JP2009013211A - Automatic concentration control apparatus for cleaning liquid and method for using the same - Google Patents

Automatic concentration control apparatus for cleaning liquid and method for using the same Download PDF

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JP2009013211A
JP2009013211A JP2007173711A JP2007173711A JP2009013211A JP 2009013211 A JP2009013211 A JP 2009013211A JP 2007173711 A JP2007173711 A JP 2007173711A JP 2007173711 A JP2007173711 A JP 2007173711A JP 2009013211 A JP2009013211 A JP 2009013211A
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liquid
cleaning
concentration
powder
cleaning liquid
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Koji Yoshida
幸司 吉田
Shohei Misaki
昌平 三崎
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Chuo Kagaku Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide an apparatus that easily prepares a cleaning liquid, automatically controls the concentration of a cleaning liquid to prepare a cleaning liquid and smoothly functions the whole system and a method for using the apparatus in a pipe conduit cleaning apparatus using a powder detergent. <P>SOLUTION: In a plant having a pipe conduit for mixing and processing a liquid, when the inside of the pipe conduit is cleaned by using a cleaning liquid composed of the powder detergent A in order to clean the pipe conduit, an apparatus for a cleaning liquid production process is installed separately from a plant main body and the process is divided into a high-concentration cleaning liquid preparation process and a diluted cleaning liquid C preparation process. Consequently, the detergent is uniformly dispersed, the concentration is easily adjusted and a plurality of powders are readily mixed and prepared. The automatic concentration control apparatus for a cleaning liquid is composed of a sensor such as a conductivity meter 5 etc., to be instantly and continuously used and a computer controller. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、洗浄液の自動濃度管理装置およびその使用方法に関するもの、詳しくは、単数あるいは複数の粉体洗浄剤を溶解してなる洗浄液の濃度を自動調整するための自動濃度管理装置およびその使用方法に関するものである。   The present invention relates to an automatic concentration management apparatus for cleaning liquid and a method for using the same, and more particularly, an automatic concentration management apparatus for automatically adjusting the concentration of a cleaning liquid obtained by dissolving one or more powder cleaning agents and a method for using the automatic concentration management apparatus. It is about.

従来、溶液の濃度管理方法および装置については、数多く知られている。また、粉体を溶解して濃度管理する方法および装置も色々なものが建設されている。例えば、ホッパーを用いて上部から分体を投入するにあたり、開口面を下方に回転させる駆動手段を備えた粉体供給手段とその下方に位置する溶融槽とを設けてなる誘拐装置(例えば、特許文献1)、貯蔵ホッパーから溶解槽に供給された粉体の計量手段と粉体量に基づいて給水量を制御するコンピューターとを有する溶解装置(例えば、特許文献2)が提案されている。 Conventionally, many solution concentration management methods and apparatuses are known. In addition, various methods and apparatuses for dissolving the powder to control the concentration have been constructed. For example, a kidnapping apparatus (for example, a patented device) provided with a powder supply means provided with a drive means for rotating the opening surface downward and a melting tank located therebelow when a hopper is used to introduce a body from the top. Document 1), a melting apparatus (for example, Patent Document 2) has been proposed that has a measuring means for powder supplied from a storage hopper to a melting tank and a computer that controls the amount of water supply based on the amount of powder.

食品生産工場(特に飲料水や牛乳などの液状食品)において、製造施設の洗浄方法としては、COP(Cleaning Out Place;分解洗浄)、CIP(Cleaning In Place;定置洗浄)がある。
COPは、機械や部品を分解し、洗剤溶液を用いて手洗い(ブラッシング)もしくは、洗剤を循環させて洗浄する方法。構造の複雑な機器や部品の洗浄、床・壁・天井・タンク外面等の洗浄に採用される。
CIPは、機器や部品を分解することなく、設備構成の中に洗浄機能を組み込ませて構築を行い、洗剤溶液の化学エネルギー・熱エネルギー・運動エネルギーを利用して洗浄する方法をいう。パイプライン等洗浄設備の構造が複雑でないものに利用されている。
使用する薬剤は、注意深く取扱い、食品を汚染する危険を避けるために食品とは区別し、明確に表示した容器に保存する必要がある。
In a food production factory (particularly liquid food such as drinking water and milk), there are COP (Cleaning Out Place) and CIP (Cleaning In Place) as cleaning methods for manufacturing facilities.
COP is a method of disassembling machines and parts and washing them with a detergent solution (brushing) or circulating detergent. It is used for cleaning equipment and parts with complex structures, and for cleaning floors, walls, ceilings, and tank outer surfaces.
CIP refers to a method in which a cleaning function is built into a facility configuration without disassembling equipment and parts, and cleaning is performed using chemical energy, thermal energy, and kinetic energy of a detergent solution. It is used for pipes and other cleaning facilities that are not complicated.
The drugs used should be handled carefully and stored in a clearly labeled container to distinguish them from food to avoid the risk of contaminating the food.

CIP洗浄は、一般的にアルカリ性洗浄剤による洗浄、および酸性洗浄剤による洗浄があり、1000〜2000L程度の洗浄液貯蔵タンク(アルカリ性、酸性共に)を有している。
CIP洗浄は、設備の使用後に アルカリ洗い→水洗→酸洗い→水洗 の順で行い、洗浄液劣化や、水洗水の混入によりタンク内の洗浄液の洗浄剤濃度が低下するために洗浄剤の原液、又は、粉末を定期的に補給する必要があった(補給時期を洗浄液の導電率で管理する場合もある。)
特開平10−232号公報 特開平6−226068号公報
CIP cleaning generally includes cleaning with an alkaline cleaning agent and cleaning with an acidic cleaning agent, and has a cleaning liquid storage tank (both alkaline and acidic) of about 1000 to 2000 L.
CIP cleaning is performed in the order of alkali cleaning → water cleaning → acid cleaning → water cleaning after use of the equipment. Since the cleaning liquid concentration in the tank decreases due to deterioration of the cleaning liquid or mixing of cleaning water, It was necessary to replenish the powder regularly (the replenishment time may be controlled by the conductivity of the cleaning solution).
JP-A-10-232 JP-A-6-226068

従来の洗剤液を上部から投入することで、洗浄を行う装置では、粉体の供給装置と溶解装置とが一体化され、供給装置のフィーダーも固定されたものであり、1種類の決められた粉体か似たような粉体(食塩、塩類)(特許文献1)、染料(特許文献2)にしか適応されず、そのため、多様な特性を有するものには対応が難しく、高精度で迅速に濃度管理をする機能を有する装置がなかった。   In an apparatus for cleaning by introducing a conventional detergent solution from the top, the powder supply device and the dissolution device are integrated, and the feeder feeder is also fixed, and one type is determined. Applicable only to powder or similar powders (salt, salt) (Patent Document 1) and dye (Patent Document 2). Therefore, it is difficult to cope with those having various characteristics, and high accuracy and speed There was no device having a function of controlling concentration.

例えば、粉体界面活性剤や粉体洗浄剤のようなものは非常に多くの種類や形状があり、粒子径や吸湿性等の性状が異なり、これらを自動で供給し濃度管理をする装置はなかった。
また、供給装置と溶解装置との高さ、位置関係が使用条件により異なる場合にも、対応が面倒であった。本発明の目的は、粉体洗浄剤(A)の特性、当該粉体供給装置と溶解装置の位置関係が変わっても簡易に対応できる、多種類の粉体洗浄剤からなる洗浄液を迅速正確に自動濃度管理ができる方法を提供することである。
For example, there are many types and shapes of powder surfactants and powder detergents, and the properties such as particle diameter and hygroscopicity are different. There wasn't.
Further, even when the height and positional relationship between the supply device and the melting device differ depending on the use conditions, it is troublesome. The object of the present invention is to quickly and accurately provide a cleaning liquid composed of various types of powder cleaning agents that can easily cope with changes in the characteristics of the powder cleaning agent (A) and the positional relationship between the powder supply device and the dissolving device. It is to provide a method capable of automatic concentration management.

