduced while the secondary defoaming process is completed and the liquid is sent to the coater of the coating machine. The process can be further enhanced by providing a process.

【0028】この塗布液調整脱泡方法は写真感光材料製
造時に、その中でも特にカーテンコーター塗布装置を用
いて高粘度高濃度大流量の塗布液を高速で塗布する写真
感光材料製造時に大きな効果をあげることが分かった。
This coating solution adjusting and defoaming method has a great effect in the production of a photographic light-sensitive material, especially in the production of a photographic light-sensitive material in which a high-viscosity, high-concentration, large-flow-rate coating liquid is applied at a high speed using a curtain coater coating apparatus. I understood that.

【0029】尚、脱泡能力としては、従来に比べ、粘度
において10倍、流量において17倍の能力を発揮する
ことが分かった。
The defoaming ability was found to be 10 times higher in viscosity and 17 times higher in flow rate than in the past.

【0030】実施の形態の一例としてのテスト結果を実
施例1として下記する。
Test results as an example of the embodiment will be described below as a first embodiment.

【0031】実施例1 被脱泡液:写真感光乳剤塗布液(3液と増粘剤の添加混
合) ここで3液とはIIR済み乳剤とカプラー分散液とゼラチ
ン水溶液とであり、増粘剤は増粘多糖類のものを用い
た。混合後の液の表面張力は30dyne/cm2であ
り、粘度はB型粘度計で測定し、またゼラチン濃度は1
0%である。
Example 1 Defoaming solution: Photosensitive emulsion coating solution (addition and mixing of 3 solutions and thickener) Here, 3 solutions are an IIR-completed emulsion, a coupler dispersion and an aqueous gelatin solution. Used thickening polysaccharides. The surface tension of the liquid after mixing was 30 dyne / cm 2 , the viscosity was measured with a B-type viscometer, and the gelatin concentration was 1
0%.

【0032】泡検出:泡検出器で行う。Foam detection: Performed with a foam detector.

【0033】脱泡装置:1)従来方法 4液を溶解後混合し、減圧脱気は30分バッチ式で行
い、更に超音波脱泡装置(25kHz,2kW,容量5
リットル,液加圧3kg/cm2)で脱泡を行う。
Defoaming apparatus: 1) Conventional method Four liquids are dissolved and mixed, and deaeration under reduced pressure is performed by a batch method for 30 minutes. Further, an ultrasonic defoaming apparatus (25 kHz, 2 kW, capacity 5)
Degassing is performed with a pressure of 3 kg / cm 2 liter.

【0034】2)本発明の方式1 4液を溶解後混合し、減圧脱気は30分バッチ式で行
い、更に遠心分離機(800rpm,容量7リットル)
で一次脱泡を行い、超音波脱泡装置(25kHz,2k
W,容量1.5リットル,液加圧3kg/cm2)で二
次脱泡を行う。
2) Method 14 of the present invention Dissolve and mix the four liquids, perform degassing under reduced pressure in a batch system for 30 minutes, and further centrifuge (800 rpm, capacity 7 liters).
Primary defoaming with an ultrasonic defoaming device (25 kHz, 2 k
W, volume 1.5 liter, liquid pressurization 3 kg / cm 2 ) to perform secondary defoaming.

【0035】3)本発明の方式2 4液を溶解後、減圧薄膜脱泡機(容量20リットル)で
一次脱泡と3液の脱気を行い、添加剤を液中混合し、更
に超音波脱泡装置(25kHz,2kW,容量1.5リ
ットル,液加圧3kg/cm2)で二次脱泡を行う。
3) Method 24 of the present invention After dissolving the four liquids, the primary defoaming and deaeration of the three liquids are performed by a reduced pressure thin film defoaming machine (capacity: 20 liters), the additives are mixed in the liquid, and the ultrasonic wave is further added. Secondary defoaming is performed by a defoaming device (25 kHz, 2 kW, capacity 1.5 liter, liquid pressure 3 kg / cm 2 ).

