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JP7050505B2 - Nori net acid treatment ship - Google Patents
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JP7050505B2 - Nori net acid treatment ship - Google Patents

Nori net acid treatment ship Download PDF

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JP7050505B2
JP7050505B2 JP2018013437A JP2018013437A JP7050505B2 JP 7050505 B2 JP7050505 B2 JP 7050505B2 JP 2018013437 A JP2018013437 A JP 2018013437A JP 2018013437 A JP2018013437 A JP 2018013437A JP 7050505 B2 JP7050505 B2 JP 7050505B2
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acid treatment
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stock solution
discharge hole
tubular member
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哲也 山本
哲也 久保田
啓明 藤本
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Daiichi Seimo Co Ltd
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Description

本発明は、養殖中に海苔網に付着する珪藻類や赤腐れ菌などの菌類を酸処理剤(液)で酸処理する海苔網の酸処理船に関する。 The present invention relates to an acid treatment vessel for a seaweed net that acid-treats fungi such as diatoms and red rot bacteria that adhere to the seaweed net during cultivation with an acid treatment agent (liquid).

従来より、海苔養殖場において海面部分に展張されている海苔網に付着する珪藻類や赤腐れ菌などの菌類をクエン酸、リンゴ酸などの有機酸等の組み合わせからなる配合組成の酸処理剤によつて効果的に酸処理を施す海苔網の酸処理船は数多くの型式、構造のものが知られている。 Conventionally, fungi such as diatoms and red rot bacteria adhering to the seaweed net spread on the sea surface in the seaweed farm have been used as an acid treatment agent having a composition composed of a combination of organic acids such as citric acid and malic acid. Therefore, many types and structures of acid treatment vessels for seaweed nets that effectively perform acid treatment are known.

このような海苔網の酸処理船としては、一般に、一定のpH値の酸処理液に海苔網を浸漬することにより、海苔の成長を早め、しかも、各海苔網の成長を一定状態として、良質の海苔を収穫することができる海苔網の酸処理船である。
この海苔網の酸処理船は、船内に、一定の容量の酸処理槽と、海苔網の引上装置と、同酸処理槽内に酸原液を補給する酸原液補給装置と、酸処理槽内の酸処理液のpH値を検出し、その検出値に基づいて前記補給装置を作動させて、酸処理液を一定のpH値、例えばpH2.0前後に保持する制御部とより構成されたものである(例えば、特許文献1参照)。
In such an acid treatment vessel for seaweed nets, generally, by immersing the seaweed nets in an acid treatment liquid having a constant pH value, the growth of the seaweed is accelerated, and the growth of each seaweed net is kept constant, so that the quality is good. It is an acid treatment ship of seaweed net that can harvest seaweed.
This acid treatment ship for seaweed net has a certain capacity acid treatment tank, a seaweed net pulling device, an acid stock solution replenishment device for replenishing the acid stock solution in the same acid treatment tank, and an acid treatment tank. It is composed of a control unit that detects the pH value of the acid-treated solution of the above and operates the replenishing device based on the detected value to keep the acid-treated solution at a constant pH value, for example, around pH 2.0. (See, for example, Patent Document 1).

また、小型の海苔網の酸処理船として、箱形船を用いた酸処理船が知られている。この小型の海苔網の酸処理船としては、例えば、
1) 海から海苔網を巻き上げるための海苔網巻上装置を設けた酸処理槽と、薬液を循環させるための薬液循環装置と、薬液循環装置で循環させる薬液の濃度を検出するための濃度検出装置とを有する海苔網酸処理船(例えば、特許文献2参照)、
2) 海苔養殖場に張られている海苔網を活性処理する活性処理剤が収容されている活性処理剤タンクと、前記活性処理剤と水とが混合された処理水が収容されて前記海苔網の活性処理が行われる処理槽と、前記活性処理剤タンクから前記処理槽へ供給パイプを介して前記活性処理剤を供給手段とを備えている海苔網活性処理剤の供給装置(例えば、特許文献3参照)
3) 酸処理液を所望のpH値に維持することが可能な箱型船として、酸処理液を貯留する酸処理槽と、該酸処理槽内に設けられ、海苔が付着した海苔網を巻き取る一対の巻取ロールとを備える箱型船であって、前記酸処理槽に設けられ、前記酸処理液のpHを検出するpHセンサと、前記巻取ロールに巻き取られる前記海苔網と干渉しない位置に設けられ、酸原液を吐出する原液吐出部と、前記pHセンサの検出値に基づいて前記原液吐出部に供給する前記酸原液の供給量を自動調節する原液供給装置とを備え、前記原液吐出部は、前記一対の巻取ロールの間に設けられ、前記酸処理液の液面に対峙するように前記酸処理槽の上方に設けられた棒状部材と、該棒状部材から前記酸処理液の液面に向かって垂下するシート部材と、該シート部材の両側に前記棒状部材に沿って設けられ、前記酸原液を前記シート部材に向かって吐出する複数の吐出孔が所定間隔で形成された管状部材とを備えることを特徴とする箱型船(例えば、特許文献4参照)、
4) 海苔網の酸処理において酸原液や所望濃度よりも高い濃度の酸処理液が海苔網に接触することを抑制するために、酸原液が希釈された酸処理液を貯留する酸処理槽と、該酸処理槽内に設けられ、海苔が付着した海苔網を巻き取る巻取ロールとを備える箱型船であって、該巻取ロールから離間すると共に垂下する可撓性シート及び該可撓性シートの表面に前記酸原液を吐出する酸原液吐出部を備えており、前記酸原液を前記可撓性シートの表面を流下させて前記酸処理槽に供給する酸原液供給部とを備え、前記酸原液供給部は、前記可撓性シートの下端が前記巻取ロールに近づくように前記酸処理槽が傾斜した場合に、前記酸処理液の液面において前記可撓性シートの下端よりも前記巻取ロールから遠い位置に前記酸原液を供給することを特徴とする箱型船(例えば、特許文献5参照)、
などが知られている。
Further, as an acid treatment ship for a small seaweed net, an acid treatment ship using a box-shaped ship is known. As an acid treatment ship for this small seaweed net, for example,
1) An acid treatment tank equipped with a seaweed net hoisting device for hoisting seaweed nets from the sea, a chemical liquid circulation device for circulating chemicals, and concentration detection for detecting the concentration of chemicals circulated by the chemical circulation device. A seaweed net acid treatment vessel having an apparatus (see, for example, Patent Document 2),
2) The nori net containing an active treatment agent tank containing an active treatment agent for activating the seaweed net stretched on the seaweed farm and treated water in which the active treatment agent and water are mixed. A seaweed net activation treatment agent supply device (for example, Patent Document) comprising a treatment tank in which the activation treatment of Nori seaweed is performed and a means for supplying the activation treatment agent from the activation treatment agent tank to the treatment tank via a supply pipe (for example, Patent Document). 3)
3) As a box-shaped ship capable of maintaining the acid-treated liquid at a desired pH value, an acid-treated tank for storing the acid-treated liquid and a seaweed net provided in the acid-treated tank to which seaweed adheres are wound. A box-shaped ship equipped with a pair of take-up rolls, which interferes with a pH sensor provided in the acid treatment tank to detect the pH of the acid treatment liquid and the seaweed net wound on the take-up roll. It is provided with a stock solution discharge unit that is provided at a position where the acid stock solution is not discharged, and a stock solution supply device that automatically adjusts the supply amount of the acid stock solution to be supplied to the stock solution discharge unit based on the detection value of the pH sensor. The undiluted solution discharge portion is provided between the pair of winding rolls, and has a rod-shaped member provided above the acid-treated tank so as to face the liquid surface of the acid-treated solution, and the acid-treated rod-shaped member. A sheet member that hangs down toward the liquid surface and a plurality of discharge holes that are provided along the rod-shaped member on both sides of the sheet member and discharge the acid stock solution toward the sheet member are formed at predetermined intervals. A box-shaped ship characterized by having a tubular member (see, for example, Patent Document 4),
4) With an acid treatment tank that stores the acid treatment solution in which the acid stock solution is diluted in order to prevent the acid stock solution and the acid treatment solution having a concentration higher than the desired concentration from coming into contact with the seaweed net in the acid treatment of the seaweed net. A box-shaped ship provided in the acid treatment tank and equipped with a take-up roll for winding up a seaweed net to which seaweed is attached, a flexible sheet that hangs away from the take-up roll and hangs down, and the flexible sheet. The surface of the sex sheet is provided with an acid stock solution discharge unit for discharging the acid stock solution, and the acid stock solution supply unit is provided with the acid stock solution flowing down the surface of the flexible sheet and supplied to the acid treatment tank. When the acid treatment tank is tilted so that the lower end of the flexible sheet approaches the take-up roll, the acid stock solution supply unit is more than the lower end of the flexible sheet at the liquid level of the acid treatment liquid. A box-shaped ship characterized by supplying the acid stock solution to a position far from the take-up roll (see, for example, Patent Document 5).
Etc. are known.

前記特許文献1~5の海苔網の酸処理船等では、一定容量の酸処理槽内の酸処理液のpH値を検出し、その検出値に基づいて供給装置のポンプ等を作動させて、処理槽内に酸処理液(酸原液等)を吐出孔を有する供給パイプや管状部材などを介して酸処理槽に供給して酸処理槽内の酸処理液を一定のpH値、通常、pH2.0前後に保持するものであった。
しかしながら、上記特許文献1~5に用いられている供給パイプや管状部材は、主に塩化ビニール製の水道管等を転用したものであるので、その内径が13mm以上と大きく、また、供給パイプや管状部材に形成される吐出孔の孔径も同じ大きさ、各吐出孔間の間隔(距離)も同じ間隔であった。そのため、供給ポンプから供給される酸原液等の一部が供給パイプや管状部材内に残存し、設定したpH値に低下しなかったりし、設定したpH値と実際の酸処理槽内のpH値との乖離が生じ、十分な酸処理が効率的に行えないという課題が生じている。
In the acid treatment ship or the like of the seaweed net of Patent Documents 1 to 5, the pH value of the acid treatment liquid in the acid treatment tank having a constant capacity is detected, and the pump or the like of the supply device is operated based on the detected value. An acid treatment liquid (acid stock solution, etc.) in the treatment tank is supplied to the acid treatment tank via a supply pipe or a tubular member having a discharge hole, and the acid treatment liquid in the acid treatment tank has a constant pH value, usually pH 2. It was held around 0.0.
However, since the supply pipes and tubular members used in the above Patent Documents 1 to 5 are mainly diverted from vinyl chloride water pipes and the like, their inner diameter is as large as 13 mm or more, and the supply pipes and the like. The hole diameters of the discharge holes formed in the tubular member were the same, and the distances (distances) between the discharge holes were also the same. Therefore, a part of the acid stock solution supplied from the supply pump may remain in the supply pipe or tubular member and may not drop to the set pH value, and the set pH value and the actual pH value in the acid treatment tank may be reached. There is a problem that sufficient acid treatment cannot be performed efficiently due to the deviation from the above.

また、上記特許文献4及び5の海苔網の酸処理船では、更に、酸原液をシート部材に向かって吐出する方式であるので、管状部材内の残存の他、表面積の大きいシート部材に酸原液の一部が付着などして残存するものとなるので、設定したpH値と実際の酸処理槽内のpH値との乖離が更に大きく、十分な酸処理が効率的に行えないという課題が生じている。 Further, in the acid treatment ship of the seaweed net of Patent Documents 4 and 5, since the acid stock solution is further discharged toward the sheet member, the acid stock solution remains in the tubular member and also on the sheet member having a large surface area. Since a part of the pH is left behind due to adhesion, the difference between the set pH value and the actual pH value in the acid treatment tank is even larger, and there is a problem that sufficient acid treatment cannot be performed efficiently. ing.

特開平5-95740号公報(特許請求の範囲、図1等)Japanese Patent Application Laid-Open No. 5-95740 (Claims, FIG. 1, etc.) 実用新案登録第3212304号公報(実用新案登録請求の範囲、図1等)Utility Model Registration No. 3212304 (Claims for Utility Model Registration, Figure 1, etc.) 実用新案登録第3210762号公報(実用新案登録請求の範囲、図1等)Utility Model Registration No. 3210762 (Claims for Utility Model Registration, Figure 1, etc.) 特許第6161016号公報(特許請求の範囲、図1,2等)Japanese Patent No. 6161016 (Claims, FIGS. 1, 2, etc.) 特許第6218984号公報(特許請求の範囲、図1~図4等)Japanese Patent No. 6218984 (Claims, FIGS. 1 to 4, etc.)