また、従来の洗剤液を上部から投入する技術では、洗浄剤のタンクが5000L以上になってくると、タンクの高さが高くなり、洗浄剤を補給するのに大変手間がかかっていた。洗浄剤が液体の場合であれば、配管を行いポンプで移送すれば容易であるが、液体洗浄剤は粉体洗浄剤に対して有効成分(アルカリ洗剤は主に水酸化ナトリウム、界面活性剤、キレート剤。酸性洗剤は主に硝酸尿素、硝酸、燐酸、キレート剤、界面活性剤。)の濃度が低く(約1/3程度)、流動性、ハンドリング性、保管場所等の問題でコスト的に不利、液体洗浄剤の濃度を高くすれば、粘性が高くなり流速が低下し、更に液体が均一にならず、分離が起こるという問題があった。 In addition, in the conventional technology in which the detergent solution is introduced from the upper part, when the tank of the cleaning agent reaches 5000 L or more, the height of the tank increases, and it takes much time to supply the cleaning agent. If the cleaning agent is liquid, it can be easily done by piping and transporting it with a pump. However, the liquid cleaning agent is an active ingredient for the powder cleaning agent (alkaline detergent is mainly sodium hydroxide, surfactant, Chelating agents. Acid detergents mainly contain urea nitrate, nitric acid, phosphoric acid, chelating agents, and surfactants.) The concentration is low (about 1/3), and costs are low due to problems such as fluidity, handling, and storage location. Disadvantageously, if the concentration of the liquid detergent is increased, there is a problem that the viscosity increases and the flow rate decreases, and the liquid does not become uniform and separation occurs.

粉体洗浄剤の場合、通常5Kgバッグで小分けされているが、その袋を持ってタンクに登って補給する作業が非常に面倒であり、また、水酸化ナトリウム等の劇物を含有した洗浄剤を高所で取り扱う必要があり、落下や飛散した場合に非常に危険であった。 In the case of powder detergent, it is usually subdivided into 5Kg bags, but the work of climbing the tank with the bag and replenishing it is very troublesome, and the detergent contains deleterious substances such as sodium hydroxide. Must be handled at high altitude, and it was very dangerous when dropped or scattered.

また、タンクのホッパーへの粉体移送装置を用いて洗浄液タンクの下から移送しようとした場合には、トランジー等の非常に高価な移送装置が必要となり、ベルトコンベアー等を用いると、狭い作業現場では設置のスペースが得にくい、また、水酸化ナトリウム等の潮解性の激しい薬品を使用するため、移送装置内に残った洗剤が湿気の為に潮解し、目詰まりをおこす等の問題があった。 In addition, when trying to transfer from the bottom of the cleaning liquid tank using a powder transfer device to the tank hopper, a very expensive transfer device such as trangie is required. In this case, it is difficult to obtain a space for installation, and there is a problem that the detergent remaining in the transfer device is deliquescent due to moisture and clogging due to the use of highly deliquescent chemicals such as sodium hydroxide. .

上記課題を構造的に解決するため、粉体供給装置の下方に高濃度液調製装置(溶解槽)を設けると共に、高濃度液を希釈する希釈洗浄装置(希釈槽)と導電率計を設け、導電率に基づいて高濃度液供給量および給水量を制御する手段を設けることで、容易に対応でき、同時にこの装置を用いて迅速正確に濃度を管理する手法を確立した。
具体的には、本発明は、上述の洗浄液の自動濃度管理装置を備えた洗浄液の濃度調製供給装置とそのシステム全体の運用方法から課題の解決をはかるものである。
In order to solve the above problems structurally, a high-concentration liquid preparation device (dissolution tank) is provided below the powder supply device, a dilution cleaning device (dilution tank) and a conductivity meter for diluting the high-concentration liquid are provided, By providing means for controlling the supply amount of high-concentration liquid and the amount of water supply based on the conductivity, a method for managing the concentration quickly and accurately using this device was established.
Specifically, the present invention solves the problem from the cleaning liquid concentration adjusting and supplying apparatus provided with the above-described cleaning liquid automatic concentration management apparatus and the operation method of the entire system.

具体的なシステムの構成としては、粉体攪拌機(1a)とホッパー(1b)を備え、粉体洗浄剤(A)を供給する、粉体供給装置(1);液体攪拌機(2a)を備えた溶解槽(2b)から構成され、ホッパー(1b)の下方に設けられた、高濃度液調製装置(2);給水装置(3);高濃度液を移送する液体移送管路(4);導電率計(5);液体攪拌機(6a)を備えた希釈槽(6b)から構成される、希釈洗浄液調製装置(6);および、導電率計(5)で計測された誘電率に基づいて、液体移送管路(4)もしくは給水装置(3)に供給指示を出す制御装置(7)、すなわち、自動濃度管理装置から構成される。 As a specific system configuration, a powder stirrer (1a) and a hopper (1b) are provided, and a powder supply device (1) and a liquid stirrer (2a) are provided to supply a powder cleaning agent (A). High-concentration liquid preparation device (2); water supply device (3); liquid transfer pipe (4) for transferring the high-concentration liquid, composed of a dissolution tank (2b) and provided below the hopper (1b); On the basis of the dielectric constant measured by the conductivity meter (5); and the diluted washing liquid preparation device (6) comprising a dilution tank (6b) equipped with a liquid stirrer (6a); It is comprised from the control apparatus (7) which gives a supply instruction | indication to a liquid transfer pipe line (4) or a water supply apparatus (3), ie, an automatic density | concentration management apparatus.

作動の流れとしては、粉体洗浄剤(A)の洗浄液の自動濃度管理装置、ならびに、自動濃度管理装置を作動させて、粉体攪拌機(1a)を始動させて、粉体供給装置(1)のホッパー(1b)から粉体洗浄剤(A)を溶解槽に投入すると共に、給水装置(3)からの水もしくは希釈槽(6b)からの希釈洗浄液を溶解槽(2b)に投入すると共に、給水装置(3)からの水もしくは希釈槽(6b)からの希釈洗浄液を溶解槽(2b)に投入し、液体攪拌機(2a)を始動させ、粉体洗浄剤(A)を水もしくは、希釈洗浄液に溶解させた、5〜30%の高濃度液(B)を調製し、高濃度液(B)を液体移送管路(4)から、希釈槽(6b)に投入すると共に給水装置(3)から水を投入し、液体攪拌機(6a)を始動させて高濃度溶液(B)を水で希釈して、0.5〜3%(以後、本出願中の溶質の濃度は、通常用いられる溶液に対する質量パーセント濃度を表すものとする)の希釈液を調製して行うが、導電率計(5)で希釈洗浄液(C)の導電率を計測し、計測された導電率に基づいて制御装置(7)から、液体移送管路(4)もしくは供給装置(3)に給水指示を出すことによって、粉体洗浄剤(A)の希釈洗浄液(C)の濃度を自動的に調整することにより、洗浄液の自動濃度管理装置を効果的に用いることができる。 As the flow of operation, an automatic concentration management device for the cleaning liquid of the powder cleaning agent (A) and an automatic concentration management device are operated to start the powder agitator (1a), and the powder supply device (1). In addition to charging the powder cleaning agent (A) from the hopper (1b) to the dissolution tank, water from the water supply device (3) or diluted cleaning liquid from the dilution tank (6b) is charged to the dissolution tank (2b), Water from the water supply device (3) or diluted cleaning liquid from the dilution tank (6b) is charged into the dissolution tank (2b), the liquid agitator (2a) is started, and the powder cleaning agent (A) is added to water or diluted cleaning liquid. A high concentration liquid (B) dissolved in 5 to 30% is prepared, and the high concentration liquid (B) is introduced into the dilution tank (6b) from the liquid transfer pipe (4) and the water supply device (3) Water is added to the liquid, and the liquid stirrer (6a) is started so that the high-concentration solution (B) Is diluted to 0.5 to 3% (hereinafter, the concentration of the solute in the present application represents the mass percent concentration with respect to a commonly used solution). In (5), the conductivity of the diluted cleaning liquid (C) is measured, and a water supply instruction is issued from the control device (7) to the liquid transfer line (4) or the supply device (3) based on the measured conductivity. By automatically adjusting the concentration of the diluted cleaning liquid (C) of the powder cleaning agent (A), the automatic concentration management device for the cleaning liquid can be effectively used.

このシステムの運用方法により、特にCIP洗浄においては、装置、部品を分解することなく、設備の使用後に製造ラインの管路に沿って洗浄液を流し込むため、残留液のために経時的に洗浄液の濃度が希釈されるという特性があるので、洗浄液の濃度が薄くなり過ぎないように次のような濃度の自動測定結果によるフィードッバック濃度調整をうまく行うことが可能になる。 With this system operation method, especially in CIP cleaning, the cleaning liquid is poured along the pipeline of the production line after use of the equipment without disassembling the equipment and parts. Therefore, it is possible to adjust the feedback density by the automatic measurement result of the following concentration so that the concentration of the cleaning solution does not become too thin.