【0036】上記各脱泡装置により被脱泡液の粘度、流
量を変化させて脱泡の効果を試験した結果を表1に示
す。ここに○印は良好な完全な脱泡が達成されることを
表し、×印は完全な脱泡が不能であることを表す。
Table 1 shows the results of testing the defoaming effect by changing the viscosity and flow rate of the liquid to be defoamed by each of the above defoaming devices. Here, the mark ○ indicates that good and complete defoaming is achieved, and the mark x indicates that complete defoaming is not possible.

【0037】[0037]

【表1】 [Table 1]

【0038】このように、従来の脱泡方法では低粘度、
低流量のときは良好な脱泡を示すが粘度、流量共に高く
なってくると完全な脱泡は不可能になるのに反し、本発
明の方式で脱泡を行うと、かなりの高粘度、高流量の被
脱泡液に対しても完全脱泡が可能であることが確認でき
た。
As described above, the conventional defoaming method has a low viscosity,
When the flow rate is low, good defoaming is shown, but when both the viscosity and the flow rate increase, complete defoaming becomes impossible.On the other hand, when defoaming is performed by the method of the present invention, a considerably high viscosity, It was confirmed that complete defoaming was possible even for a high-flow rate defoaming liquid.

【0039】[0039]

【発明の効果】本発明の塗布液調整脱泡方法により脱泡
とともに塗布液中の溶存する空気の抜気も完全になり、
高粘度高濃度大流量の塗布液を高速で塗布する塗布液供
給方法が確立した。
According to the coating solution adjusting and defoaming method of the present invention, the deaeration of dissolved air in the coating solution is completely achieved together with defoaming.
A coating liquid supply method for applying a coating liquid with a high viscosity, a high concentration and a large flow rate at a high speed has been established.

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

【図1】超音波照射による破裂泡径と液圧との関係を示
すグラフ。
FIG. 1 is a graph showing a relationship between a burst bubble diameter and a liquid pressure by ultrasonic irradiation.

【図2】本発明の具体的な実施の形態の一例の概略構成
図。
FIG. 2 is a schematic configuration diagram of an example of a specific embodiment of the present invention.

【図3】本発明の具体的な実施の形態の一例の概略構成
図。
FIG. 3 is a schematic configuration diagram of an example of a specific embodiment of the present invention.

【図4】本発明の具体的な実施の形態の一例の概略構成
図。
FIG. 4 is a schematic configuration diagram of an example of a specific embodiment of the present invention.

【図5】本発明の具体的な実施の形態の一例の概略構成
図。
FIG. 5 is a schematic configuration diagram of an example of a specific embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10 溶解釜 20 混合釜 22 減圧装置 23 攪拌機 30 遠心分離装置 30B 薄膜流延減圧装置 32,42 ポンプ 34 貯留バッファー 40 超音波脱泡装置 43 圧力計 44 加圧弁 45 流量計 50 泡検出器 DESCRIPTION OF SYMBOLS 10 Dissolution pot 20 Mixing pot 22 Decompression device 23 Stirrer 30 Centrifuge 30B Thin film casting decompression device 32, 42 Pump 34 Storage buffer 40 Ultrasonic defoaming device 43 Pressure gauge 44 Pressure valve 45 Flow meter 50 Foam detector