本発明は、前記従来の課題等について、これを解消しようとするものであり、養殖中に海苔網に付着する珪藻類や赤腐れ菌などの菌類を酸処理剤(液)で酸処理する海苔網の酸処理船において、設定したpH値と実際の酸処理槽内のpH値との乖離を最小限として、且つ、酸処理槽内の濃度ムラが生じないようにして、十分な酸処理を効率的に行える海苔網の酸処理船を提供することを目的とする。 The present invention is intended to solve the above-mentioned conventional problems, and is to treat nori such as diatoms and red rot bacteria adhering to the nori net during cultivation with an acid treatment agent (liquid). In the acid treatment ship of the net, sufficient acid treatment is performed by minimizing the deviation between the set pH value and the actual pH value in the acid treatment tank and preventing the concentration unevenness in the acid treatment tank from occurring. The purpose is to provide an acid treatment ship for seaweed nets that can be performed efficiently.

本発明者らは、前記従来の課題等について鋭意検討した結果、少なくとも、酸処理液を収容する酸処理槽と、該酸処理槽内に酸処理液の原液を供給する酸原液供給装置と、酸処理槽内の酸処理液のpH値を検出し、その検出値に基づいて前記酸原液供給装置を作動させて、酸処理液を一定のpH値に制御する制御部とを備えた海苔網の酸処理船であって、前記酸原液供給装置には、前記酸処理槽上の任意の位置に、酸原液を噴出する複数の吐出孔を有する有底筒状の管状部材を少なくとも1つ以上備えると共に、該管状部材の内径、吐出孔の数、吐出孔の孔径、最初の吐出孔の孔径に対して最後の吐出孔の孔径の比をそれぞれ特定の範囲とすることにより、上記海苔網の酸処理船が得られることを見い出し、本発明を完成するに至ったのである。 As a result of diligent studies on the above-mentioned conventional problems, the present inventors have at least an acid treatment tank for accommodating an acid treatment liquid, and an acid stock solution supply device for supplying a stock solution of the acid treatment liquid into the acid treatment tank. A seaweed net provided with a control unit that detects the pH value of the acid treatment liquid in the acid treatment tank, operates the acid stock solution supply device based on the detected value, and controls the acid treatment liquid to a constant pH value. In the acid treatment vessel of the above, the acid stock solution supply device is provided with at least one bottomed tubular tubular member having a plurality of discharge holes for ejecting the acid stock solution at an arbitrary position on the acid treatment tank. By setting the inner diameter of the tubular member, the number of discharge holes, the hole diameter of the discharge holes, and the ratio of the hole diameter of the last discharge hole to the hole diameter of the first discharge hole within a specific range, the seaweed net can be prepared. They found that an acid-treated ship could be obtained, and completed the present invention.

すなわち、次の(1)~(6)に存する。
(1) 少なくとも、酸処理液を収容する酸処理槽と、該酸処理槽内に酸処理液の原液を供給する酸原液供給装置と、前記酸処理槽内の酸処理液のpH値を検出し、その検出値に基づいて前記酸原液供給装置を作動させて、酸処理液を一定のpH値に制御する制御部とを備えた海苔網の酸処理船であって、前記酸原液供給装置には、前記酸処理槽上の任意の位置に、酸原液を噴出する複数の吐出孔を有する有底筒状の管状部材を少なくとも1つ以上備えると共に、該管状部材は内径が3~8mmであり、吐出孔の数が3~10個であり、該吐出孔の孔径が1.0~2.0mmであることを特徴とする海苔網の酸処理船。
(2) 前記管状部材の最初の吐出孔の孔径に対して最後の吐出孔の孔径の比が1.08~1.27倍となることを特徴とする上記(1)記載の海苔網の酸処理船。
(3) 前記管状部材の吐出孔の数(a)が4個以上の場合は、最初の吐出孔と2番目の吐出孔との間隔(X)と、最後の吐出孔の一つ前の吐出孔と最後の吐出孔の間隔が同じ(X=Xa-1,aは吐出孔の個数)であり、2番目の吐出孔(X)から最後の吐出孔の一つ前の吐出孔(Xa-1)の各間隔が同じ(X=X=…)であることを特徴とする上記(1)又は(2)記載の海苔網の酸処理船。
(4) 海苔網の酸処理船には、酸処理槽内に海苔網を巻き取る巻取ロールが設けられていることを特徴とする上記(1)~(3)のいずれか一つに記載の海苔網の酸処理船。
(5) 前記海苔網の酸処理船には、前記酸処理槽の中央部に懸架された支持部材と、該支持部材から前記酸処理槽の酸処理液に垂下するシート状部材とを有し、該シート状部材の片側又は両側に前記管状部材を備えたことを特徴とする上記(1)~(4)の何れか一つに記載の海苔網の酸処理船。
(6) 前記管状部材の各吐出孔には、視認性を有する可撓性チューブが取り付けられたことを特徴とする上記(1)~(5)の何れか一つに記載の海苔網の酸処理船。
That is, it exists in the following (1) to (6).
(1) At least, the acid treatment tank containing the acid treatment liquid, the acid stock solution supply device for supplying the stock solution of the acid treatment liquid into the acid treatment tank, and the pH value of the acid treatment liquid in the acid treatment tank are detected. The acid stock solution supply device is a seaweed net acid treatment ship equipped with a control unit that operates the acid stock solution supply device based on the detected value to control the acid treatment liquid to a constant pH value. Is provided with at least one bottomed tubular member having a plurality of discharge holes for ejecting the acid stock solution at an arbitrary position on the acid treatment tank, and the tubular member has an inner diameter of 3 to 8 mm. A seaweed net acid treatment vessel, characterized in that the number of discharge holes is 3 to 10, and the hole diameter of the discharge holes is 1.0 to 2.0 mm.
(2) The acid of the seaweed net according to (1) above, wherein the ratio of the hole diameter of the last discharge hole to the hole diameter of the first discharge hole of the tubular member is 1.08 to 1.27 times. Processing ship.
(3) When the number of discharge holes (a) of the tubular member is 4 or more, the distance between the first discharge hole and the second discharge hole (X 1 ) and one before the last discharge hole. The distance between the discharge hole and the last discharge hole is the same (X 1 = X a-1 , a is the number of discharge holes), and the second discharge hole (X 2 ) is discharged immediately before the last discharge hole. The acid-treated seaweed net according to (1) or (2) above, wherein the intervals between the holes (X a-1 ) are the same (X 2 = X 3 = ...).
(4) Described in any one of (1) to (3) above, wherein the nori net acid treatment vessel is provided with a winding roll for winding the nori net in the acid treatment tank. Nori seaweed net acid treatment ship.
(5) The acid treatment ship of the seaweed net has a support member suspended from the central portion of the acid treatment tank and a sheet-like member hanging from the support member to the acid treatment liquid of the acid treatment tank. The acid-treated seaweed net according to any one of (1) to (4) above, wherein the tubular member is provided on one side or both sides of the sheet-shaped member.
(6) The acid of the seaweed net according to any one of (1) to (5) above, wherein a flexible tube having visibility is attached to each discharge hole of the tubular member. Processing ship.

本発明の請求項1及び2によれば、酸原液を供給する管状部材の内径、吐出孔の数、吐出孔の孔径及び最初の吐出孔の孔径に対して最後の吐出孔の孔径の比を各特定の範囲に設定することにより、設定したpH値と実際の酸処理槽内のpH値との乖離を最小限として、且つ、酸処理槽内の濃度ムラが生じないようにして、十分な酸処理を効率的に行える海苔網の酸処理船が提供される。
請求項3の発明によれば、設定したpH値と実際の酸処理槽内のpH値との乖離を更に必要最小限として、十分な酸処理を更に効率的に行える海苔網の酸処理船が提供される。
請求項4及び5の発明によれば、各種装置(巻取ロール、シート状部材)を有する海苔網の酸処理船にも十分な酸処理を効率的に行えるものとなる。
請求項6の発明によれば、酸原液を酸処理槽内に確実に供給でき、十分な酸処理を効率的に行える海苔網の酸処理船が提供される。
According to claims 1 and 2 of the present invention, the inner diameter of the tubular member that supplies the acid stock solution, the number of discharge holes, the hole diameter of the discharge hole, and the ratio of the hole diameter of the last discharge hole to the hole diameter of the first discharge hole are determined. By setting each specific range, it is sufficient to minimize the deviation between the set pH value and the actual pH value in the acid treatment tank and prevent the concentration unevenness in the acid treatment tank from occurring. An acid treatment vessel for seaweed nets that can efficiently perform acid treatment is provided.
According to the invention of claim 3, an acid treatment vessel of a seaweed net capable of more efficiently performing sufficient acid treatment by further minimizing the deviation between the set pH value and the pH value in the actual acid treatment tank. Provided.
According to the inventions of claims 4 and 5, sufficient acid treatment can be efficiently performed even on an acid treatment ship of a seaweed net having various devices (winding rolls, sheet-shaped members).
According to the sixth aspect of the present invention, there is provided a seaweed net acid treatment vessel capable of reliably supplying an acid stock solution into an acid treatment tank and efficiently performing sufficient acid treatment.

本発明の第1実施形態を示す海苔網の酸処理船の図面であり、(a)は概略平面図、(b)は概略正面図である。It is a drawing of the acid treatment ship of the seaweed net which shows 1st Embodiment of this invention, (a) is a schematic plan view, (b) is a schematic front view. (a)は図1の海苔網の酸処理船に用いる管状部材の一例を示す底面側から見た図面、(b)は図1(b)の概略側面図である。(A) is a drawing seen from the bottom surface side showing an example of a tubular member used for the acid treatment ship of the seaweed net of FIG. 1, and (b) is a schematic side view of FIG. 1 (b). (a)は、図1の海苔網の酸処理船に用いる管状部材の比較形態の一例を示す底面側から見た図面であり、(b)~(d)は図1の海苔網の酸処理船に用いる管状部材の他例を示す底面側から見た各図面である。(A) is a drawing seen from the bottom surface side showing an example of the comparative form of the tubular member used for the acid treatment ship of the seaweed net of FIG. 1, and (b) to (d) are the acid treatment of the seaweed net of FIG. It is each drawing seen from the bottom side which shows the other example of the tubular member used for a ship. 本発明の第2実施形態を示す海苔網の酸処理船の図面であり、(a)は概略正面図、(b)は(a)の概略側面図、(c)は管状部材と可撓性チューブとの取り付け状態の一例を示す概略図面である。It is a drawing of the acid treatment ship of the seaweed net which shows the 2nd Embodiment of this invention, (a) is a schematic front view, (b) is a schematic side view of (a), (c) is a tubular member and flexibility. It is a schematic drawing which shows an example of the attachment state with a tube. 本発明の第3実施形態を示す海苔網の酸処理船の図面であり、(a)は概略正面図、(b)は(a)の概略側面図である。It is a drawing of the acid treatment ship of the seaweed net which shows the 3rd Embodiment of this invention, (a) is a schematic front view, (b) is a schematic side view of (a). 本発明の第4実施形態を示す海苔網の酸処理船の概略平面図である。It is a schematic plan view of the acid processing ship of the seaweed net which shows the 4th Embodiment of this invention. 本発明の第5実施形態を示す海苔網の酸処理船の図面であり、(a)は概略平面図、(b)は実施状態の一例を示す概略側面図である。It is a drawing of the acid treatment ship of the seaweed net which shows the 5th Embodiment of this invention, (a) is a schematic plan view, (b) is a schematic side view which shows an example of the embodiment. 試験2における測定用ハンディpH計5台を海苔網の酸処理船の酸処理槽に網羅するように配置した配置図面である。It is a layout drawing which arranged 5 handy pH meters for measurement in test 2 so as to cover the acid treatment tank of the acid treatment ship of a seaweed net.

以下に、本発明の各実施形態を詳しく説明する。
図1は、本発明の第1実施形態を示す海苔網の酸処理船の図面であり、(a)は概略平面図、(b)は概略正面図、図2(a)は図1の海苔網の酸処理船に用いる管状部材の一例を示す底面側から見た図面、(b)は図1(b)の概略側面図である。
本第1実施形態の海苔網の酸処理船Aは、図1(a)及び(b)に示すように、FRP等の繊維強化プラスチック等から構成される樹脂製の船本体10内に、少なくとも、酸処理液11を収容する酸処理槽15と、該酸処理槽15内に設けられる海苔網(図示せず)を巻き取る巻取ロール20と、前記酸処理槽15の中央部に懸架された支持部材25と、該支持部材25から前記酸処理槽15の酸処理液11に向かって垂下するシート状部材30と、前記酸処理槽15内に酸処理液11の酸原液Zを供給する酸原液供給装置40と、酸処理槽15内の酸処理液11のpH値を検出し、その検出値に基づいて前記酸原液供給装置40を作動させて、酸処理液11を一定のpH値に制御する制御部50とを備えたものである。
Hereinafter, each embodiment of the present invention will be described in detail.
1A and 1B are drawings of an acid-treated seaweed net showing the first embodiment of the present invention, FIG. 1A is a schematic plan view, FIG. 1B is a schematic front view, and FIG. 2A is a seaweed of FIG. A drawing seen from the bottom surface side showing an example of a tubular member used for an acid treatment ship of a net, (b) is a schematic side view of FIG. 1 (b).
As shown in FIGS. 1 (a) and 1 (b), the acid-treated ship A of the seaweed net of the first embodiment is contained in at least a resin-made ship body 10 made of fiber-reinforced plastic such as FRP. , The acid treatment tank 15 for accommodating the acid treatment liquid 11, the winding roll 20 for winding the seaweed net (not shown) provided in the acid treatment tank 15, and the central portion of the acid treatment tank 15. A support member 25, a sheet-shaped member 30 hanging from the support member 25 toward the acid treatment liquid 11 of the acid treatment tank 15, and an acid stock solution Z of the acid treatment liquid 11 are supplied into the acid treatment tank 15. The pH values of the acid stock solution supply device 40 and the acid treatment liquid 11 in the acid treatment tank 15 are detected, and the acid stock solution supply device 40 is operated based on the detected values to keep the acid treatment liquid 11 at a constant pH value. It is provided with a control unit 50 for controlling.