導電率からの下限値以下の濃度の信号が来た場合に、一定量の洗浄剤を溶解槽にて計量し、ポンプで移送可能な濃度(50%以下、好ましくは25%以下)まで、水で希釈後、攪拌して洗浄液タンクへの配管で移送する。
高濃度液を移送後に溶解槽に水を送り、溶解槽、ポンプ、配管をすすぐようにする。
洗浄液タンク内の洗浄液の濃度は、注水して任意の濃度(通常3〜1%)に再調整されるか、高濃度洗浄液が注水後に洗浄液タンク内の濃度が許容される上限値(通常5〜3%)以下であれば、CIPの水洗水や洗浄液の劣化の為に、経時的に規定濃度まで低下する。いずれにしても、下限値(0.8%以下程度)を下回れば、自動的に高濃度液が補充される。
When a signal with a concentration below the lower limit value from the conductivity comes, weigh a certain amount of cleaning agent in the dissolution tank and bring it to a concentration (50% or less, preferably 25% or less) that can be pumped. After diluting with, it is stirred and transferred by piping to the cleaning liquid tank.
After transferring the high-concentration liquid, send water to the dissolution tank and rinse the dissolution tank, pump, and piping.
The concentration of the cleaning liquid in the cleaning liquid tank is adjusted to an arbitrary concentration (usually 3 to 1%) by pouring water, or an upper limit (usually 5 to 5) at which the concentration in the cleaning liquid tank is allowed after the high concentration cleaning liquid is poured. 3%) or less, it will fall to the specified concentration over time due to deterioration of CIP water and cleaning solution. In any case, the high-concentration solution is automatically replenished when the value falls below the lower limit (about 0.8% or less).

低コストの粉体の洗浄剤を手間をかけずに安全に洗浄液タンクに投入可能となった。   A low-cost powder cleaning agent can be safely put into the cleaning liquid tank without much effort.

高濃度洗浄液を移送直前に溶解槽で攪拌して、全量を移送するために、高濃度洗浄液が分離するような液であっても、成分比に変動なく洗浄タンクへ移送可能となった。   Since the high-concentration cleaning liquid is stirred in the dissolution tank immediately before the transfer and the entire amount is transferred, even a liquid that separates the high-concentration cleaning liquid can be transferred to the cleaning tank without fluctuation in the component ratio.

高濃度洗浄液を移送後に、溶解槽、ポンプ配管を水ですすぐため、層分離する液体を成分比に変動無く送られる利点に加えて、ポンプや配管が洗剤の残渣による腐食や目詰まりを起こすことも無くなる利点がある。 Since the dissolution tank and pump piping are rinsed with water after transferring the high-concentration cleaning solution, the pump and piping can be corroded and clogged by detergent residues in addition to the advantage that the liquid that separates the layers can be sent without fluctuation in the component ratio. There is also an advantage to be eliminated.

移送する必要量の洗剤(通常5Kg)のみを溶解し、移送するため、溶解槽、攪拌設備等が非常に小型で低コストで作製することが可能になった。   Since only the necessary amount of detergent (usually 5 kg) to be transported is dissolved and transported, the dissolution tank, the stirring equipment, etc. can be made very small and low-cost.

非常に多種類の性状も異なる粉体、例えば、吸湿性や潮解性を有し、ブロックキング、未混合塊状残留、未溶解物残存を起こしやすい粉体洗浄剤についても、迅速正確に濃度調整された洗浄液を製造することができる。特に、水酸化ナトリウムについては、潮解性の高い劇薬で上記の取扱いが困難な粉体あるが、従来から、洗浄用としての需要が高く、近年、狂牛病の異常プリオンの毒性の除去においても、厚生労働省指定の世界保健機関(WHO)の処理基準でも約2.8パーセントの水酸化ナトリウム水溶液の使用が義務付けられ、その優れた洗浄殺菌力は、高く評価され、食品産業の代表的な洗浄剤であり、中でも、CIP洗浄においては、初期洗浄に不可欠な洗浄液となっている。 Concentrations of powders with very different types of properties, such as powder detergents that have hygroscopicity and deliquescence and are prone to block king, unmixed bulk residue, and undissolved residue, can be quickly and accurately adjusted. Can be produced. In particular, sodium hydroxide is a highly deliquescent powerful drug that is difficult to handle as described above. However, there has been a high demand for washing from the past. According to the World Health Organization (WHO) treatment standards designated by the Ministry of Health, Labor and Welfare, the use of about 2.8 percent sodium hydroxide aqueous solution is obligatory. In particular, in CIP cleaning, the cleaning liquid is indispensable for initial cleaning.

未溶解粉体の溶解を完了させるための手段(未溶解粉体を溶解槽に押戻す、噴射ノズルや循環ライン)を用いる必要がなく、未溶解粉体の溶解に要する時間と手間がかからないようにできる。   There is no need to use the means to complete the dissolution of the undissolved powder (pushing the undissolved powder back into the dissolution tank, spray nozzle or circulation line), so that it does not take time and effort to dissolve the undissolved powder. Can be.

従来の直接、生産ラインの上方からホッパーで洗浄液を投入するのでなくて、洗浄液の攪拌製造を分離したことにより、プラントの構成が、用地の形状、製造ラインの形態に合わせて設置することができる、また運転やメンテナンスも容易となり、低コスト化を図れる。   Rather than supplying the cleaning liquid directly from the top of the production line with a hopper, the plant configuration can be installed in accordance with the shape of the site and the form of the manufacturing line by separating the stirring manufacturing of the cleaning liquid. In addition, operation and maintenance are easy, and cost can be reduced.

次に、本発明の実施の形態を図面に基づいて説明する。
図1は、本発明の1実施例(洗浄後の自動濃度管理装置)を模式的に示すフロー図である。
この自動濃度管理装置は、粉体供給装置(1)、高濃度液調製装置(2)、給水装置(3)、液体移送管路(4)、導電率形(5)、希釈溶液調製装置(6)、および制御装置(7)から構成される。各装置の大きさや形状は、特に限定されない。
Next, embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is a flowchart schematically showing one embodiment (automatic concentration management apparatus after cleaning) of the present invention.
This automatic concentration management device comprises a powder supply device (1), a high concentration liquid preparation device (2), a water supply device (3), a liquid transfer line (4), a conductivity type (5), a diluted solution preparation device ( 6) and a control device (7). The size and shape of each device are not particularly limited.

粉体供給装置は(1)は、必要に応じてブリッジ防止機能を有する粉体攪拌機(1a)とホッパー(1b)を備える。
粉体攪拌機(1a)は、ホッパーの投入口から鉛直線方向に設置された粉体のブリッジ防止機能を備えた攪拌翼のついたもの、例えば、スクリュー型やリボン型、ミキサー型が好ましい形状である。
The powder supply apparatus (1) includes a powder agitator (1a) and a hopper (1b) having a bridge prevention function as necessary.
The powder stirrer (1a) is preferably provided with a stirring blade having a function of preventing powder bridging installed in the vertical direction from the inlet of the hopper, for example, a screw type, a ribbon type, or a mixer type. is there.

ホッパー(1b)は、粉体洗浄剤をその下方の溶解槽(2b)落下投入するので、その投入に適した外形状のものであれば特に制限されないが、滑らかな形状であることが望ましい。また、ホッパーの少なくとも内壁表面にフッ素系樹脂加工のような低摩擦、低付着処理を施すことが望ましい。また、ホッパーに振動を加え、粉体が、落下しやすくする方式を採用することもできる。
ホッパーは、また、湿気を遮断した構造、例えば、特許文献1に記載のような構造、すなわち、外部から異物が混入しないように、側面が囲い(13)で覆われ、また上面が開閉蓋(14)で覆われた密閉構造、下方の溶解槽(2b)からの湿気の影響を受けて粉体が、吸湿固化しないように、ホッパー(1)下部側に開口部をもたない構造、囲い(13)の側面の一部には、フィルター(15)が設けられていて、内部の湿気を外部に排気するとともに外部の異物などが混入しない構造とすることもできる。
The hopper (1b) drops the powder cleaning agent into the dissolution tank (2b) below the hopper (1b), and is not particularly limited as long as it has an outer shape suitable for the charging, but it is preferably a smooth shape. In addition, it is desirable that at least the inner wall surface of the hopper be subjected to a low friction and low adhesion treatment such as fluorine resin processing. In addition, it is possible to adopt a method in which vibration is applied to the hopper so that the powder easily falls.
The hopper also has a structure in which moisture is blocked, for example, a structure as described in Patent Document 1, that is, a side surface is covered with an enclosure (13) so that foreign matter does not enter from the outside, and an upper surface is an open / close lid ( 14) A sealed structure covered with 14), a structure without an opening on the lower side of the hopper (1), an enclosure so that the powder does not absorb and solidify under the influence of moisture from the lower dissolution tank (2b) A filter (15) may be provided on a part of the side surface of (13) to exhaust internal moisture to the outside and prevent external foreign matter from entering.