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 複数の塗布液構成液を溶解する溶解プロ
セスと、続いてそれらを混合し塗布液に調整する混合プ
ロセスと、液の脱気プロセスと、前記混合した液の大径
泡を分離除去する一次脱泡プロセスと、一次脱泡後の液
を加圧した加圧液に超音波を照射し小径泡を溶解する二
次脱泡プロセスとを持つ塗布液調整脱泡方法であって、
前記二次脱泡プロセスが前記混合プロセス以降より下流
にあり、前記一次脱泡プロセスと前記脱気プロセスが前
記溶解プロセスと前記混合プロセス間又は該混合プロセ
ス中又は該混合プロセスと前記二次脱泡プロセス間の何
れかにあり、前記一次脱泡プロセスと前記脱気プロセス
はそれぞれ1つ以上含まれることを特徴とする塗布液調
整脱泡方法。
1. A dissolving process for dissolving a plurality of coating liquid constituent solutions, a mixing process for mixing them to prepare a coating liquid, a degassing process for the liquid, and separating a large-diameter bubble of the mixed liquid. A coating liquid adjustment defoaming method having a primary defoaming process for removing and a secondary defoaming process for irradiating ultrasonic waves to a pressurized liquid obtained by pressurizing the liquid after the primary defoaming to dissolve small-diameter bubbles,
The secondary defoaming process is downstream from the mixing process and the primary defoaming process and the degassing process are performed between the dissolving process and the mixing process or during the mixing process or the mixing process and the secondary defoaming. The method of any of claims 1 to 3, wherein the primary degassing process and the degassing process each include one or more processes.
【請求項2】 複数の塗布液構成液を溶解する溶解プロ
セスと、続いてそれらを混合し塗布液に調整する混合プ
ロセスと、液の脱気プロセスと、前記混合した液の大径
泡を分離除去する一次脱泡プロセスと、一次脱泡後の液
を加圧した加圧液に超音波を照射し小径泡を溶解する二
次脱泡プロセスとを持つ塗布液調整脱泡方法であって、
前記構成液を溶解後、薄膜流延減圧装置にそれぞれ又は
同時に通液して、前記脱気プロセスと前記一次脱泡プロ
セスとを行わせた後、前記混合プロセスを経て前記二次
脱泡プロセスを行うことを特徴とする塗布液調整脱泡方
法。
2. A dissolving process for dissolving a plurality of coating liquid constituent solutions, a mixing process for mixing them to prepare a coating liquid, a degassing process for the liquid, and separating a large-diameter bubble of the mixed liquid. A coating liquid adjustment defoaming method having a primary defoaming process for removing and a secondary defoaming process for irradiating ultrasonic waves to a pressurized liquid obtained by pressurizing the liquid after the primary defoaming to dissolve small-diameter bubbles,
After dissolving the constituent liquid, the liquid is passed through the thin film casting and depressurizing device respectively or simultaneously, and after performing the degassing process and the primary defoaming process, the secondary defoaming process is performed through the mixing process. A method of adjusting and defoaming a coating solution.
【請求項3】 複数の塗布液構成液を溶解する溶解プロ
セスと、続いてそれらを混合し塗布液に調整する混合プ
ロセスと、液の脱気プロセスと、前記混合した液の大径
泡を分離除去する一次脱泡プロセスと、一次脱泡後の液
を加圧した加圧液に超音波を照射し小径泡を溶解する二
次脱泡プロセスとを持つ塗布液調整脱泡方法であって、
前記構成液を溶解プロセスを経て、減圧下の混合釜に流
下添加させて前記脱気プロセスと前記混合プロセスを行
わせた後、遠心分離装置又は薄膜流延減圧処理装置で構
成される前記一次脱泡プロセスを経て前記二次脱泡プロ
セスを行わせることを特徴とする塗布液調整脱泡方法。
3. A dissolving process for dissolving a plurality of coating liquid constituent solutions, a mixing process for mixing them to prepare a coating liquid, a degassing process for the liquid, and separating a large-diameter bubble of the mixed liquid. A coating liquid adjustment defoaming method having a primary defoaming process for removing and a secondary defoaming process for irradiating ultrasonic waves to a pressurized liquid obtained by pressurizing the liquid after the primary defoaming to dissolve small-diameter bubbles,
After passing the dissolving process through the dissolving process and adding it down to a mixing vessel under reduced pressure to perform the degassing process and the mixing process, the primary degassing device configured by a centrifugal separator or a thin film casting and depressurizing device. A method of preparing and applying a coating solution, wherein the secondary defoaming process is performed through a foaming process.
【請求項4】 複数の塗布液構成液を溶解する溶解プロ
セスと、続いてそれらを混合し塗布液に調整する混合プ
ロセスと、液の脱気プロセスと、前記混合した液の大径
泡を分離除去する一次脱泡プロセスと、一次脱泡後の液
を加圧した加圧液に超音波を照射し小径泡を溶解する二
次脱泡プロセスとを持つ塗布液調整脱泡方法であって、
前記溶解プロセスと前記混合プロセスとを経て薄膜流延
減圧処理装置で連続的に前記脱気プロセスと前記一次脱
泡プロセスを行わせ、その後で前記二次脱泡プロセスを
行わせることを特徴とする塗布液調整脱泡方法。
4. A dissolving process for dissolving a plurality of coating liquid constituent liquids, a mixing process for mixing and adjusting them into a coating liquid, a liquid degassing process, and separating a large-diameter bubble of the mixed liquid. A coating liquid adjustment defoaming method having a primary defoaming process for removing and a secondary defoaming process for irradiating ultrasonic waves to a pressurized liquid obtained by pressurizing the liquid after the primary defoaming to dissolve small-diameter bubbles,
The deaeration process and the primary defoaming process are continuously performed in a thin film casting decompression treatment device through the dissolving process and the mixing process, and then the secondary defoaming process is performed. Coating liquid adjustment defoaming method.
【請求項5】 前記二次脱泡プロセス以降コーターまで
の間で液温を低下させるようにしたことを特徴とする請
求項1〜4の何れか1項に記載の塗布液調整脱泡方法。
5. The method for adjusting and defoaming a coating solution according to claim 1, wherein the temperature of the liquid is lowered between the secondary defoaming process and the coater.
【請求項6】 前記塗布液は写真感光材料用の塗布液で
あることを特徴とする請求項1〜5の何れか1項に記載
の塗布液調整脱泡方法。
6. The method according to claim 1, wherein the coating liquid is a coating liquid for a photographic light-sensitive material.
【請求項7】 前記塗布液がカーテン塗布コーターで塗
布されることを特徴とする請求項1〜6の何れか1項に
記載の塗布液調整脱泡方法。
7. The method according to claim 1, wherein the coating liquid is applied by a curtain coating coater.
JP06564198A 1998-03-16 1998-03-16 Coating liquid adjustment defoaming method Expired - Fee Related JP3658982B2 (en)