酸処理液11は、クエン酸、リンゴ酸などの有機酸等の酸原液〔市販品があれば市販の酸処理剤(液)、本実施形態では、第一製網社製の「グローゲン」〕Zが海水等によって希釈されたものであり、所定のpH値、例えば、pH1.7~2.3を有する酸希釈液である。
この酸処理液11は、酸処理槽15内に一定量(500~1,000L)が収容されており、巻き取られる海苔網(図示せず)を浸漬処理することによって海苔網に付着した海苔を酸処理するものである。
The acid treatment solution 11 is an acid stock solution such as an organic acid such as citric acid or malic acid [a commercially available acid treatment agent (liquid) if there is a commercially available product, in this embodiment, “Grogen” manufactured by Daiichi Netsui Co., Ltd.]. Z is diluted with seawater or the like, and is an acid diluted solution having a predetermined pH value, for example, pH 1.7 to 2.3.
A certain amount (500 to 1,000 L) of the acid-treated liquid 11 is contained in the acid-treated tank 15, and the seaweed attached to the seaweed net by dipping the seaweed net (not shown) to be wound up. Is acid-treated.

酸処理槽15は、船本体10の中央に形成された長方形状の凹状体となっており、所定量の酸処理液11を収容するものである。酸処理槽15の両側のスペース16、16には、酸原液供給装置40、制御部50、巻取ロール等の駆動部22、これらを駆動するバッテリー(図示せず)などが配置されると共に、作業者が作業するスペースとなっている。 The acid treatment tank 15 is a rectangular concave body formed in the center of the ship body 10, and accommodates a predetermined amount of the acid treatment liquid 11. In the spaces 16 and 16 on both sides of the acid treatment tank 15, an acid stock solution supply device 40, a control unit 50, a drive unit 22 such as a take-up roll, a battery (not shown) for driving these, and the like are arranged. It is a space for workers to work.

巻取ロール20は、海苔網を巻き取る回転軸であり、少なくとも1つ有するものであるが、本実施形態では、酸処理槽15内の所定の箇所に一対配置されている。この巻取ロール20、20は、回転自在に取り付けられており、一方の巻取ロール20は船本体10が前進した際(図1上では上側)に前方の海苔網を順次巻き取るものであり、他方の巻取ロール20は、船本体10が後進した際(図1上では下側)に後方の海苔網を順次巻き取るものである。また、本実施形態では、支持部材25の両側近傍に、海苔網を海側に繰り出す回転軸となる繰出ロール21、21が回転自在に取り付けられている。
前記支持部材の両側に配置される一対の巻取ロール20と繰出ロール21は、スペース16に設けられる操作装置を有する駆動部22、22により駆動される。
The take-up roll 20 is a rotation axis for winding the seaweed net, and has at least one. In the present embodiment, a pair of take-up rolls 20 are arranged at predetermined positions in the acid treatment tank 15. The take-up rolls 20 and 20 are rotatably attached, and one take-up roll 20 sequentially winds the front seaweed net when the ship body 10 moves forward (upper side in FIG. 1). On the other hand, the take-up roll 20 sequentially winds the rear seaweed net when the ship body 10 moves backward (lower side in FIG. 1). Further, in the present embodiment, feeding rolls 21 and 21 which serve as rotation axes for feeding the seaweed net to the sea side are rotatably attached to both sides of the support member 25.
The pair of winding rolls 20 and the feeding rolls 21 arranged on both sides of the support member are driven by the driving units 22 and 22 having an operating device provided in the space 16.

支持部材25は、棒状の部材から構成され、前記酸処理槽15の幅方向の中央部に懸架されるものであり、酸処理槽15の両側の上面部に取付部材(図示せず)を介して又は直接固着されるものである。
この支持部材25には、酸処理槽15の酸処理液11に向かって垂下する樹脂製のシート状部材30、本実施形態では軟質塩化ビニール製のシート状部材30が取り付けられており、酸処理槽15の酸処理液11内の底部近傍まで配置されている。シート状部材30の底部には、重り(沈子)となる棒状の部材31が取り付けられている。
このシート状部材30は、シート状部材30の両側に配置される巻取ロール20又は繰出ロール21に巻き取られた海苔網同士の直接接触による絡まりを防止する部材(カーテン)となるものである。従って、シート状部材30の下部は、酸処理槽15の酸処理液11内の底部近傍まで配置されていることが好ましい。
The support member 25 is composed of a rod-shaped member and is suspended in the central portion in the width direction of the acid treatment tank 15, and is interposed on the upper surface portions on both sides of the acid treatment tank 15 via mounting members (not shown). Or directly fixed.
A resin sheet-like member 30 hanging toward the acid treatment liquid 11 of the acid treatment tank 15 and a soft vinyl chloride sheet-like member 30 in the present embodiment are attached to the support member 25 for acid treatment. It is arranged up to the vicinity of the bottom in the acid treatment liquid 11 of the tank 15. A rod-shaped member 31 that serves as a weight (sinker) is attached to the bottom of the sheet-shaped member 30.
The sheet-shaped member 30 is a member (curtain) for preventing entanglement due to direct contact between the seaweed nets wound on the take-up roll 20 or the feeding roll 21 arranged on both sides of the sheet-shaped member 30. .. Therefore, it is preferable that the lower portion of the sheet-shaped member 30 is arranged up to the vicinity of the bottom portion in the acid treatment liquid 11 of the acid treatment tank 15.

酸原液供給装置40は、図1(a)に示すように、酸処理槽15のスペース16の適宜位置(海苔網の巻き取り及び繰り出しに干渉しない程度に酸処理槽から離れ、作業の邪魔にならない、例えば、作業者簡易座席の下空間)に配置されるものであり、前記酸処理槽15内に酸処理液11の酸原液Zを供給するものである。本実施形態では、酸原液供給装置40には、酸処理液11の酸原液Zを収容する原液タンク41と、該原液タンク41からポンプ42を介してライン43により連結されている。
制御部50は、酸処理槽15内の適宜位置(酸処理槽の平均的pHを検出可能な中央位置で、操出ロールに干渉されない、例えば、シート状部材近傍)に、酸処理液11のpH値を検出するpH検出器51を有し、pH検出器51で検出した検出値に基づいて前記酸原液供給装置40のポンプ42を作動させて、酸処理槽15内へ酸処理液の酸原液Zを供給して酸処理液を一定のpH値に制御するための装置である。制御部50は、pH検出器51の検出値に基づいて、供給する酸原液Zの供給量を自動調節するものである。
As shown in FIG. 1A, the acid stock solution supply device 40 is separated from the acid treatment tank at an appropriate position of the space 16 of the acid treatment tank 15 (to the extent that it does not interfere with the winding and feeding of the seaweed net, and interferes with the work. It is arranged in the space under the worker's simple seat, for example, and supplies the acid stock solution Z of the acid treatment liquid 11 into the acid treatment tank 15. In the present embodiment, the acid stock solution supply device 40 is connected to the stock solution tank 41 accommodating the acid stock solution Z of the acid treatment liquid 11 from the stock solution tank 41 via a line 43 via a pump 42.
The control unit 50 places the acid treatment liquid 11 at an appropriate position in the acid treatment tank 15 (at the center position where the average pH of the acid treatment tank can be detected and is not interfered with by the brewing roll, for example, in the vicinity of the sheet-like member). It has a pH detector 51 that detects a pH value, and operates the pump 42 of the acid stock solution supply device 40 based on the detection value detected by the pH detector 51 to enter the acid of the acid treatment liquid into the acid treatment tank 15. It is a device for supplying the undiluted solution Z to control the acid treatment solution to a constant pH value. The control unit 50 automatically adjusts the supply amount of the acid stock solution Z to be supplied based on the detection value of the pH detector 51.

シート状部材30の上部両側には、前記支持部材25の近傍に樹脂製の管状部材60、本実施形態ではFRP製の管状部材60が結束バンド等の取り付け具26により取り付けられている。
この管状部材60には、図1(b)及び図2(a)、(b)に示すように、一方の開口部60aから酸原液Zが供給され、他方の端部60bには栓部材60cが固着されており、管状部材60の下部(底面側)に、酸原液を滴下する複数の吐出孔61a、61b…、本実施形態では5個の吐出孔61a~61eが設けられている。
なお、本発明に用いる管状部材60は、FRP製の他、酸原液Zに対して耐酸性、耐候性、耐久性などを有するものであれば、特に限定されず、塩化ビニール製(以下、単に、「塩ビ」という場合がある)などの各種樹脂で構成でき、また、不透明(肉眼で酸原液を確認できないもの)、視認性を有する(肉眼で酸原液を確認できる)ものの何れかであってもよく、透明、半透明であれば、酸原液の送液状態が肉眼で確認できるものとなる。
A resin tubular member 60 and, in the present embodiment, an FRP tubular member 60 are attached to both sides of the upper portion of the sheet-shaped member 30 by attachments 26 such as a binding band in the vicinity of the support member 25.
As shown in FIGS. 1 (b) and 2 (a) and 2 (b), the acid stock solution Z is supplied to the tubular member 60 from one opening 60a, and the plug member 60c is supplied to the other end 60b. Is fixed, and a plurality of discharge holes 61a, 61b ... For dropping the acid stock solution, and five discharge holes 61a to 61e in the present embodiment are provided in the lower portion (bottom side) of the tubular member 60.
The tubular member 60 used in the present invention is not particularly limited as long as it is made of FRP or has acid resistance, weather resistance, durability, etc. with respect to the acid stock solution Z, and is made of vinyl chloride (hereinafter, simply referred to as “simply”). , "PVC", etc.), opaque (the acid stock solution cannot be confirmed with the naked eye), and visible (the acid stock solution can be confirmed with the naked eye). If it is transparent or translucent, the feeding state of the acid stock solution can be visually confirmed.

本発明では、酸原液の管状部材60内での残存漏れや空隙ロスを極めて少なくすることでポンプと吐出孔噴出の始動及び停止の応答時間差をなくし、設定したpH値と実際の酸処理槽内のpH値との乖離を最小限として、十分な酸処理が効率的に行えるようにするため、管状部材60の内径は3~8mmとすることが必要であり、また、吐出孔の数を3~10個とし、吐出孔の孔径(直径)を1.0~2.0mmであることが必要である。そして、複数吐出孔の噴出量バランスを調整して、酸処理槽の濃度ムラを更になくすために、好ましくは、管状部材60の内径を3~5mmとし、また、最初の吐出孔61aの孔径に対して最後の吐出孔61eの孔径の比が1.08~1.27倍となることが望ましい。
ここで、管状部材60の内径とは、管状部材60の直径(外径)から、管の厚み分を差し引いた、実際に液体(酸原液)が流れる部分の径のことを指す〔図2(a)の図示符号D〕。また、管状部材60の長手方向に垂直な断面は、円形であることが好ましい。また、前記垂直断面が楕円形である場合、管状部材60の内径とは、管状部材の前記垂直断面の中心を通るように引かれた直線の内、最も長い線のことを指す。また、管状部材は長手方向において内径が変化しない形状であることが好ましい。
なお、管状部材60の長さは、海苔網の巻き取り及び繰り出しなどに干渉しない箇所で、酸処理槽15上の任意の位置に配置するものであるので、酸処理槽15の大きさなどにより変動するが、酸処理槽15の幅方向の長さと同じか、取り付け態様を勘案すれば若干長いか若干短いものとなる。本実施形態では、酸処理槽15の幅方向の長さが210cmであり、管状部材60の長さは、190cmである。また、管状部材60の外径は8~13mmであることが好ましい。
In the present invention, the residual leakage and void loss in the tubular member 60 of the acid stock solution are extremely reduced to eliminate the difference in response time between the start and stop of the pump and the discharge hole ejection, and the set pH value and the actual acid treatment tank are used. It is necessary that the inner diameter of the tubular member 60 is 3 to 8 mm and the number of discharge holes is 3 in order to minimize the deviation from the pH value of the above and enable sufficient acid treatment efficiently. It is necessary that the number is ~ 10, and the hole diameter (diameter) of the discharge holes is 1.0 to 2.0 mm. Then, in order to adjust the ejection amount balance of the plurality of discharge holes and further eliminate the concentration unevenness in the acid treatment tank, the inner diameter of the tubular member 60 is preferably set to 3 to 5 mm, and the hole diameter of the first discharge hole 61a is set. On the other hand, it is desirable that the ratio of the hole diameters of the final discharge holes 61e is 1.08 to 1.27 times.
Here, the inner diameter of the tubular member 60 refers to the diameter of the portion where the liquid (acid stock solution) actually flows, which is obtained by subtracting the thickness of the pipe from the diameter (outer diameter) of the tubular member 60 [FIG. 2 (FIG. 2). The illustrated reference numeral D] in a). Further, the cross section of the tubular member 60 perpendicular to the longitudinal direction is preferably circular. When the vertical cross section is elliptical, the inner diameter of the tubular member 60 refers to the longest straight line drawn so as to pass through the center of the vertical cross section of the tubular member. Further, it is preferable that the tubular member has a shape in which the inner diameter does not change in the longitudinal direction.
Since the length of the tubular member 60 is arranged at an arbitrary position on the acid treatment tank 15 at a location that does not interfere with the winding and feeding of the seaweed net, it depends on the size of the acid treatment tank 15 and the like. Although it varies, it may be the same as the length in the width direction of the acid treatment tank 15, or slightly longer or slightly shorter in consideration of the mounting mode. In the present embodiment, the length of the acid treatment tank 15 in the width direction is 210 cm, and the length of the tubular member 60 is 190 cm. Further, the outer diameter of the tubular member 60 is preferably 8 to 13 mm.