ホッパー(1b)は、粉体洗浄剤をその下方の溶解槽(2b)に落下投入するので、ホッパー(1b)の下部には、その投入に用いる粉体投入弁としてスライドゲートバルブ(SGB)を設けることが好ましく、それによって粉体投入の制御(投入の時期、速度および投入量の調整)を行うこと(すなわち、通常行われる、1回目は、全開にして大投入(約3〜4Kg)を行い、2回目以降は、半開または、微開にして、小投入を繰り返す好ましい方法など)ができる。また、粉体投入弁に代えて、他の投入手段、例えば、特許文献1時記載のような、開口部を上面に有し、開口面を下方に移動させる駆動手段を備えた粉体供給手段を用いて、粉体投入の制御を行うこともできる。   Since the hopper (1b) drops the powder cleaning agent into the dissolution tank (2b) below it, a slide gate valve (SGB) is provided at the lower part of the hopper (1b) as a powder charging valve used for the charging. It is preferable to provide, thereby controlling the powder feeding (adjustment of the timing, speed and amount of feeding) (that is, normally performed, the first time, fully opened and large charging (about 3 to 4 kg)). In the second and subsequent times, a preferable method in which small input is repeated by half-opening or slightly opening is possible. Further, in place of the powder injection valve, other supply means, for example, a powder supply means having an opening on the top surface and a drive means for moving the opening surface downward as described in Patent Document 1 It is also possible to control the charging of powder using

粉体供給装置(1)粉体攪拌機(1a)粉体投入弁(SGB)もしくは、他の投入制御手段は、制御装置(7)と連携して、攪拌のオン・オフおよび攪拌速度を自動で制御し、自動的に所望量の粉体洗浄剤(A)の投入を制御することができる。   Powder supply device (1) Powder stirrer (1a) Powder input valve (SGB) or other input control means, in conjunction with the control device (7), automatically turns on / off stirring and stirring speed It is possible to control and automatically supply a desired amount of the powder cleaning agent (A).

高濃度液調製装置(2)は、液体攪拌機(2a)を備えた溶解槽(2b)から構成さえる。液体攪拌機(2a)および溶解槽(2b)としては、従来公知のものを用いることができる。
液体攪拌機(2a)には、粉体の液体中への混合攪拌に通常用いられているものが使用でき、攪拌翼によるものが代表的であり、3枚プロペラによるものが好ましい。
液体攪拌装置(2a)を用いる数に制限は、無く、設置位置にも制限はないが、洗剤を上部からの投入するため、攪拌は、底面から行うのが好ましい。
The high-concentration liquid preparation device (2) is composed of a dissolution tank (2b) equipped with a liquid stirrer (2a). A conventionally well-known thing can be used as a liquid stirrer (2a) and a dissolution tank (2b).
As the liquid stirrer (2a), those usually used for mixing and stirring powder into a liquid can be used, and those using a stirring blade are typical, and those using a three-propeller are preferable.
There is no limit to the number of liquid stirrers (2a) used, and the installation position is not limited. However, since the detergent is introduced from the top, stirring is preferably performed from the bottom.

溶解槽(2b)としては、粉体の溶解に通常使用されているものが使用できる。その形状は、とくに制限されず、円筒状でも、直方体状でもよく、底面に傾斜部分を設け、粉体が攪拌部(攪拌機に近い部分)に集まりやすい構造としたのでよい。その材質も特に限定されず、ステンレススチール製のものが好適に使用できる。また、溶解槽(2b)の容量は用途に応じて設定が可能である。通常は、10〜50L、好ましくは、20〜30Lである。 As the dissolution tank (2b), those usually used for powder dissolution can be used. The shape is not particularly limited, and may be a cylindrical shape or a rectangular parallelepiped shape, and may have a structure in which an inclined portion is provided on the bottom surface and the powder easily collects in the stirring portion (portion close to the stirrer). The material is not particularly limited, and those made of stainless steel can be suitably used. Moreover, the capacity | capacitance of a dissolution tank (2b) can be set according to a use. Usually, it is 10-50L, Preferably it is 20-30L.

溶解槽(2b)は、ホッパー(1b)から、粉体投入弁または、他の手段(好ましくは粉体投入弁)を介して、粉体洗浄剤が投入されるように、ホッパー(1b)の下方に設けられ、一方、給水装置(3)から水が供給されるように配管する。また、必要により、給水装置(3)からの給水に加えて(または、それに代えて)、希釈槽(2b)の上方に設置される粉体供給装置(1)〔粉体攪拌機(1a)およびホッパー(1b)〕は、1個でも複数個でもよい。 The dissolution tank (2b) is disposed in the hopper (1b) so that the powder cleaning agent is charged from the hopper (1b) via a powder charging valve or other means (preferably a powder charging valve). On the other hand, piping is provided so that water is supplied from the water supply device (3). If necessary, in addition to (or instead of) the water supply from the water supply device (3), the powder supply device (1) installed above the dilution tank (2b) [powder stirrer (1a) and The hopper (1b)] may be one or plural.

溶解槽(2b)には、必要により、液面センサー(2c)が備えられ。また、他の測定装置(温度計など)が差し込まれている。これらは、制御装置(7)に繋がっており、それらの測定値に基づいて、制御装置(7)による供給等の指示を行うことができる。
高濃度液調製装置(2)〔液体攪拌機(2a)、液面センサー(2c)〕も制御装置(7)に連絡して攪拌のオン・オフおよび攪拌速度、ならびに粉体洗浄剤および水(もしくは希釈液)の供給がコンピューター制御により、細かく設定条件で自動的に制御できる構成とする。
The dissolution tank (2b) is provided with a liquid level sensor (2c) if necessary. In addition, other measuring devices (such as thermometers) are inserted. These are connected to the control device (7), and based on the measured values, instructions such as supply by the control device (7) can be performed.
The high-concentration liquid preparation device (2) [liquid stirrer (2a), liquid level sensor (2c)] also communicates with the control device (7) to turn on / off the stirring and stirring speed, as well as powder detergent and water (or The supply of the diluent is controlled automatically by computer control with fine setting conditions.

給水装置(3)としては、給水が制御できるものなら、特に限定はされず、溶解槽(2b)への配管の先端部もしくは、その近辺に制御弁(水投入弁)を設けたものでも、給水源そのものに制御弁が連結したものでもよい。給水装置(3)は、制御装置(7)と連結して自動給的に給水が制御できる構成とする。給水装置(3)には、溶解槽(2b)へ給水するものと希釈槽(6b)へ給水するものとが含まれ、それぞれの水投入弁が制御装置(7)の指示に従って自動的に給水が制御できるようにする。   The water supply device (3) is not particularly limited as long as the water supply can be controlled. Even if the control valve (water supply valve) is provided at or near the tip of the pipe to the dissolution tank (2b), A control valve may be connected to the water supply source itself. The water supply device (3) is connected to the control device (7) so that the water supply can be controlled automatically. The water supply device (3) includes one that supplies water to the dissolution tank (2b) and one that supplies water to the dilution tank (6b), and each water supply valve automatically supplies water according to the instructions of the control device (7). To be able to control.

液体移送管路(4)は高濃度制御装置(2)で、調整された高濃度液(B)を希釈洗浄液調製装置(6)〔希釈槽(6b)〕へ移送するラインである。管路(4)は、高濃度液投入弁(4a)および排出ポンプ(4b)を備えた液体配管から構成される。
高濃度液投入弁(4a)および排出ポンプ(4b)は制御装置(7)と連結して、自動的に高濃度液の供給が制御できる。管路(4)の途中もしくは、高濃度液調製装置(2)〔溶解槽(2b)〕の排出口には、必要により、未溶解の粉体洗浄を濾別する手段(ストレイナー、フィルター、スクリーン等)が設けられてもよい。
The liquid transfer pipe (4) is a line for transferring the adjusted high concentration liquid (B) to the diluted cleaning liquid preparation apparatus (6) [dilution tank (6b)] by the high concentration control apparatus (2). The pipe (4) is constituted by a liquid pipe provided with a high concentration liquid charging valve (4a) and a discharge pump (4b).
The high-concentration liquid input valve (4a) and the discharge pump (4b) can be connected to the control device (7) to automatically control the supply of the high-concentration liquid. In the middle of the pipe (4) or at the outlet of the high-concentration liquid preparation device (2) [dissolution tank (2b)], if necessary, means for filtering out undissolved powder washing (strainer, filter, A screen or the like) may be provided.