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US6884281B2 (en) 2000-09-01 2005-04-26 Fuji Photo Film Co., Ltd. Method and apparatus for preparation and deaeration of coating liquid
US7294171B2 (en) 2003-12-01 2007-11-13 Fujifilm Corporation Method and apparatus for degassing coating liquid
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JP2020171908A (en) * 2019-04-10 2020-10-22 大阪サニタリー株式会社 High-viscosity liquid automatic preparation device and preparation method
CN112058203A (en) * 2020-09-10 2020-12-11 江苏飞亚化学工业有限责任公司 Self-defoaming reactor for liquid alkylation reaction
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Publication number Priority date Publication date Assignee Title
US6884281B2 (en) 2000-09-01 2005-04-26 Fuji Photo Film Co., Ltd. Method and apparatus for preparation and deaeration of coating liquid
JP4715001B2 (en) * 2001-02-23 2011-07-06 株式会社Ihi Colored paper manufacturing method and apparatus
KR20030010486A (en) * 2002-03-28 2003-02-05 주식회사 피엠시코리아 Dearating apparatus for coating colour
US7294171B2 (en) 2003-12-01 2007-11-13 Fujifilm Corporation Method and apparatus for degassing coating liquid
JP2010214833A (en) * 2009-03-18 2010-09-30 Ricoh Co Ltd Coating material for thermosensitive recording medium, and method and apparatus for manufacturing thermosensitive recording medium
JP2020171908A (en) * 2019-04-10 2020-10-22 大阪サニタリー株式会社 High-viscosity liquid automatic preparation device and preparation method
CN112058203A (en) * 2020-09-10 2020-12-11 江苏飞亚化学工业有限责任公司 Self-defoaming reactor for liquid alkylation reaction
CN112213270A (en) * 2020-09-29 2021-01-12 湖北鑫英泰系统技术股份有限公司 Stirring speed control method and device based on viscosity
CN112573860A (en) * 2020-12-21 2021-03-30 深圳恒固纳米科技有限公司 Novel water-based nano thermal insulation material and preparation method thereof

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