上記管状部材60の内径は3~8mmであり、好ましくは、3~7mm、更に好ましくは、3~5mmであることが望ましい。この管状部材60の内径が8mm超過であると、酸原液の管状部材60内での残存漏れや空隙量が多くなるため、設定したpH値と実際の酸処理槽内のpH値との乖離が大きくなり、好ましくなく、一方、内径が3mm未満であると、噴出量(トータル量)の低下及び複数吐出孔の噴出量バランスの調整が困難となり、好ましくない。
また、管状部材60に形成した吐出孔61の数は、管状部材60の長さ、すなわち、酸処理槽15上に配置するものであるので、酸処理槽15の大きさなどにより変動するが、(管状部材1本あたりに)3~10個であり、好ましくは、3~6個、特に好ましくは、5~6個とすることが望ましい。この吐出孔61の数が2個以下であると、酸処理槽15への吐出(滴下を含む)箇所が少なく、酸処理槽15内での溶解等に時間がかかり濃度ムラが生じ、一方、10個超過であると、複数吐出孔の噴出量バランスの調整が複雑化することとなり、好ましくない。
更に、吐出孔の孔径が1.0mm未満であると、噴出量(トータル量)の低下と管状部材60の各吐出孔61、61…に均一に配分することができず、酸処理槽内の濃度ムラの要因となり、一方、吐出孔の孔径が2.0mm超過であると、管内の圧力が不足する傾向となり、管状部材60の各吐出孔61、61…に安定圧力で配分することができず、酸処理槽内の濃度ムラの要因となり、好ましくない。
最初の吐出孔61aの孔径に対して最後の吐出孔61eの孔径の比は同じであっても良いが、1.08倍未満であると、最後の吐出孔61eの噴出量が若干過少となり、一方、上記孔径の比が1.27倍超過であると、最後の吐出孔61eの噴出量が若干過多となる。
これらの内径、吐出孔の数及び孔径、孔径の比の関係性等については、後述する実施例等で詳述する。
The inner diameter of the tubular member 60 is preferably 3 to 8 mm, preferably 3 to 7 mm, and more preferably 3 to 5 mm. If the inner diameter of the tubular member 60 exceeds 8 mm, the residual leakage of the acid stock solution in the tubular member 60 and the amount of voids increase, so that the set pH value and the actual pH value in the acid treatment tank deviate from each other. On the other hand, if the inner diameter is less than 3 mm, it becomes difficult to reduce the ejection amount (total amount) and adjust the ejection amount balance of the plurality of discharge holes, which is not preferable.
Further, the number of discharge holes 61 formed in the tubular member 60 varies depending on the length of the tubular member 60, that is, because it is arranged on the acid treatment tank 15, the size of the acid treatment tank 15 and the like. The number is 3 to 10 (per tubular member), preferably 3 to 6, and particularly preferably 5 to 6. When the number of the discharge holes 61 is 2 or less, there are few places to discharge (including dropping) to the acid treatment tank 15, it takes time to dissolve in the acid treatment tank 15, and concentration unevenness occurs. If the number exceeds 10, the adjustment of the ejection amount balance of the plurality of discharge holes becomes complicated, which is not preferable.
Further, if the hole diameter of the discharge hole is less than 1.0 mm, the ejection amount (total amount) is reduced and the tubular member 60 cannot be uniformly distributed to the discharge holes 61, 61 ... On the other hand, if the hole diameter of the discharge hole exceeds 2.0 mm, the pressure in the pipe tends to be insufficient, and the pressure can be distributed to the discharge holes 61, 61 ... Of the tubular member 60 with a stable pressure. However, it causes uneven concentration in the acid treatment tank, which is not preferable.
The ratio of the hole diameter of the last discharge hole 61e to the hole diameter of the first discharge hole 61a may be the same, but if it is less than 1.08 times, the ejection amount of the last discharge hole 61e becomes slightly too small. On the other hand, if the ratio of the hole diameters exceeds 1.27 times, the amount of ejection from the final discharge hole 61e becomes slightly excessive.
The relationship between the inner diameter, the number of discharge holes, the hole diameter, the ratio of the hole diameters, and the like will be described in detail in Examples and the like described later.

前記管状部材60の各吐出孔61a、61b…の間隔(距離)は、所定間隔でよいが、吐出孔の数が4個以上の場合は、酸原液を更に均一に吐出(滴下含む)せしめる点等から、最初の吐出孔と2番目の吐出孔との間隔(X)と、最後の吐出孔の一つ前の吐出孔と最後の吐出孔の間隔が同じ(X=Xa-1,aは吐出孔の個数)であり、2番目の吐出孔(X)から最後の吐出孔の一つ前の吐出孔(Xa-1)の各間隔が同じ(X=X=…)であることが好ましい。
本実施形態では、図2(a)に示すように、酸原液Zのポンプ42の圧力(水圧)、管状部材の長さを勘案して、各吐出孔61a~61eから酸原液を更に均一に吐出(滴下含む)せしめる点等から、吐出孔61a、61b…間の距離(長さ)を変動せしめており、最初の吐出孔61aと2番目の吐出孔61bとの間隔(X)と、最後の吐出孔の一つ前の吐出孔61dと最後の吐出孔61eの間隔(X)が同じであり、2番目の吐出孔(X)から最後の吐出孔の一つ前の吐出孔の各間隔(X)の各間隔が同じ(X=X)であることが望ましい。
The interval (distance) between the discharge holes 61a, 61b ... Of the tubular member 60 may be a predetermined interval, but when the number of discharge holes is 4 or more, the acid stock solution is more uniformly discharged (including dropping). Therefore, the distance between the first discharge hole and the second discharge hole (X 1 ) is the same as the distance between the discharge hole immediately before the last discharge hole and the last discharge hole (X 1 = X a-1 ). , A is the number of discharge holes), and the distance between the second discharge hole (X 2 ) and the discharge hole (X a-1 ) immediately before the last discharge hole is the same (X 2 = X 3 =). ...).
In the present embodiment, as shown in FIG. 2A, the acid stock solution is further uniformly distributed from the discharge holes 61a to 61e in consideration of the pressure (water pressure) of the pump 42 of the acid stock solution Z and the length of the tubular member. The distance (length) between the discharge holes 61a, 61b ... Is varied from the point of discharging (including dropping), and the distance (X 1 ) between the first discharge hole 61a and the second discharge hole 61b is determined. The distance (X 4 ) between the discharge hole 61d immediately before the last discharge hole and the last discharge hole 61e is the same, and the discharge hole immediately before the last discharge hole from the second discharge hole (X 2 ) It is desirable that each interval of each interval (X 3 ) is the same (X 2 = X 3 ).

本実施形態では、管状部材60の長さ(全長X:一方の端部から他方の端部、以下同様)が190cmであり、内径3mm、外径8mmであり、5つの吐出孔61a~61eを有し、最初の吐出孔61a(中心、以下同様)までの間隔(距離X)が35cm、最初の吐出孔61aと次の吐出孔61bまでの間隔(距離X)が40cm、次の吐出孔61c、61dまでの間隔(距離X、距離X)が各20cm、次の吐出孔61eまでの間隔(距離X)が40cmとなっており、吐出孔61a~61dの孔径が1.5mm、最後の吐出孔61eの孔径が1.9mm(1.27倍)となっている。
これらの管状部材60の内径、吐出孔61a~61e間の間隔(距離)、また、各吐出孔の孔径(孔の大きさ)、その数等は、酸処理槽15の大きさ、形状、ポンプ種等により上記各範囲で変動させることができる。なお、管状部材60の入口となる端部から最初の吐出孔までの長さ(X)は、処理槽の大きさ、取り付け態様により変動するが全長Xに対して、0.12X~0.25Xであることが好ましい。
In the present embodiment, the tubular member 60 has a length (total length X: one end to the other end, the same applies hereinafter) of 190 cm, an inner diameter of 3 mm, an outer diameter of 8 mm, and five discharge holes 61a to 61e. The distance (distance X 0 ) to the first discharge hole 61a (center, the same applies hereinafter) is 35 cm, the distance (distance X 1 ) between the first discharge hole 61a and the next discharge hole 61b is 40 cm, and the next discharge The distance between the holes 61c and 61d (distance X 2 , distance X 3 ) is 20 cm each, the distance to the next discharge hole 61e (distance X 4 ) is 40 cm, and the hole diameters of the discharge holes 61a to 61d are 1. The hole diameter of the final discharge hole 61e is 1.9 mm (1.27 times).
The inner diameter of these tubular members 60, the distance (distance) between the discharge holes 61a to 61e, the hole diameter (hole size) of each discharge hole, the number thereof, etc. are the size, shape, and pump of the acid treatment tank 15. It can be varied in each of the above ranges depending on the species and the like. The length (X 0 ) from the end portion which is the inlet of the tubular member 60 to the first discharge hole varies depending on the size of the treatment tank and the mounting mode, but is 0.12 X to 0. It is preferably 25X.

このように構成される本第1実施形態の海苔網の酸処理船による海苔網の酸処理作業について、以下に、説明する。なお、船本体10が前進する場合と後進する場合とでは、同様であるので、本実施形態においては、船本体10が前進する場合(図1の上側)についてのみ説明する。
海苔網の酸処理船Aを養殖している海苔網が設置されている海上まで移動させた後、船本体10を海苔網を巻き取る力により前進せしめると、前進するにつれて、海苔網が酸処理槽15に前方から侵入し、侵入した海苔網は、駆動部22の駆動により巻取ロール20が回転することによって、順次巻取ロール20に巻き取られることとなる。巻き取られた海苔網は、酸処理槽15内に収容されている酸処理液11に浸漬処理され、海苔が酸処理されることとなる。
酸処理槽15内には、酸処理液11のpHをpH検出器51により検出し、このpH検出器51が検出した検出値は、制御部50に出力される。制御部50は、pH検出器51から入力された検出値と予め設定した制御しきい値とに基づいて、酸原液供給装置40のポンプ42をフィードバック制御する。ポンプ42は、制御部50から入力される作動信号に基づいて、該作動信号に応じた所定量の酸原液Zを酸原液タンク41から吸い出してライン44により管状部材60、60に供給する。また、前記制御部50は、pH検出器51の検出値に基づいて、ポンプ42を制御して酸処理液11に供給する酸原液Zの供給量を自動調節することができるものである。
The acid treatment work of the seaweed net by the acid treatment ship of the seaweed net of the first embodiment described in this way will be described below. Since the case where the ship body 10 moves forward and the case where the ship body 10 moves backward are the same, in the present embodiment, only the case where the ship body 10 moves forward (upper side of FIG. 1) will be described.
Nori net acid treatment After moving the Nori net cultivating seaweed net to the sea where the seaweed net is installed, the ship body 10 is advanced by the force of winding the seaweed net, and as it moves forward, the seaweed net is treated with acid. The seaweed net that has invaded the tank 15 from the front and has invaded is sequentially taken up by the take-up roll 20 by rotating the take-up roll 20 by the drive of the drive unit 22. The rolled seaweed net is immersed in the acid treatment liquid 11 contained in the acid treatment tank 15, and the seaweed is acid-treated.
In the acid treatment tank 15, the pH of the acid treatment liquid 11 is detected by the pH detector 51, and the detection value detected by the pH detector 51 is output to the control unit 50. The control unit 50 feedback-controls the pump 42 of the acid stock solution supply device 40 based on the detection value input from the pH detector 51 and the preset control threshold value. Based on the operation signal input from the control unit 50, the pump 42 sucks out a predetermined amount of the acid stock solution Z corresponding to the operation signal from the acid stock solution tank 41 and supplies it to the tubular members 60 and 60 by the line 44. Further, the control unit 50 can control the pump 42 to automatically adjust the supply amount of the acid stock solution Z to be supplied to the acid treatment liquid 11 based on the detection value of the pH detector 51.