導電率計(5)としては、液体の導電率(電導度)の測定に通常使用されているものが使用できるし、多様な洗浄液の濃度調整に対応できるよう、ペーハー(水素イオン濃度)測定を併側するなど多機能を備えたものを用いることもできる。 As the conductivity meter (5), one that is usually used for measuring the conductivity (conductivity) of liquid can be used, and the pH (hydrogen ion concentration) measurement can be used to adjust the concentration of various cleaning solutions. It is also possible to use one having multiple functions such as side by side.

希釈洗浄液調製装置(6)は、液体攪拌機(6a)を備えた希釈槽(6b)から構成される。
液体攪拌機(6a)には、液体の混同攪拌に通常用いられているものが使用でき、攪拌翼がプロペラとして、底面から設置されているものが好ましい。また、攪拌翼は、1個用いても複数個用いてもよい。
希釈槽(6b)としては、従来公知のものが使用でき、その形状は特に制限されず、円筒状でも、直方体状でもよい。その材質も特に限定されず、ステンレススチール製のものが好適に使用できる。希釈槽の容量は、洗浄液の用途、使用量等に応じて種々変更が可能である。
希釈槽(6b)には、液体移送管路(4)から高濃度液が供給され、給水装置(3)から給水されるように配管され、また、希釈槽(6b)で調製された希釈液が排出ポンプ(6c)から、洗浄配管へ送り出されるよう配管される。
The diluted cleaning liquid preparation device (6) is composed of a dilution tank (6b) equipped with a liquid stirrer (6a).
As the liquid agitator (6a), those usually used for mixing and agitating liquids can be used, and those having a stirring blade installed from the bottom as a propeller are preferable. One stirring blade or a plurality of stirring blades may be used.
A conventionally well-known thing can be used as a dilution tank (6b), The shape in particular is not restrict | limited, A cylindrical shape or a rectangular parallelepiped shape may be sufficient. The material is not particularly limited, and those made of stainless steel can be suitably used. The capacity of the dilution tank can be variously changed according to the use and usage amount of the cleaning liquid.
The dilution tank (6b) is supplied with a high-concentration liquid from the liquid transfer pipe (4) and supplied with water from the water supply device (3), and is also prepared in the dilution tank (6b). Is piped out from the discharge pump (6c) to the cleaning pipe.

希釈槽(6b)には、導電率計(5)が装備されるが、特にCIP洗浄では、洗浄液の濃度管理上、特に重要であり、同時に液面センサー(6c)や温度計が装備されることが好ましい。これらのセンサーは、制御装置(7)に繋がっており、それらの測定情報に基づいて、制御装置(7)による供給等の指示が可能となる。 The diluting tank (6b) is equipped with a conductivity meter (5). Particularly in CIP cleaning, it is particularly important for the concentration management of the cleaning solution, and at the same time, a liquid level sensor (6c) and a thermometer are equipped. It is preferable. These sensors are connected to the control device (7), and based on the measurement information, instructions such as supply by the control device (7) can be made.

制御装置(7)は、導電率計(5)で計測された導電率に基づいて、液体移送管路(4)に高濃度液の供給の指示〔高濃度投入弁(4a)および排出ポンプ(4b)のオン・オフの指示〕もしくは給水装置(3)に給水の指示を出す〔すなわち、希釈液の導電率を測定して濃度が薄ければ、高濃度液の供給の指示を出し、一方、濃度が濃ければ、給水装置(3)に給水の指示を出す〕場合もあるが、特に、CIP洗浄では、経時的に洗浄液の濃度が薄くなる傾向がある。この制御装置は、コンピューターで制御されるシステムを用いて制御される。制御装置(7)には、通常測定機能も内蔵されるが、導電率計測機能(装置)は別装置でもよい。 Based on the conductivity measured by the conductivity meter (5), the control device (7) instructs the liquid transfer line (4) to supply a high-concentration liquid [high-concentration input valve (4a) and discharge pump ( 4b) ON / OFF instruction] or a water supply instruction to the water supply device (3) [that is, if the conductivity of the diluted solution is measured and the concentration is low, an instruction to supply a high concentration liquid is issued. If the concentration is high, the water supply device (3) is instructed to supply water.] In particular, in CIP cleaning, the concentration of the cleaning liquid tends to decrease with time. This controller is controlled using a computer controlled system. The control device (7) also includes a normal measurement function, but the conductivity measurement function (device) may be a separate device.

また、制御装置(7)は、希釈槽(6b)に設けられた液面センサー(6c)で計側された液量と導電率計(5)で計測された伝導率に基づいて、液体移送管(4)もしくは、給水装置(3)に供給指示を出すことができる。制御装置(7)は、高濃度液の供給もしくは、給水の指示を出すと共に、液体攪拌機(6a)のオン・オフの指示を出し、また、前述のように、粉体攪拌機(1a)、粉体投入弁(SGC)および液体攪拌機(2a)のオン・オフの指示を出す。   Further, the control device (7) transfers the liquid based on the liquid amount measured by the liquid level sensor (6c) provided in the dilution tank (6b) and the conductivity measured by the conductivity meter (5). A supply instruction can be issued to the pipe (4) or the water supply device (3). The control device (7) issues an instruction to supply or supply high-concentration liquid and also to turn on / off the liquid agitator (6a). As described above, the powder agitator (1a), powder An instruction to turn on and off the body charging valve (SGC) and the liquid agitator (2a) is issued.

希釈洗浄液調製装置(6)の希釈液(6b)で調整された希釈液は、導電率計(5)で導電率を計測し、制御装置(7)による指示に従って、規定の範囲内の導電率に達するまで濃度調整が行われる。所定の範囲内の導電率に調整された希釈液は、希釈洗浄液調製装置(6)の排出ポンプ(6c)から、洗浄配管へ送り出され、その使用(対象物の洗浄)に供される。   For the diluted solution prepared by the diluted solution (6b) of the diluted cleaning solution preparation device (6), the conductivity is measured by the conductivity meter (5), and the conductivity within the specified range is determined according to the instruction by the control device (7). The density is adjusted until the value is reached. The diluted solution adjusted to have a conductivity within a predetermined range is sent from the discharge pump (6c) of the diluted cleaning solution preparation device (6) to the cleaning pipe and used for use (cleaning of the object).

次に、本発明に係る洗浄液の自動濃度管理装置の使用方法(濃度管理方法)を説明する。洗浄液の調製は、基本的には、給水装置から溶解用水を溶解槽に入れ粉体供給装置から粉体洗浄剤を供給して溶解させて高濃度液を調製し、次いで高濃度液を希釈槽に移送して希釈すると共に洗浄液を測定して洗浄液の濃度調整を行う(すなわち導電率を計測しながら、自動的に水を追加し、所定の導電率になるよう希釈する)。また、当然、同じ仕組みでCIP洗浄に伴う複数回洗浄(アルカリ洗い→水洗→酸洗い→水洗 )の水洗工程にも応用することができる。   Next, a usage method (concentration management method) of the automatic concentration management apparatus for cleaning liquid according to the present invention will be described. The cleaning liquid is basically prepared by putting dissolving water from a water supply device into a dissolution tank, supplying a powder cleaning agent from a powder supply device and dissolving it, preparing a high concentration liquid, and then diluting the high concentration liquid. Then, the concentration of the cleaning solution is adjusted by adjusting the concentration of the cleaning solution (that is, while measuring the conductivity, water is automatically added to dilute to a predetermined conductivity). Of course, the same mechanism can be applied to a water washing process of multiple times (alkali washing → water washing → acid washing → water washing) associated with CIP cleaning.