前記pH検出器51からの作動信号を受信したポンプ42によって酸原液タンク41から吸い出された酸原液Zは、管状部材60、60に供給され、管状部材60、60に設けられた複数の吐出孔61a、61b…から、酸処理液11内に吐出(滴下)される。酸処理液11内に滴下された酸原液Zは、酸処理液11内で直ぐに溶解することとなる。この溶解性は、前記酸原液Zが水溶性であり、船本体10の揺れ、巻取ロール20の回転などによって酸処理液11中に生成される回流等によって、酸処理液11が撹拌状態となることによって、酸処理での海水により薄まった酸処理液11中に溶解し拡散することとなり、これにより酸処理液11中の高値に変動したpH値を所定のpH値にすることができる。なお、pH値の表示は、制御部50に備えた防水性のpH表示液晶画面等(図示せず)で確認することもできる。
前記酸処理する養殖海苔の付着した海苔網が巻取ロール20への巻取りを経て更に操出ロール21に巻き取られ、酸処理された後、繰出ロール21に巻き付けられている海苔網は、船本体10が前進するにつれて、船本体10外へ巻き出されて巻き取った海苔網が設置されていた場所に設置されることとなる。
The acid stock solution Z sucked out from the acid stock solution tank 41 by the pump 42 that received the operation signal from the pH detector 51 is supplied to the tubular members 60, 60, and a plurality of discharges provided in the tubular members 60, 60. It is discharged (dropped) into the acid treatment liquid 11 from the holes 61a, 61b. The acid stock solution Z dropped into the acid treatment liquid 11 is immediately dissolved in the acid treatment liquid 11. The solubility of the acid stock solution Z is that the acid stock solution Z is water-soluble, and the acid treatment solution 11 is in a stirred state due to the circulation generated in the acid treatment solution 11 due to the shaking of the ship body 10, the rotation of the take-up roll 20, and the like. As a result, it dissolves and diffuses in the acid-treated liquid 11 diluted with seawater in the acid treatment, whereby the pH value that fluctuates to a high value in the acid-treated liquid 11 can be set to a predetermined pH value. The display of the pH value can also be confirmed on a waterproof pH display liquid crystal screen or the like (not shown) provided in the control unit 50.
The seaweed net to which the acid-treated cultured seaweed is attached is wound on the take-up roll 20 and then further wound on the manipulating roll 21, and after being acid-treated, the seaweed net wound on the feeding roll 21 is formed. As the ship body 10 moves forward, it will be installed in the place where the seaweed net that has been unwound and wound out of the ship body 10 has been installed.

このように構成される本第1実施形態の海苔網の酸処理船Aによれば、酸原液供給装置40には、支持部材25の近傍に設けられた酸原液Zを吐出する複数の吐出孔61a、61b…を有する管状部材60、60を備えており、該管状部材60の内径、吐出孔61a…の数、該吐出孔61a…の孔径を上記各特定の範囲に設定することにより、設定したpH値と実際の酸処理槽内のpH値との乖離が最小限となり、十分な酸処理を効率的に行える海苔網の酸処理船が得られることとなる。好ましくは、上記条件に加え、更に、最初の吐出孔61aの孔径に対して最後の吐出孔61eの孔径の比を上記特定比の範囲(1.08~1.27倍)に設定することにより、更に設定したpH値と実際の酸処理槽内のpH値との乖離が極めて最小限となり、十分な酸処理を更に効率的に行える海苔網の酸処理船が得られることとなる。 According to the acid treatment vessel A of the seaweed net of the first embodiment configured as described above, the acid stock solution supply device 40 has a plurality of discharge holes for discharging the acid stock solution Z provided in the vicinity of the support member 25. The tubular members 60, 60 having 61a, 61b ... Are provided, and the inner diameter of the tubular member 60, the number of discharge holes 61a ..., and the hole diameter of the discharge holes 61a ... The deviation between the pH value obtained and the actual pH value in the acid treatment tank is minimized, and an acid treatment vessel of a seaweed net capable of efficiently performing sufficient acid treatment can be obtained. Preferably, in addition to the above conditions, the ratio of the hole diameter of the last discharge hole 61e to the hole diameter of the first discharge hole 61a is set within the range of the specific ratio (1.08 to 1.27 times). Further, the deviation between the set pH value and the actual pH value in the acid treatment tank is extremely minimized, and a seaweed net acid treatment vessel capable of performing sufficient acid treatment more efficiently can be obtained.

本発明に用いる管状部材60は、上述の如く、内径を3~8mmとし、吐出孔の数を3~10個とし、吐出孔の孔径を1.0~2.0mmとすることが必要であり、更に好ましい形態として、最初の吐出孔の孔径に対して最後の吐出孔の孔径の比を1.08~1.27倍とすることにより、酸原液の管状部材60内での残存漏れや空隙ロスを極めて少なくすることでポンプと吐出孔噴出の始動及び停止の応答時間差をなくし、設定したpH値と実際の酸処理槽内のpH値との乖離を最小限として、且つ、酸処理槽内の濃度ムラが生じないようにして、十分な酸処理を更に効率的に行うことができるものとなる。 As described above, the tubular member 60 used in the present invention needs to have an inner diameter of 3 to 8 mm, a number of discharge holes of 3 to 10, and a hole diameter of 1.0 to 2.0 mm. As a more preferable form, by setting the ratio of the hole diameter of the last discharge hole to the hole diameter of the first discharge hole to 1.08 to 1.27 times, residual leakage or voids of the acid stock solution in the tubular member 60 By extremely reducing the loss, the difference in response time between the start and stop of the pump and the discharge hole ejection is eliminated, the deviation between the set pH value and the actual pH value in the acid treatment tank is minimized, and in the acid treatment tank. Sufficient acid treatment can be performed more efficiently by preventing the concentration unevenness of the above.

図3の(b)~(d)は、上記実施形態の海苔網の酸処理船に用いる管状部材60の他例を示す底面側から見た各図面である。なお、図3(a)は、比較形態の図面である。
図3(a)は、管状部材60(FRP素材)の長さが200cmであり、内径3mm、外径8mmであり、2つの吐出孔61a、61bを有し、最初の吐出孔61aまでの間隔(距離X)が70cm、最初の吐出孔61aと次の吐出孔61bまでの間隔(距離X)が60cmとなっており、吐出孔61aの孔径が1.2mm、最後の吐出孔61bの孔径が1.5mm(1.25倍)となっている。
図3(b)は、管状部材60(FRP素材)の長さが200cmであり、内径3mm、外径8mmであり、3つの吐出孔61a~61cを有し、最初の吐出孔61aまでの間隔(距離X)が50cm、最初の吐出孔61aと次の吐出孔61bまでの間隔(距離X)が50cm、次の吐出孔61cまでの間隔(距離X)が50cmとなっており、吐出孔61a~61bの孔径が1.2mm、最後の吐出孔61cの孔径が1.5mm(1.25倍)となっている。
図3(c)は、管状部材60(FRP素材)の長さが200cmであり、内径3mm、外径5mmであり、6つの吐出孔61a~61fを有し、最初の吐出孔61aまでの間隔(距離X)が25cm、最初の吐出孔61aと次の吐出孔61bまでの間隔(距離X)が30cm、次の吐出孔61c、61d、61eまでの間隔(距離X、距離X、距離X)が各30cm、次の吐出孔61fまでの間隔(距離X)が30cmとなっており、吐出孔61a~61eの孔径が1.2mm、最後の吐出孔61fの孔径が1.2又は1.3又は1.5又は1.6mm(1.00又は1.08又は1.25又は1.33倍)となっている。
図3(d)は、管状部材60(透明な塩ビ素材)の長さが200cmであり、内径5mm、外径10mmであり、6つの吐出孔61a~61fを有し、最初の吐出孔61aまでの間隔(距離X)が25cm、最初の吐出孔61aと次の吐出孔61bまでの間隔(距離X)が30cm、次の吐出孔61c、61d、61eまでの間隔(距離X、距離X、距離X)が各30cm、次の吐出孔61fまでの間隔(距離X)が30cmとなっており、吐出孔61a~61eの孔径が1.8mm、最後の吐出孔61fの孔径が2.0又は2.1〔比較形態〕mm(1.11又は1.17倍)となっている。
3 (b) to 3 (d) are drawings seen from the bottom surface side showing another example of the tubular member 60 used in the acid-treated ship of the seaweed net of the above embodiment. Note that FIG. 3A is a comparative drawing.
FIG. 3A shows a tubular member 60 (FRP material) having a length of 200 cm, an inner diameter of 3 mm, an outer diameter of 8 mm, two discharge holes 61a and 61b, and a distance to the first discharge hole 61a. (Distance X 0 ) is 70 cm, the distance between the first discharge hole 61a and the next discharge hole 61b (distance X 1 ) is 60 cm, the hole diameter of the discharge hole 61a is 1.2 mm, and the last discharge hole 61b. The hole diameter is 1.5 mm (1.25 times).
FIG. 3B shows a tubular member 60 (FRP material) having a length of 200 cm, an inner diameter of 3 mm, an outer diameter of 8 mm, three discharge holes 61a to 61c, and an interval to the first discharge hole 61a. (Distance X 0 ) is 50 cm, the distance between the first discharge hole 61a and the next discharge hole 61b (distance X 1 ) is 50 cm, and the distance between the next discharge hole 61c (distance X 2 ) is 50 cm. The hole diameters of the discharge holes 61a to 61b are 1.2 mm, and the hole diameter of the final discharge hole 61c is 1.5 mm (1.25 times).
FIG. 3C shows a tubular member 60 (FRP material) having a length of 200 cm, an inner diameter of 3 mm, an outer diameter of 5 mm, six discharge holes 61a to 61f, and an interval to the first discharge hole 61a. (Distance X 0 ) is 25 cm, the distance between the first discharge hole 61a and the next discharge hole 61b (distance X 1 ) is 30 cm, and the distance between the next discharge holes 61c, 61d, 61e (distance X 2 , distance X 3 ). , The distance X 4 ) is 30 cm each, the distance to the next discharge hole 61f (distance X 5 ) is 30 cm, the hole diameters of the discharge holes 61a to 61e are 1.2 mm, and the hole diameter of the last discharge hole 61f is 1. It is .2 or 1.3 or 1.5 or 1.6 mm (1.00 or 1.08 or 1.25 or 1.33 times).
FIG. 3D shows a tubular member 60 (transparent vinyl chloride material) having a length of 200 cm, an inner diameter of 5 mm, an outer diameter of 10 mm, six discharge holes 61a to 61f, and up to the first discharge hole 61a. The distance (distance X 0 ) is 25 cm, the distance between the first discharge hole 61a and the next discharge hole 61b (distance X 1 ) is 30 cm, and the distance between the next discharge holes 61c, 61d, 61e (distance X 2 , distance). X 3 and distance X 4 ) are 30 cm each, the distance to the next discharge hole 61f (distance X 5 ) is 30 cm, the hole diameters of the discharge holes 61a to 61e are 1.8 mm, and the hole diameter of the last discharge hole 61f. Is 2.0 or 2.1 [comparative form] mm (1.11 or 1.17 times).

図4は、本発明の第2実施形態を示す海苔網の酸処理船の要部を示す図面である。以下の第2実施形態~第5実施形態において、前記第1実施形態と同様の構成は、図面において同一の図示符号を示し、その説明を省略する。
本発明となる第2実施形態を示す海苔網の酸処理船Bは、上記管状部材60の各吐出孔61a~61eに、該各吐出孔61a~61eから吐出する酸原液Zを酸処理液11の液面に導く樹脂製、エラストマー製又はゴム製の視認性を有する可撓性チューブ62、62…を固着、溶着、取り付け具などにより取り付けた形態となるものある。
視認性を有する可撓性チューブ62、62…の長さは、図4(a)に示すように、管状部材60、60の下部から液面Yまでの長さ(距離)をWとした場合に、本実施形態のチューブ62a、62a…の長さは2/3Wであり、この長さであれば、視認性を有する可撓性チューブ62a、62a…から吐出する酸原液Zがシート状部材30に更に付着することなく、酸処理液に滴下されるものとなる。
FIG. 4 is a drawing showing a main part of an acid treatment ship of a seaweed net showing a second embodiment of the present invention. In the following second to fifth embodiments, the same configurations as those in the first embodiment show the same reference numerals in the drawings, and the description thereof will be omitted.
In the seaweed net acid treatment vessel B according to the second embodiment of the present invention, the acid stock solution Z discharged from the discharge holes 61a to 61e of the tubular member 60 is subjected to the acid treatment liquid 11 in the discharge holes 61a to 61e. Flexible tubes 62, 62 ... Made of resin, elastomer, or rubber that lead to the liquid surface of the above can be attached by fixing, welding, attachment, or the like.
As shown in FIG. 4A, the length of the flexible tubes 62, 62 ... With visibility is the case where the length (distance) from the lower portion of the tubular members 60, 60 to the liquid level Y is W. In addition, the length of the tubes 62a, 62a ... Of the present embodiment is 2/3 W, and if this length is used, the acid stock solution Z discharged from the flexible tubes 62a, 62a ... With visibility is a sheet-like member. It will be dropped into the acid treatment liquid without further adhering to 30.

また、可撓性チューブ62、62…は、視認性を有する(肉眼で酸原液を確認できる)ものであればよく、透明、半透明の何れでもよく、透明、半透明であれば、可撓性チューブ内の酸原液Zの滴下が肉眼で確認できるものとなる。また、視認性を有する可撓性の孔径(内径)は、吐出孔61a~61e61の孔径と同じ又は大きい孔径となっており、本実施形態では、内径6mmであり、塩化ビニール製の透明な視認性を有する可撓性チューブから構成されている。 Further, the flexible tubes 62, 62 ... may be transparent or translucent as long as they have visibility (the acid stock solution can be confirmed with the naked eye), and if they are transparent or translucent, they are flexible. The dropping of the acid stock solution Z in the sex tube can be visually confirmed. Further, the flexible hole diameter (inner diameter) having visibility is the same as or larger than the hole diameter of the discharge holes 61a to 61e61, and in the present embodiment, the inner diameter is 6 mm, and the transparent visibility made of vinyl chloride. It is composed of a flexible tube having a property.

本第2実施形態においても、前記第1実施形態と同様に、酸原液供給装置40、制御部50等の作動により、前記酸処理作業により高値に変動した酸処理液のpH値を所定のpH値に自動調節することができ、また、管状部材60の内径、吐出孔61a…の数、該吐出孔61a…の孔径、及び、最初の吐出孔61aの孔径に対して最後の吐出孔61eの孔径の比を上記各特定の範囲に設定することにより、設定したpH値と実際の酸処理槽内のpH値との乖離が最小限となり、且つ、酸処理槽内の濃度ムラが生じないようにして、十分な酸処理を効率的に行えるものとなる。更に、本実施形態では、シート状部材30に酸原液Zを吐出するものではないので、シート状部材30に酸原液Zが付着することもなく、巻き取られた海苔網がシート状部材30に残存する酸原液に接触することがなく、酸原液の飛沫もなく、海苔網を確実に酸処理液で酸処理でき、無駄な酸原液の消費が行われることがない海苔網の酸処理船が得られることとなる。
前記第2実施形態において、前記視認性を有する可撓性チューブ62a、62a…の長さを2/3Wとしたが、管状部材60、60の取り付け位置をシート状部材30に吐出される酸原液Zが付着できない場所に取り付けたりすれば、酸処理液の液面までの長さの1/3Wであってもよく、また、視認性を有する可撓性チューブ62a、62a…の長さWが前記液面に接触するまでの長さ、更に、液面Yより下部となる酸処理液11内に侵入する長さとしてもよいものである。
Also in the second embodiment, as in the first embodiment, the pH value of the acid-treated solution, which has changed to a high value due to the acid-treating operation by the operation of the acid stock solution supply device 40, the control unit 50, etc., is set to a predetermined pH. The value can be automatically adjusted, and the inner diameter of the tubular member 60, the number of discharge holes 61a ..., the hole diameter of the discharge holes 61a ..., and the hole diameter of the first discharge hole 61a of the last discharge hole 61e. By setting the ratio of the pore diameters to each of the above specific ranges, the deviation between the set pH value and the actual pH value in the acid treatment tank is minimized, and the concentration unevenness in the acid treatment tank does not occur. Therefore, sufficient acid treatment can be efficiently performed. Further, in the present embodiment, since the acid stock solution Z is not discharged to the sheet-shaped member 30, the acid stock solution Z does not adhere to the sheet-shaped member 30, and the rolled seaweed net is transferred to the sheet-shaped member 30. An acid treatment ship for seaweed nets that does not come into contact with the remaining acid stock solution, does not splash the acid stock solution, can reliably acidify the seaweed net with the acid treatment liquid, and does not waste the acid stock solution. Will be obtained.
In the second embodiment, the length of the flexible tubes 62a, 62a ... Having visibility is set to 2/3 W, but the attachment position of the tubular members 60, 60 is the acid stock solution discharged to the sheet-shaped member 30. If it is attached to a place where Z cannot adhere, it may be 1/3 W of the length to the liquid surface of the acid treatment liquid, and the length W of the flexible tubes 62a, 62a ... Having visibility may be. It may be the length until it comes into contact with the liquid surface, and the length may be such that it penetrates into the acid-treated liquid 11 below the liquid level Y.

図5は、本発明の第3実施形態を示す海苔網の酸処理船の要部を示す図面である。
本発明の第3実施形態を示す海苔網の酸処理船Cは、酸原液を吐出する複数の吐出孔61a、61b…を備えた管状部材60、60が、酸処理液の液面Yの近傍、具体的には、液面Yから1~15cmの上部に設けられたものである。本実施形態では、液面Yから5cmの上部に設けられたものである。
本第3実施形態においても、前記第1実施形態と同様に、酸原液供給装置40、制御部50等の作動により、前記酸処理作業により高値に変動した酸処理液のpH値を所定のpH値に自動調節することができ、また、該管状部材60の内径、吐出孔61a…の数、該吐出孔61a…の孔径、及び、最初の吐出孔61aの孔径に対して最後の吐出孔61eの孔径の比を上記各特定の範囲に設定することにより、設定したpH値と実際の酸処理槽内のpH値との乖離が最小限となり、且つ、酸処理槽内の濃度ムラが生じないようにして、十分な酸処理を効率的に行える海苔網の酸処理船が得られることとなる。更に、酸原液を吐出する吐出孔61a、61b…を備えた管状部材60、60は酸処理液の液面Yの近傍に設けたものであるので、管状部材60、60の吐出孔61a、61b…の吐出が肉眼で確認でき、シート状部材30に酸原液が付着することもなく、しかも、巻き取られた海苔網がシート状部材30に残存する酸原液に接触することがないので、海苔網を確実に酸処理液で酸処理できる海苔網の酸処理船が得られることとなる。
FIG. 5 is a drawing showing a main part of an acid treatment ship of a seaweed net showing a third embodiment of the present invention.
In the seaweed net acid treatment vessel C according to the third embodiment of the present invention, the tubular members 60, 60 provided with a plurality of discharge holes 61a, 61b ... For discharging the acid stock solution are in the vicinity of the liquid level Y of the acid treatment liquid. Specifically, it is provided above the liquid level Y by 1 to 15 cm. In the present embodiment, it is provided above the liquid level Y 5 cm.
Also in the third embodiment, as in the first embodiment, the pH value of the acid-treated solution, which has changed to a high value due to the acid-treating operation by the operation of the acid stock solution supply device 40, the control unit 50, etc., is set to a predetermined pH. The value can be automatically adjusted, and the inner diameter of the tubular member 60, the number of discharge holes 61a ..., the hole diameter of the discharge holes 61a ..., and the last discharge hole 61e with respect to the hole diameter of the first discharge hole 61a. By setting the ratio of the pore diameters in each of the above specific ranges, the deviation between the set pH value and the actual pH value in the acid treatment tank is minimized, and the concentration unevenness in the acid treatment tank does not occur. In this way, an acid treatment vessel with a seaweed net that can efficiently perform sufficient acid treatment can be obtained. Further, since the tubular members 60, 60 provided with the discharge holes 61a, 61b ... for discharging the acid stock solution are provided in the vicinity of the liquid level Y of the acid treatment liquid, the discharge holes 61a, 61b of the tubular members 60, 60 are provided. The discharge of ... can be confirmed with the naked eye, the acid stock solution does not adhere to the sheet-shaped member 30, and the rolled seaweed net does not come into contact with the acid stock solution remaining on the sheet-shaped member 30. It is possible to obtain an acid-treated seaweed net that can reliably acid-treat the net with an acid-treated liquid.

図6は、本発明の第4実施形態を示す海苔網の酸処理船の要部を示す図面である。
本発明の第4実施形態を示す海苔網の酸処理船Dは、シート状部材30が存在しない場合の形態であり、酸処理槽15の両側端部に設けた支持部材26,26に前記第1実施形態と同様の吐出孔61a~61eを有する管状部材60、60を取り付けたもので、上記第1実施形態と相違するものである。
本第4実施形態においても、酸原液供給装置40、制御部50等の作動により、前記酸処理作業により高値に変動した酸処理液のpH値を所定のpH値に自動調節することができ、また、管状部材60の内径、吐出孔61a…の数、該吐出孔61a…の孔径、及び、最初の吐出孔61aの孔径に対して最後の吐出孔61eの孔径の比を上記第1実施形態で詳述した各特定の範囲に設定することにより、設定したpH値と実際の酸処理槽内のpH値との乖離が最小限となり、且つ、酸処理槽内の濃度ムラが生じないようにして、十分な酸処理を効率的に行える海苔網の酸処理船が得られることとなる。
FIG. 6 is a drawing showing a main part of an acid treatment ship of a seaweed net showing a fourth embodiment of the present invention.
The seaweed net acid treatment vessel D according to the fourth embodiment of the present invention is in the case where the sheet-like member 30 does not exist, and the support members 26 and 26 provided at both end portions of the acid treatment tank 15 have the above-mentioned first. Tubular members 60, 60 having discharge holes 61a to 61e similar to those of the first embodiment are attached, and are different from the first embodiment.
Also in the fourth embodiment, the pH value of the acid-treated solution, which has changed to a high value due to the acid treatment operation, can be automatically adjusted to a predetermined pH value by operating the acid stock solution supply device 40, the control unit 50, and the like. Further, the ratio of the inner diameter of the tubular member 60, the number of discharge holes 61a ..., the hole diameter of the discharge holes 61a ..., and the hole diameter of the first discharge hole 61a to the hole diameter of the last discharge hole 61e is the first embodiment. By setting each specific range described in detail in the above section, the deviation between the set pH value and the actual pH value in the acid treatment tank is minimized, and the concentration unevenness in the acid treatment tank is prevented from occurring. As a result, an acid treatment vessel with a seaweed net that can efficiently perform sufficient acid treatment can be obtained.

図7は、本発明の第5実施形態を示す海苔網の酸処理船の要部を示す図面である。
本発明の第5実施形態を示す海苔網の酸処理船Eは、巻取ロールを設けない素通し酸処理船に適用したものであり、酸処理槽15の進行側端部に設けた支持部材26に前記第1実施形態と同様の吐出孔61a、61b…を有する管状部材60〔図2(a),図3(b)~(d)等〕を取り付けたものである。
本第5実施形態においても、酸原液供給装置40、制御部50等の作動により、前記酸処理作業により高値に変動した酸処理液のpH値を所定のpH値に自動調節することができ、また、管状部材60の内径、吐出孔61a…の数、該吐出孔61a…の孔径、及び、最初の吐出孔61aの孔径に対して最後の吐出孔61c又はfの孔径の比を上記第1実施形態で詳述した各特定の範囲に設定することにより、設定したpH値と実際の酸処理槽内のpH値との乖離が最小限となり、且つ、酸処理槽内の濃度ムラが生じないようにして、十分な酸処理を効率的に行える海苔網の酸処理船が得られることとなる。
FIG. 7 is a drawing showing a main part of an acid treatment ship of a seaweed net showing a fifth embodiment of the present invention.
The seaweed net acid treatment vessel E according to the fifth embodiment of the present invention is applied to a pass-through acid treatment vessel not provided with a take-up roll, and is a support member 26 provided at the advancing side end of the acid treatment tank 15. A tubular member 60 [FIGS. 2 (a), 3 (b) to (d), etc.] having discharge holes 61a, 61b ... Similar to that of the first embodiment is attached to the surface.
Also in the fifth embodiment, the pH value of the acid-treated solution, which has changed to a high value due to the acid treatment operation, can be automatically adjusted to a predetermined pH value by operating the acid stock solution supply device 40, the control unit 50, and the like. Further, the ratio of the inner diameter of the tubular member 60, the number of discharge holes 61a ..., the hole diameter of the discharge holes 61a ..., and the hole diameter of the last discharge hole 61c or f to the hole diameter of the first discharge hole 61a is the first. By setting each specific range described in detail in the embodiment, the deviation between the set pH value and the actual pH value in the acid treatment tank is minimized, and the concentration unevenness in the acid treatment tank does not occur. In this way, an acid treatment vessel with a seaweed net that can efficiently perform sufficient acid treatment can be obtained.