本発明に係る方法の各ステップを具体的に説明すると。次の通りである。
〔1〕高濃度液調製工程
(I−1)先ず、スタートスイッチを手動でオンにし、粉体攪拌機(1a)を始動させ、粉体投入弁(スライドゲートバルブ:SGB)を開いて、粉体供給装置(1)のホッパー(1b)から、粉体洗浄剤(A)を溶解槽(2b)に投入する。制御装置(7)で指示された量の粉体洗浄剤(A)が投入されると、粉体攪拌機(1a)を停止し、粉体投入弁(SGB)を閉じる。粉体洗剤(A)は、一括投入しても、分割して投入してもよいが、分割して投入するのが好ましい。
The steps of the method according to the present invention will be specifically described. It is as follows.
[1] High concentration liquid preparation step (I-1) First, the start switch is manually turned on, the powder agitator (1a) is started, the powder injection valve (slide gate valve: SGB) is opened, and the powder From the hopper (1b) of the supply device (1), the powder cleaning agent (A) is charged into the dissolution tank (2b). When the amount of the powder cleaning agent (A) instructed by the control device (7) is charged, the powder agitator (1a) is stopped and the powder charging valve (SGB) is closed. The powder detergent (A) may be charged all at once or dividedly, but it is preferable to add it separately.

〔I−2〕次いで、溶解槽(2b)に水投入弁を開いて給水装置(3)から水を投入し、液体攪拌機(2a)を始動させ、粉体洗浄剤(A)を水もしくは希釈洗浄液に溶解させて、高濃度液(B)を調製する。制御装置(7)で指示された時間だけ攪拌した後に液体攪拌機(2a)を停止し、水投入弁を閉じる。
高濃度液(B)の濃度は洗浄剤の種類や用途に応じて変えられるが、通常は5〜30%、好ましくは、10〜20%である。
[I-2] Next, the water introduction valve is opened in the dissolution tank (2b), water is introduced from the water supply device (3), the liquid agitator (2a) is started, and the powder detergent (A) is diluted with water or diluted. Dissolve in a cleaning solution to prepare a high concentration solution (B). After stirring for the time specified by the control device (7), the liquid agitator (2a) is stopped and the water supply valve is closed.
Although the density | concentration of a high concentration liquid (B) can be changed according to the kind and use of a cleaning agent, it is 5-30% normally, Preferably, it is 10-20%.

(II)希釈洗浄液調製工程
(II‐1)工程(I)に続いて、導電率計から、下限レベル信号が出されたときに、液体攪拌機(6a)を始動させ、高濃度液投入弁(4a)を開き、排出ポンプ(4b)を作動させて液体移送管路(4)から高濃度液(B)を希釈槽(6b)に投入し、高濃度液(B)の全量が投入されると、液体攪拌機(6a)および排出ポンプ(4a)を停止し、高濃度液投入弁(4a)を閉じる。
水投入弁を開いて、溶解槽に一定量の水(約2Kg)を投入し、再び、排出ポンプを作動させて、希釈液へ投入する(すすぎ作業)。
(II) Diluted cleaning liquid preparation step (II-1) Subsequent to step (I), when the lower limit level signal is output from the conductivity meter, the liquid stirrer (6a) is started and the high concentration liquid injection valve ( 4a) is opened, the discharge pump (4b) is operated, the high-concentration liquid (B) is introduced into the dilution tank (6b) from the liquid transfer line (4), and the entire amount of the high-concentration liquid (B) is introduced. Then, the liquid agitator (6a) and the discharge pump (4a) are stopped, and the high-concentration liquid introduction valve (4a) is closed.
Open the water supply valve, supply a certain amount of water (about 2 kg) to the dissolution tank, operate the discharge pump again, and supply it to the diluent (rinse operation).

(II‐2)かくして調製された希釈洗浄液(C)の導電率を導電率計(5)で計測する。その導電率が制御装置(7)で指示された範囲内であれば、希釈洗浄液調製は、完了し、その範囲外である場合は、計測された導電率に基づいて、制御装置(7)から、液体移送管路(4)もしくは給水装置(3)に供給の指示が出され、上記範囲内の導電率に達すると供給が停止され、希釈洗浄液(C)の濃度が自動的に調製される。
希釈液洗浄液(C)の濃度は洗浄剤の種類や用途に応じて変えられるが、通常0.5〜3%、好ましくは、1〜%である。また、希釈洗浄液(C)の導電率の範囲は、洗浄剤の種類や用途によって種々異なるが、一般には、10〜100mS/cm(ミリジーメンス毎センチメートル)、好ましくは、30〜60mS/cmである。
(II-2) The conductivity of the diluted cleaning solution (C) thus prepared is measured with a conductivity meter (5). If the electrical conductivity is within the range indicated by the control device (7), the diluted cleaning liquid preparation is completed. If the electrical conductivity is out of the range, the control device (7) is used based on the measured electrical conductivity. The liquid transfer pipe (4) or the water supply device (3) is instructed to supply, and when the electric conductivity within the above range is reached, the supply is stopped and the concentration of the diluted cleaning liquid (C) is automatically adjusted. .
Although the density | concentration of a dilution liquid washing | cleaning liquid (C) can be changed according to the kind and use of a cleaning agent, it is 0.5 to 3% normally, Preferably, it is 1 to%. The range of the conductivity of the diluted cleaning liquid (C) varies depending on the type and application of the cleaning agent, but is generally 10 to 100 mS / cm (milli Siemens per centimeter), preferably 30 to 60 mS / cm. is there.

また、本発明に係る洗浄液の自動濃度管理装置を複数組(2セットまたはそれ以上)用意して、2種またはそれ以上の、異なる洗浄液(希釈洗浄剤)(C)、(C’)等、たとえば、アルカリ洗浄液と酸洗浄液を調製し、これらの洗浄液を希釈槽(6b)、(6b’)等から排出ポンプ(6c)、(6c’)等を経て洗浄配管へ送り出されるよう、配管し、各洗浄液(C)、(C’)等を使用(対象物の洗浄、たとえばCIP洗浄)に供することもできる。複数組の自動濃度管理装置を用いる場合、制御装置(7)は、それぞれの装置に個別に設けてもよいが、各組に共通した単一の制御装置(7)を用いて洗浄液(C)(C’)等の全体の自動濃度管理を行うことができる。 Also, multiple sets (two sets or more) of cleaning liquid automatic concentration management devices according to the present invention are prepared, and two or more different cleaning liquids (diluted cleaning agents) (C), (C ′), etc. For example, an alkali cleaning liquid and an acid cleaning liquid are prepared, and these cleaning liquids are piped so as to be sent from the dilution tanks (6b), (6b ′) etc. to the cleaning pipes via the discharge pumps (6c), (6c ′), etc. Each cleaning liquid (C), (C ′), etc. can be used (cleaning of an object, for example, CIP cleaning). In the case of using a plurality of sets of automatic concentration management devices, the control device (7) may be individually provided in each device, but the cleaning liquid (C) using a single control device (7) common to each set. The whole automatic density management such as (C ′) can be performed.

本発明に係る洗浄液の自動濃度管理装置は、これらの操作を自動的にかつ連続的に行えるよう、希釈洗浄液を所定の濃度に調整するために導電率測定による濃度を検出しつつ、高濃度液の供給量を制限して希釈槽に供給するように作動するが、希釈洗浄液濃度の検出手段に使用する導電率計による濃度の検出原理は、導電率が洗浄剤の濃度により異なることに基づいている。導電率と洗浄剤の濃度との関係は、洗浄剤の濃度との関係を求めておき、導電率から粉体洗浄剤の濃度を求める。この関係を制御装置にインプットしておき、また、この誘電率は洗浄液の濃度によって異なる。
洗浄液の温度が高いほど、濃度変化に対する伝導率の変化が大きい。これは、洗浄温度が高い方が、導電率による濃度の検出感度が高く、濃度の微小差も導電率の変化として、より容易に検出できることを示している。これは、洗浄剤の濃度を精度良く調整するために必要な条件である。
The automatic concentration management apparatus for cleaning liquid according to the present invention detects the concentration by conductivity measurement in order to adjust the diluted cleaning liquid to a predetermined concentration so that these operations can be performed automatically and continuously. However, the principle of concentration detection by the conductivity meter used for the diluted cleaning solution concentration detection means is based on the fact that the conductivity varies depending on the concentration of the cleaning agent. Yes. As for the relationship between the conductivity and the concentration of the cleaning agent, the relationship between the concentration of the cleaning agent is obtained, and the concentration of the powder cleaning agent is obtained from the conductivity. This relationship is input to the control device, and the dielectric constant varies depending on the concentration of the cleaning liquid.
The higher the temperature of the cleaning solution, the greater the change in conductivity with respect to the concentration change. This indicates that the higher the cleaning temperature, the higher the sensitivity for detecting the concentration due to the conductivity, and the more easily the minute difference in concentration can be detected as a change in conductivity. This is a necessary condition for accurately adjusting the concentration of the cleaning agent.