このように構成される本第5実施形態の海苔網の酸処理船による海苔網の酸処理作業(素通し処理)について、以下に、説明する〔図7(b)〕。
海苔網の酸処理船Eを養殖している海苔網Nが設置されている海上まで移動させた後、海苔網ガイド71を海苔網Nの下に潜らせて船本体10を(図に示す進行方向に)船外機70の駆動力により前進せしめると、前進するにつれて、海苔網Nが酸処理槽15に前方から侵入し、侵入した海苔網Nは、塩ビ製等の両端有底円筒形の浮上体(俗称「コロ」)72の下方を通り、酸処理槽15内に収容されている酸処理液11に浸漬処理され、海苔が酸処理されることとなる。
酸処理槽15内には、酸処理液11のpHをpH検出器51により検出し、このpH検出器51が検出した検出値は、制御部50に出力される。制御部50は、pH検出器51から入力された検出値と予め設定した制御しきい値とに基づいて、酸原液供給装置40のポンプ42をフィードバック制御する。ポンプ42は、制御部50から入力される作動信号に基づいて、該作動信号に応じた所定量の酸原液Zを酸原液タンク41から吸い出してライン44により管状部材60に供給する。また、前記制御部50は、pH検出器51の検出値に基づいて、ポンプ42を制御して酸処理液11に供給する酸原液Zの供給量を自動調節することができるものである。
前記pH検出器51からの作動信号を受信したポンプ42によって酸原液タンク41から吸い出された酸原液Zは、管状部材60に供給され、管状部材60に設けられた複数の吐出孔61a、61b…から、酸処理液11内に吐出(滴下)される。酸処理液11内に滴下された酸原液Zは、酸処理液11内で直ぐに溶解することとなる。この溶解性は、前記酸原液Zが水溶性であり、船本体10の推進、海苔網の通過及びコロ72の回転などによって酸処理液11中に生成される回流等によって、酸処理液11が撹拌状態となることによって、酸処理での海水により薄まった酸処理液11中に溶解し拡散することとなり、これにより酸処理液11中の高値に変動したpH値を所定のpH値にすることができる。なお、pH値の表示は、制御部50に備えた防水性のpH表示液晶画面等(図示せず)で確認することもできる。
前記酸処理する養殖海苔の付着した海苔網Nは、コロ72の下方を通過し酸処理された後、船本体10が更に前進するにつれて、船本体10外、船後方へ位置することとなり海苔網Nが元の養殖海面へ戻ることとなる。
The acid treatment work (passing treatment) of the seaweed net by the acid treatment ship of the seaweed net according to the fifth embodiment described in this manner will be described below [FIG. 7 (b)].
After moving the seaweed net acid treatment ship E to the sea where the seaweed net N cultivating is installed, the seaweed net guide 71 is submerged under the seaweed net N to move the ship body 10 (progress shown in the figure). When the seaweed net N is advanced by the driving force of the outboard unit 70 (in the direction), the seaweed net N invades the acid treatment tank 15 from the front as it advances, and the invaded seaweed net N is made of vinyl chloride or the like and has a bottomed cylindrical shape at both ends. The seaweed is acid-treated by passing under the floating body (commonly known as "coro") 72 and being immersed in the acid-treated liquid 11 contained in the acid-treating tank 15.
In the acid treatment tank 15, the pH of the acid treatment liquid 11 is detected by the pH detector 51, and the detection value detected by the pH detector 51 is output to the control unit 50. The control unit 50 feedback-controls the pump 42 of the acid stock solution supply device 40 based on the detection value input from the pH detector 51 and the preset control threshold value. Based on the operation signal input from the control unit 50, the pump 42 sucks out a predetermined amount of the acid stock solution Z corresponding to the operation signal from the acid stock solution tank 41 and supplies it to the tubular member 60 by the line 44. Further, the control unit 50 can control the pump 42 to automatically adjust the supply amount of the acid stock solution Z to be supplied to the acid treatment liquid 11 based on the detection value of the pH detector 51.
The acid stock solution Z sucked out from the acid stock solution tank 41 by the pump 42 that received the operation signal from the pH detector 51 is supplied to the tubular member 60, and a plurality of discharge holes 61a and 61b provided in the tubular member 60. From ..., it is discharged (dropped) into the acid treatment liquid 11. The acid stock solution Z dropped into the acid treatment liquid 11 is immediately dissolved in the acid treatment liquid 11. This solubility is such that the acid stock solution Z is water-soluble, and the acid treatment liquid 11 is subjected to circulation or the like generated in the acid treatment liquid 11 by propulsion of the ship body 10, passage of a seaweed net, rotation of a roller 72, or the like. By being in a stirred state, it dissolves and diffuses in the acid-treated liquid 11 diluted with seawater in the acid treatment, whereby the pH value that fluctuates to a high value in the acid-treated liquid 11 is set to a predetermined pH value. Can be done. The display of the pH value can also be confirmed on a waterproof pH display liquid crystal screen or the like (not shown) provided in the control unit 50.
The seaweed net N to which the acid-treated cultured seaweed adheres passes under the roller 72 and is acid-treated, and then as the ship body 10 further advances, it is located outside the ship body 10 and behind the ship. N will return to the original farmed sea surface.

本発明の海苔網の酸処理船は、少なくとも、酸処理液を収容する酸処理槽と、該酸処理槽内に酸処理液の原液を供給する酸原液供給装置と、酸処理槽内の酸処理液のpH値を検出し、その検出値に基づいて前記酸原液供給装置を作動させて、酸処理液を一定のpH値に制御する制御部とを備えた海苔網の酸処理船であって、前記酸原液供給装置には、前記酸処理槽上の任意の位置に、酸原液を噴出する複数の吐出孔を有する有底筒状の管状部材を少なくとも1つ以上備えると共に、該管状部材は内径、吐出孔の数、該吐出孔の孔径を各特定の範囲とすることを要旨とするので、上記第1実施形態~第5実施形態に限定されるものでなく、本発明の要旨を変更しない範囲で、以下の各変形の実施形態を採用することができる。
例えば、前記第1実施形態~第4実施形態の各種装置(巻取ロール、シート状部材等)を有する海苔網の酸処理船では、管状部材をシート状部材の両側などに2本設けたが、第5実施形態の巻取ロール、シート状部材を有しない海苔網の酸処理船(素通し船)のように海苔網の巻き取り及び繰り出しなどに干渉しない箇所で、酸処理槽上の任意の位置に配置するものであれば任意の位置に1本(片側)だけであってもよく、また、適用する酸処理槽の形態、巻取ロールやシート状部材の有無などにより海苔網の巻き取り及び繰り出しなどに干渉しない箇所となる酸処理槽上の任意の位置に3本以上の複数本を設けてもよいものである。
更に、取付け様式も酸処理槽に対して水平位置だけでなく、垂直又は斜め位置であってもよいものである。
The acid treatment vessel of the seaweed net of the present invention has at least an acid treatment tank for accommodating the acid treatment liquid, an acid stock solution supply device for supplying the stock solution of the acid treatment liquid into the acid treatment tank, and an acid in the acid treatment tank. It is an acid treatment ship of seaweed net equipped with a control unit that detects the pH value of the treatment liquid and operates the acid stock solution supply device based on the detection value to control the acid treatment liquid to a constant pH value. The acid stock solution supply device is provided with at least one bottomed tubular member having a plurality of discharge holes for ejecting the acid stock solution at an arbitrary position on the acid treatment tank, and the tubular member. The gist is that the inner diameter, the number of discharge holes, and the hole diameter of the discharge holes are within each specific range. Therefore, the present invention is not limited to the first to fifth embodiments. The following embodiments of each modification can be adopted as long as they are not changed.
For example, in an acid-treated seaweed net having various devices (winding rolls, sheet-shaped members, etc.) of the first to fourth embodiments, two tubular members are provided on both sides of the sheet-shaped member. , Arbitrary on the acid treatment tank at a place that does not interfere with the winding and feeding of the seaweed net, such as the winding roll of the fifth embodiment and the acid processing ship (passing ship) of the seaweed net having no sheet-like member. As long as it is placed at a position, only one (one side) may be used at any position, and the seaweed net may be wound depending on the form of the acid treatment tank to be applied, the presence or absence of a winding roll or a sheet-like member, and the like. In addition, a plurality of three or more may be provided at an arbitrary position on the acid treatment tank so as not to interfere with feeding or the like.
Further, the mounting mode may be not only a horizontal position but also a vertical or diagonal position with respect to the acid treatment tank.

次に、実施例及び比較例により、本発明を更に詳述するが、本発明は下記実施例等により制限されるものではない。 Next, the present invention will be described in more detail with reference to Examples and Comparative Examples, but the present invention is not limited to the following Examples and the like.

〔実施例1~21及び比較例1~11〕
〔試験1〕
下記構成の海苔網酸処理船のテスト装置を用いて、下記表1に示す各管状部材(管状部材1~32)の内径、吐出孔の数、吐出孔の孔径、最初の吐出孔の孔径に対して最後の吐出孔の孔径の比を変動させたものを用いて、下記試験方法により、各吐出孔からの酸原液の噴出量バランスとポンプ/噴出の応答時間差について試験を行った。
[Examples 1 to 21 and Comparative Examples 1 to 11]
[Test 1]
Using the test equipment of the seaweed mesh acid treatment ship with the following configuration, the inner diameter of each tubular member (tubular members 1 to 32) shown in Table 1 below, the number of discharge holes, the hole diameter of the discharge hole, and the hole diameter of the first discharge hole were determined. On the other hand, the balance of the amount of the acid stock solution ejected from each ejection hole and the difference in the response time of the pump / ejection were tested by the following test method using the one in which the ratio of the pore diameters of the last ejection holes was varied.

(海苔網酸処理船のテスト装置の主な構成)
酸原液Z:第一製網社製、「グローゲン」
ポンプ42:電磁駆動定量ポンプEHN、イワキ社製(吐出量:1000±50ml/分)
管状部材60の大きさ等:下記表1に示す各寸法
(Main configuration of test equipment for seaweed net acid treatment ship)
Acid stock solution Z: "Grogen" manufactured by Daiichi Seisakusho
Pump 42: Electromagnetically driven metering pump EHN, manufactured by Iwaki Co., Ltd. (Discharge rate: 1000 ± 50 ml / min)
Size of tubular member 60, etc .: Each dimension shown in Table 1 below

(試験方法)
ポンプ42を始動させ、酸原液Zを管状部材60に送液し予め管内に酸原液を充填させ、ポンプ42を停止させた。その後速やかに、ポンプ42を1分間始動せしめて停止させ、管状部材の各吐出孔から噴出した酸原液を各々採取し、各吐出孔からの噴出量を測定した(2本の管状部材に分けた場合は、2本各吐出孔の合計)。この各噴出量より、最初の吐出孔と最後の吐出孔、2番目の吐出孔と最後から一つ前の吐出孔、前半の吐出孔と後半の吐出孔についての噴出量の相対差(噴出量バランス)を算出した。
また、ポンプ始動と管状部材の全吐出孔からの噴出開始の時間、ポンプ停止と管状部材の全吐出孔からの噴出停止の時間を測定し、ポンプと吐出の応答時間差を算出した。
これらの噴出量バランス、ポンプ/噴出応答時間差の各評価の目安を下記に示すと共に、その評価結果を下記表2に示す。
(Test method)
The pump 42 was started, the acid stock solution Z was sent to the tubular member 60, the pipe was filled with the acid stock solution in advance, and the pump 42 was stopped. Immediately after that, the pump 42 was started and stopped for 1 minute, the acid stock solution ejected from each discharge hole of the tubular member was collected, and the amount ejected from each discharge hole was measured (divided into two tubular members). In the case, the total of the two discharge holes). From each of these ejection amounts, the relative difference (ejection amount) between the first discharge hole and the last discharge hole, the second discharge hole and the previous discharge hole, and the first half discharge hole and the second half discharge hole. Balance) was calculated.
In addition, the time between the start of the pump and the start of ejection from all the discharge holes of the tubular member, and the time of stop of the pump and the stop of ejection from all the discharge holes of the tubular member were measured, and the difference in response time between the pump and the discharge was calculated.
The guideline for each evaluation of these ejection volume balance and pump / ejection response time difference is shown below, and the evaluation results are shown in Table 2 below.

〔評価の目安〕
噴出量バランスは、50%以下が好ましく、更に好ましくは35%以下、より好ましくは、20%未満、特に好ましくは10%未満が望ましい。
ポンプ/噴出応答時間差は、3秒未満が好ましく、更に好ましくは、2秒以下、より好ましくは、1秒以下が特に望ましい。
[Evaluation guideline]
The ejection amount balance is preferably 50% or less, more preferably 35% or less, more preferably less than 20%, and particularly preferably less than 10%.
The pump / ejection response time difference is preferably less than 3 seconds, more preferably 2 seconds or less, and more preferably 1 second or less.