導電率の温度検出感度を高くするためには、洗浄液温度を高くすることが必要で、溶解用水を加温するか、洗浄液を加温するなど、洗浄液温度を適当な温度範囲(好ましくは20〜70℃)に保つようにする。このようにして、洗浄液温度の微小差を検出できる手段を講じ、所定の洗浄剤の濃度になるように粉体洗浄剤や水の供給量を制御することにより、濃度精度の良い洗浄液を調製することができる。 In order to increase the temperature detection sensitivity of conductivity, it is necessary to increase the temperature of the cleaning solution. The temperature of the cleaning solution is set to an appropriate temperature range (preferably 20 to 20), such as heating the water for dissolution or heating the cleaning solution. 70 ° C). In this way, a means for detecting a minute difference in the temperature of the cleaning liquid is taken, and a cleaning liquid with a high concentration accuracy is prepared by controlling the supply amount of the powder cleaning agent and water so that the concentration of the predetermined cleaning agent is reached. be able to.

本発明で用いられる粉体洗剤(A)としては、従来公知の粉体洗浄剤が用いられ、洗浄液製作時に粉体であればよい。種類としては、中性、アニオン性、カチオン性、および両性の界面活性剤をはじめ、水酸化ナトリウムやクエン酸などの酸性やアルカリ性物質といった幅広い洗浄力をもった物資が使用できる。
特に、界面活性剤とキレート剤、および、水酸化ナトリウム等のアルカリビルダーとの混合液を用いることが好ましい。
粉体は粉末状もしくは粒状を意味し、粉体供給装置でフィードできれば、粒度についても、特に限定はない。また、溶解度についても、特に、制限はない。
As a powder detergent (A) used by this invention, a conventionally well-known powder cleaning agent is used and should just be a powder at the time of cleaning liquid manufacture. As types, neutral, anionic, cationic, and amphoteric surfactants as well as materials having a wide range of detergency such as acidic and alkaline substances such as sodium hydroxide and citric acid can be used.
In particular, it is preferable to use a mixed solution of a surfactant, a chelating agent, and an alkali builder such as sodium hydroxide.
The powder means powdery or granular, and the particle size is not particularly limited as long as it can be fed by a powder supply device. There is no particular limitation on the solubility.

実施のフローチャート
本発明に係る洗浄液の自動濃度管理測定装置およびその使用方法を実施例により解明するが、本発明はこれに限定されるものでは無く、システムとしての可能な運用方法の総てにわたるものである。
Flowchart of Implementation The cleaning liquid automatic concentration management measuring device and its usage method according to the present invention will be elucidated by examples, but the present invention is not limited to this, and covers all possible operation methods as a system. It is.

ステップ1
制御装置(7)の指示に従って、電導モーター(M1)で粉体攪拌機(1a)を始動させ、粉体投入弁(SGB)を開いて、粉体供給装置(1)のホッパー(1b)から粉体洗浄剤(A)を、溶解槽(2b)に連続的に投入する。所定量〔制御装置(7)で指示された量〕の粉体洗浄剤(A)が投入されると、粉体攪拌機(1a)を停止し、
粉体投入弁(SGB)を閉じる。
Step 1
In accordance with the instruction of the control device (7), the powder agitator (1a) is started by the electric motor (M1), the powder charging valve (SGB) is opened, and the powder is fed from the hopper (1b) of the powder supply device (1). The body cleaning agent (A) is continuously charged into the dissolution tank (2b). When a predetermined amount (instructed by the control device (7)) of the powder cleaning agent (A) is charged, the powder agitator (1a) is stopped,
Close the powder injection valve (SGB).

ステップ2
次いで、高濃度液調製装置(2)において、溶解槽(2b)に、水投入弁を開いて給水装置(3)から所定量の水を投入し、粉体洗剤(A)を水に溶解させて、高濃度液(B)を調製する。
Step 2
Next, in the high-concentration liquid preparation apparatus (2), a predetermined amount of water is introduced from the water supply apparatus (3) to the dissolution tank (2b) and the powder detergent (A) is dissolved in water. To prepare a high-concentration liquid (B).

ステップ3
一方、希釈洗浄液調製装置(6)において、電動モーター(M3)で、液体攪拌機(6a)を始動させ、高濃度液投入弁(4a)を開き排出ポンプ(4b)を作動させて液体移送管路(4)から、高濃度液(B)を希釈槽(6b)に投入し、希釈洗浄液(C)を調整する。高濃度液全量を移送後、搬出ポンプ(4b)を停止し、高濃度投入弁(4a)および水投入弁を閉じる。
Step 3
On the other hand, in the diluted cleaning liquid preparation apparatus (6), the liquid stirrer (6a) is started by the electric motor (M3), the high concentration liquid inlet valve (4a) is opened, and the discharge pump (4b) is operated to supply the liquid transfer line. From (4), the high-concentration liquid (B) is charged into the dilution tank (6b) to adjust the diluted cleaning liquid (C). After transferring the entire high-concentration liquid, the carry-out pump (4b) is stopped, and the high-concentration injection valve (4a) and the water injection valve are closed.

ステップ4
調整された希釈洗浄液(C)の導電率を導電率計(5)で測定し、その導電率が所定の範囲内〔制御装置(7)で指示された範囲内〕であれば、希釈洗浄液調製は完了する。その範囲外にある場合は、計測された導電率に基づいて、制御装置(7)から液体移送管路(4)もしくは給水装置(3)に供給の指示が出され、上記範囲内の導電率に達すると供給が停止され、希釈洗浄液(C)の濃度が、自動的に調整される。
導電率は希釈槽に入れられたセンサーを通じて導電率計測装置で(4)で想定され、信号が制御装置(5)に送られ、濃度が感知される。この場合、目標の洗浄液濃度調整は、たとえば、目標よりも若干高めの濃度(2.0%)に設定され、それを補充給水しながら、目標の1.5%に調製するというフィードバックによる調整が有効である。
Step 4
If the conductivity of the adjusted diluted cleaning solution (C) is measured with a conductivity meter (5) and the conductivity is within a predetermined range [within the range specified by the control device (7)], the diluted cleaning solution is prepared. Is completed. When it is out of the range, based on the measured conductivity, the controller (7) issues a supply instruction to the liquid transfer pipe (4) or the water supply device (3), and the conductivity within the above range. Is reached, the supply is stopped, and the concentration of the diluted cleaning solution (C) is automatically adjusted.
The conductivity is assumed in (4) by the conductivity measuring device through a sensor placed in the dilution tank, a signal is sent to the control device (5), and the concentration is sensed. In this case, for example, the target cleaning liquid concentration adjustment is set to a slightly higher concentration (2.0%) than the target, and the adjustment by feedback that the target cleaning liquid concentration is adjusted to 1.5% of the target while replenishing water is supplied. It is valid.

ステップ5
かくして調製された自動濃度管理されたアルカリ洗浄液(希釈洗浄液)(C)と粉体洗浄液(A)を用いて、上記と同様にして調製された自動濃度管理された酸洗浄液(希釈洗浄液)(C’)とを、それぞれ、希釈槽(6b)および(6b’)から排出ポンプ(6C)および(6C’)を始動させて、連続的に洗浄配管に送り出し、両洗浄液(C)および(C’)をその使用(CIP洗浄)に供した希釈洗浄液(C)、(C’)を洗浄配管へ送り出して、希釈槽(6b’)の液面が所定のレベル(L)以下になった段階で、制御装置(7)より、高濃度液(B)および水の供給の指示が出され、ステップ1の操作が繰り返されて、次いでステップ2に移る。
Step 5
Using the thus-prepared alkali cleaning liquid (diluted cleaning liquid) (C) and powder cleaning liquid (A), the automatic concentration-controlled acid cleaning liquid (diluted cleaning liquid) (C) prepared in the same manner as described above. ') From the dilution tanks (6b) and (6b'), respectively, by starting the discharge pumps (6C) and (6C ') and continuously feeding them to the cleaning pipes, both cleaning liquids (C) and (C' ) Was used for its use (CIP cleaning), and the diluted cleaning liquids (C) and (C ′) were sent to the cleaning pipe, and the liquid level in the dilution tank (6b ′) was below a predetermined level (L). The control device (7) issues an instruction to supply the high-concentration liquid (B) and water, the operation of step 1 is repeated, and then the operation proceeds to step 2.

ステップ6
また、高濃度液(B)が、液体移送管(4)へ移送された溶解槽(2b)の液面が所定のレベル(L)以下になった段階で、制御装置(7)より、粉体洗浄剤(A)および水の供給の指示が出され、ステップ1〜2の操作が繰り返され、ステップ3以降の操作に引き継ぐ。
Step 6
In addition, when the liquid level of the dissolution tank (2b) transferred to the liquid transfer pipe (4) is less than or equal to a predetermined level (L), the high concentration liquid (B) is powdered by the control device (7). An instruction to supply the body cleaning agent (A) and water is issued, the operations in steps 1 and 2 are repeated, and the operations in step 3 and subsequent steps are taken over.

本発明に係る洗浄液の自動濃度装置および、その使用方法は、粉体洗浄剤を用いた洗浄液を使用するあらゆる工場、研究所等で種々の対象物の洗浄に好適に用いられる。本発明は、自動化された(コンピューター制御された)洗浄配管を経て対象物の洗浄を行う用途、特に食品産業を中心とするCIP洗浄において、水酸化ナトリウムの高濃度溶液(25%程度)から、自動的に希釈洗浄液(0.5〜3%)を他の洗浄剤との混合調製できることは、生産性、信頼性の向上に大きく貢献するものと思われる。   The automatic concentration apparatus for cleaning liquid and the method for using the same according to the present invention are suitably used for cleaning various objects in any factory or laboratory that uses a cleaning liquid using a powder cleaning agent. The present invention is an application for cleaning an object through an automated (computer-controlled) cleaning pipe, particularly in CIP cleaning mainly in the food industry, from a high concentration solution (about 25%) of sodium hydroxide, The ability to automatically mix and prepare a diluted cleaning solution (0.5 to 3%) with other cleaning agents seems to greatly contribute to the improvement of productivity and reliability.

本発明の洗浄液の自動濃度管理装置の実施例を模式的に示すフロー図である。It is a flowchart which shows typically the Example of the automatic density | concentration management apparatus of the washing | cleaning liquid of this invention.

符号の説明Explanation of symbols

(A)粉体洗剤
(B)高濃度液
(C)希釈洗浄液
(1)粉体供給装置
(2)高濃度液調製装置
(3)給水装置
(4)液体移送管路
(5)伝導率計
(6)希釈洗浄液調製装置
(7)制御装置
(A) Powder detergent (B) High concentration liquid (C) Diluted cleaning liquid (1) Powder supply device (2) High concentration liquid preparation device (3) Water supply device (4) Liquid transfer line (5) Conductivity meter (6) Dilution cleaning liquid preparation device (7) Control device

Claims (4)

粉体攪拌機(1a)とホッパー(1b)を備え、粉体洗浄剤(A)を供給する粉体供給装置(1)、液体攪拌機(2a)を備えた溶解槽(2)から構成され、ホッパー(1b)の下方に設けられた、高濃度液調製装置(2)、給水装置(3)、高濃度液を移送する液体移送管路(4)、導電率計(5)、液体攪拌機(6a)を備えた希釈槽(6b)から構成される、希釈洗浄液調製装置(6)、および、導電率計で計測された導電率に基づいて、液体移送管路(4)もしくは給水装置(3)に供給指示を出す、制御装置(7)から構成される、洗浄液の自動濃度管理装置。 A hopper comprising a powder agitator (1a) and a hopper (1b), a powder supply device (1) for supplying a powder cleaning agent (A), and a dissolution tank (2) having a liquid agitator (2a). (1b), a high concentration liquid preparation device (2), a water supply device (3), a liquid transfer pipe (4) for transferring the high concentration liquid, a conductivity meter (5), a liquid stirrer (6a) ) And a liquid transfer line (4) or a water supply device (3) based on the conductivity measured by the conductivity meter. An automatic concentration management device for cleaning liquid, comprising a control device (7) for issuing a supply instruction. 希釈洗浄液調製装置(6)が液面センサーを含む流量計(6c)を備え、制御装置(7)が、流量計(6c)で計測された液量と導電率計(5)で、計測された導電率に基づいて、液体移送管路(4)もしくは、給水装置(3)に供給指示を出す、請求項1記載の洗浄液の自動濃度管理装置。 The diluted cleaning liquid preparation device (6) includes a flow meter (6c) including a liquid level sensor, and the control device (7) is measured by the liquid amount measured by the flow meter (6c) and the conductivity meter (5). The cleaning liquid automatic concentration management device according to claim 1, wherein a supply instruction is issued to the liquid transfer pipe (4) or the water supply device (3) based on the conductivity. 請求項1または2に記載の洗浄液の自動濃度管理装置を用いて、粉体攪拌機(1a)を作動させて、粉体供給装置(1)のホッパー(1b)から、粉体洗浄剤(A)を溶解槽(2b)に投入すると共に、給水装置(3)からの水もしくは希釈槽(6b)からの希釈洗浄液を溶解槽(2b)に投入し、液体攪拌機(6a)を始動させ、5〜30%質量%濃度の高濃度液(B)を調製し、高濃度液(B)を水で希釈して、0.5〜3質量%濃度の希釈洗浄液(C)を2段階または、複数回で単独あるいは、他の粉体洗剤と混合調製し、導電率計(5)で希釈洗浄液の導電率を計測し、計測された導電率に基づいて、制御装置(7)から、液体移送管路(4)もしくは給水装置(3)に給水指示を出すことによって、希釈洗浄剤(C)の濃度をフィードバックシステムにより、自動的に調整することを特徴とする、洗浄液の自動濃度管理装置の使用方法、ならびにCIP洗浄に伴うアルカリ洗浄、水でのすすぎ、酸での洗浄、水でのすすぎ工程を取り入れた上記洗浄液の自動濃度管理装置の使用方法。 The powder cleaning agent (A) is operated from the hopper (1b) of the powder supply device (1) by operating the powder agitator (1a) using the cleaning liquid automatic concentration management device according to claim 1 or 2. Is added to the dissolution tank (2b), and water from the water supply device (3) or diluted cleaning liquid from the dilution tank (6b) is added to the dissolution tank (2b), and the liquid agitator (6a) is started. A high concentration liquid (B) having a concentration of 30% by mass is prepared, the high concentration liquid (B) is diluted with water, and a diluted washing liquid (C) having a concentration of 0.5 to 3% by mass is prepared in two steps or a plurality of times. Or by mixing with other powder detergents, and measuring the conductivity of the diluted cleaning solution with a conductivity meter (5). Based on the measured conductivity, the liquid transfer line from the control device (7) (4) Or by giving a water supply instruction to the water supply device (3), the concentration of the diluted cleaning agent (C) is reduced. Incorporates the use of an automatic concentration control device for cleaning liquid, which is automatically adjusted by the back-back system, and alkali cleaning, water rinsing, acid rinsing, and water rinsing steps associated with CIP cleaning And a method for using the cleaning liquid automatic concentration control device. 上記、請求項1、請求項2および請求項3における、フィードバックシステムを構成する「導電率計(5)」をペーハー測定器、比重測定器、粘性測定器、屈折率測定器、透明度測定器、色測定器、圧力計などの「液体センサー(5)」に置き換え、請求項2および請求項3に記載の「計測された導電率」を「計測された液体センサーの数値」の置き換えた請求項1および請求項2に規定する規定する洗浄液の自動濃度管理装置。ならびに請求項3に規定する自動濃度管理装置の使用方法。 In claim 1, claim 2, and claim 3, the "conductivity meter (5)" constituting the feedback system is a pH measuring device, a specific gravity measuring device, a viscosity measuring device, a refractive index measuring device, a transparency measuring device, Claims replaced with "Liquid sensor (5)" such as a color measuring device, pressure gauge, etc., and "Measured conductivity" according to claim 2 and Claim 3 replaced with "Measured liquid sensor value" An automatic concentration management device for a cleaning liquid as defined in claim 1 and claim 2. And a method of using the automatic concentration management device as defined in claim 3.
JP2007173711A 2007-07-02 2007-07-02 Automatic concentration control apparatus for cleaning liquid and method for using the same Pending JP2009013211A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011153867A (en) * 2010-01-26 2011-08-11 Sysmex Corp Reagent preparation device
CN113201741A (en) * 2021-05-06 2021-08-03 东风汽车车轮随州有限公司 Bright aluminum alloy wheel acid pickling mixed flow production process

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011153867A (en) * 2010-01-26 2011-08-11 Sysmex Corp Reagent preparation device
CN113201741A (en) * 2021-05-06 2021-08-03 东风汽车车轮随州有限公司 Bright aluminum alloy wheel acid pickling mixed flow production process
CN113201741B (en) * 2021-05-06 2022-11-15 东风汽车车轮随州有限公司 Bright aluminum alloy wheel acid pickling mixed flow production process

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