〔試験2〕
図1及び図2、並びに、下記構成の海苔網の酸処理船を用いて、下記表1に示す各管状部材(管状部材1~32)の内径、吐出孔の数、吐出孔の孔径、最初の吐出孔の孔径に対して最後の吐出孔の孔径の比を変動させたものを用いて、下記試験方法により、設定したpH値と実際の酸処理槽内のpH値との乖離について試験を行った。
[Test 2]
Using the seaweed net acid treatment vessel of FIG. 1 and FIG. 2 and the seaweed net having the following configuration, the inner diameter of each tubular member (tubular members 1 to 32) shown in Table 1 below, the number of discharge holes, the hole diameter of the discharge holes, first. The difference between the set pH value and the actual pH value in the acid treatment tank was tested by the following test method using the one in which the ratio of the hole diameter of the last discharge hole to the hole diameter of the discharge hole was changed. gone.

(海苔網の酸処理船の主な構成)
酸原液Z:第一製網社製、「グローゲン」
酸処理槽15に収容の海水:800L(熊本県荒尾市有明海地先採取の海水、以下同様)
ポンプ42:電磁駆動定量ポンプEHN、イワキ社製(吐出量:1000±50ml/分)
制御部50:pH検出器51の検出値に基づいて、供給する酸原液Zの供給量を自動調節する装置。
pH検出器51:PET-M3、セムコーポレーション社製
管状部材60の大きさ等:下記表1に示す各寸法
測定用pH計:ハンディpH計「TPX-999」、東興化学研究所社製
(Main composition of nori net acid treatment ship)
Acid stock solution Z: "Grogen" manufactured by Daiichi Seisakusho
Seawater contained in acid treatment tank 15: 800L (seawater collected from the Ariake Sea, Arao City, Kumamoto Prefecture, the same applies hereinafter)
Pump 42: Electromagnetically driven metering pump EHN, manufactured by Iwaki Co., Ltd. (Discharge rate: 1000 ± 50 ml / min)
Control unit 50: A device that automatically adjusts the supply amount of the acid stock solution Z to be supplied based on the detection value of the pH detector 51.
pH detector 51: PET-M3, size of tubular member 60 manufactured by Sem Corporation: pH meter for measuring each dimension shown in Table 1 below: Handy pH meter "TPX-999", manufactured by Toko Kagaku Kenkyusho Co., Ltd.

(試験方法)
海苔網の酸処理船の酸処理槽15内の処理液pHをグローゲンを用いて2.00に予め調整した(処理液温度:18℃)。制御部50の設定pHを2.00とした。酸処理船の巻取りロールを回転させることにより撹拌しながら、この酸処理槽15に(希釈用)海水を毎分30Lを連続給水させ、そして、同液量の処理液を処理槽外に連続排水させた。この酸処理槽15内の処理液が継続的に希釈される状況(海苔養殖場の酸処理を模したもの)において、制御部50を10分間稼働させ、pH検出器51のモニターに表示されたpHを測定して、設定したpHとのpHの差(乖離)及び制御の振れ幅(最大値から最小値を引いた値)を算出した。
また、測定用ハンディpH計5台を酸処理槽15内を網羅するように5点に配置(最初の吐出孔に近い方から〈1〉、〈2〉、〈3〉、〈4〉、〈5〉の順番に配置、図8参照)させ、酸処理槽15内のpHバラツキ(各点平均における最大値から最小値を引いた値)を算出した。管状部材の本数が1本の場合は、図8上の支持部材25の上側に取り付けた。
これらの試験2の評価であるpH乖離、制御振れ幅、pHバラツキの各評価の目安、並びに、総合判定を下記に示すと共に、評価結果を下記表2に示す。
(Test method)
The pH of the treatment liquid in the acid treatment tank 15 of the acid treatment ship of the seaweed net was adjusted in advance to 2.00 using Grogen (treatment liquid temperature: 18 ° C.). The set pH of the control unit 50 was set to 2.00. While stirring by rotating the take-up roll of the acid treatment vessel, the acid treatment tank 15 is continuously supplied with 30 L of seawater (for dilution) per minute, and the same amount of treatment liquid is continuously supplied to the outside of the treatment tank. It was drained. In a situation where the treatment liquid in the acid treatment tank 15 was continuously diluted (simulating the acid treatment of a seaweed farm), the control unit 50 was operated for 10 minutes and displayed on the monitor of the pH detector 51. The pH was measured, and the difference (deviation) in pH from the set pH and the fluctuation range of control (value obtained by subtracting the minimum value from the maximum value) were calculated.
In addition, five handy pH meters for measurement are arranged at five points so as to cover the inside of the acid treatment tank 15 (from the side closest to the first discharge hole, <1>, <2>, <3>, <4>, <5> was arranged in this order (see FIG. 8), and the pH variation in the acid treatment tank 15 (the value obtained by subtracting the minimum value from the maximum value in the average of each point) was calculated. When the number of tubular members was one, it was attached to the upper side of the support member 25 on FIG.
The guideline for each evaluation of pH deviation, control fluctuation width, and pH variation, which are the evaluations of these tests 2, and the comprehensive judgment are shown below, and the evaluation results are shown in Table 2 below.

〔評価の目安〕
pH乖離は、0.03以下が好ましく、0.02以下が特に好ましい(何れも絶対値)。
制御振れ幅は、0.06以下が好ましく、より好ましくは、0.05以下、特に好ましくは、0.04以下が望ましい。
pHバラツキは、0.1以下が好ましく、より好ましくは、0.06以下、直に好ましくは、0.04以下が望ましい。
[Evaluation guideline]
The pH deviation is preferably 0.03 or less, and particularly preferably 0.02 or less (both are absolute values).
The control runout width is preferably 0.06 or less, more preferably 0.05 or less, and particularly preferably 0.04 or less.
The pH variation is preferably 0.1 or less, more preferably 0.06 or less, and directly preferably 0.04 or less.

〔総合判定〕
◎:噴出量の相対差(バランス)15%以下、ポンプ/噴出応答時間差1秒以内、pH乖離0.02以下、制御振れ幅0.05以下、pHバラツキ0.04以下
○:噴出量の相対差(バランス)20%以下、ポンプ/噴出応答時間差2秒以内、pH乖離0.02以下、制御振れ幅0.06以下、pHバラツキ0.06以下
△~○:噴出量の相対差(バランス)50%以下、ポンプ/噴出応答時間差2秒以内、pH乖離0.03以下、制御振れ幅0.06以下、pHバラツキ0.10以下
△:噴出量の相対差(バランス)60%以下、ポンプ/噴出応答時間差2秒以内、pH乖離、0.05以下、制御振れ幅が0.10以下、pHバラツキが0.15以下
×:上記△の各評価目安において、少なくとも2つ以上が△の基準を満たさないもの。
〔Comprehensive judgment〕
⊚: Relative difference (balance) of ejection amount 15% or less, pump / ejection response time difference within 1 second, pH deviation 0.02 or less, control swing width 0.05 or less, pH variation 0.04 or less ○: Relative ejection amount Difference (balance) 20% or less, pump / ejection response time difference within 2 seconds, pH deviation 0.02 or less, control swing width 0.06 or less, pH variation 0.06 or less △ ~ ○: Relative difference (balance) in ejection amount 50% or less, pump / ejection response time difference within 2 seconds, pH deviation 0.03 or less, control swing width 0.06 or less, pH variation 0.10 or less Δ: Relative difference (balance) of ejection amount 60% or less, pump / Ejection response time difference within 2 seconds, pH deviation, 0.05 or less, control fluctuation width 0.10 or less, pH variation 0.15 or less ×: In each evaluation guideline of △ above, at least two or more are based on △ criteria. Things that do not meet.

Figure 0007050505000001
Figure 0007050505000001

Figure 0007050505000002
Figure 0007050505000002

表1及び表2(試験1,2)の結果から明らかなように、本発明の実施例1~21は、本発明の範囲外となる比較例1~11に較べ、管状部材の各吐出孔噴出量の相対差が少なく、管状部材の噴出量バランスも良好であることが確認され、ポンプ始動・停止と噴出始動・停止の時間差が著しく少なく、また、ポンプ/噴出応答が良好であることが確認された。また、試験2より、設定したpH値と実際の酸処理槽内のpH値との乖離が最小限となり、且つ、酸処理槽内の濃度ムラが生じないようにして、本発明範囲の管状部材を用いることにより、十分な酸処理を効率的に行える海苔網の酸処理船が得られることが確認された。これらの結果から、内径が3~7mmであり、吐出孔の数が3~10個であり、該吐出孔の孔径が1.0~2.0mとなる管状部材が優れていることが初めて明らかとなった。更に、前記条件に加え、最初の吐出孔の孔径に対して最後の吐出孔の孔径の比が1.08~1.27倍となる管状部材(実施例2、4、5、7、10、11、17)が特に優れていることが明らかとなった。 As is clear from the results of Tables 1 and 2 (Tests 1 and 2), Examples 1 to 21 of the present invention have each discharge hole of the tubular member as compared with Comparative Examples 1 to 11 which are outside the scope of the present invention. It was confirmed that the relative difference in the ejection amount was small, the ejection amount balance of the tubular member was good, the time difference between the pump start / stop and the ejection start / stop was extremely small, and the pump / ejection response was good. confirmed. Further, from Test 2, the tubular member within the scope of the present invention is made so that the deviation between the set pH value and the actual pH value in the acid treatment tank is minimized and the concentration unevenness in the acid treatment tank does not occur. It was confirmed that an acid treatment vessel with a seaweed net that can efficiently perform sufficient acid treatment can be obtained by using. From these results, it is clear for the first time that a tubular member having an inner diameter of 3 to 7 mm, a number of discharge holes of 3 to 10, and a hole diameter of 1.0 to 2.0 m is excellent. It became. Further, in addition to the above conditions, a tubular member (Examples 2, 4, 5, 7, 10) in which the ratio of the hole diameter of the last discharge hole to the hole diameter of the first discharge hole is 1.08 to 1.27 times. It became clear that 11 and 17) were particularly excellent.

養殖中に海苔網に付着する珪藻類や赤腐れ菌などの菌類を酸処理剤(液)で効率的に酸処理を施すことができる海苔網の酸処理船に好適に利用することができる。 It can be suitably used for an acid treatment vessel for seaweed nets, which can efficiently perform acid treatment with an acid treatment agent (liquid) for fungi such as diatoms and red rot bacteria that adhere to the seaweed net during cultivation.

A 海苔網の酸処理船
10 船本体
11 酸処理液
15 酸処理槽
20 巻取ロール
25 支持部材
30 シート状部材
40 酸原液供給装置
50 制御部
60 管状部材
61a~61e 吐出孔
62 視認性を有する可撓性チューブ
A Nori net acid treatment ship 10 Ship body 11 Acid treatment liquid 15 Acid treatment tank 20 Winding roll 25 Support member 30 Sheet-like member 40 Acid stock solution supply device 50 Control unit 60 Tubular member 61a to 61e Discharge hole 62 Has visibility Flexible tube

Claims (5)

少なくとも、酸処理液を収容する酸処理槽と、該酸処理槽内に酸処理液の原液を供給する酸原液供給装置と、前記酸処理槽内の酸処理液のpH値を検出し、その検出値に基づいて前記酸原液供給装置を作動させて、酸処理液を一定のpH値に制御する制御部とを備えた海苔網の酸処理船であって、前記酸原液供給装置には、前記酸処理槽上の任意の位置に、酸原液を噴出する複数の吐出孔を有する有底筒状の管状部材を少なくとも1つ以上備えると共に、該管状部材は内径が3~8mmであり、吐出孔の数が3~10個であり、該吐出孔の孔径が1.0~2.0mmであり、前記管状部材の最初の吐出孔の孔径に対して最後の吐出孔の孔径の比が1.08~1.27倍となることを特徴とする海苔網の酸処理船。 At least, the pH value of the acid treatment tank containing the acid treatment liquid, the acid stock solution supply device for supplying the stock solution of the acid treatment liquid into the acid treatment tank, and the acid treatment liquid in the acid treatment tank is detected, and the pH value thereof is detected. A seaweed net acid treatment vessel equipped with a control unit that operates the acid stock solution supply device based on the detected value to control the acid treatment liquid to a constant pH value, and the acid stock solution supply device includes the acid stock solution supply device. At least one bottomed tubular member having a plurality of discharge holes for ejecting the acid stock solution is provided at an arbitrary position on the acid treatment tank, and the tubular member has an inner diameter of 3 to 8 mm and is discharged. The number of holes is 3 to 10, the hole diameter of the discharge hole is 1.0 to 2.0 mm, and the ratio of the hole diameter of the last discharge hole to the hole diameter of the first discharge hole of the tubular member is An acid treatment ship for seaweed nets, which is characterized by being 1.08 to 1.27 times larger . 前記管状部材の吐出孔の数(a)が4個以上の場合は、最初の吐出孔と2番目の吐出孔との間隔(X1)と、最後の吐出孔の一つ前の吐出孔と最後の吐出孔の間隔が同じ(X1=Xa-1,aは吐出孔の個数)であり、2番目の吐出孔(X2)から最後の吐出孔の一つ前の吐出孔(Xa-1)の各間隔が同じ(X2=X3=…)であることを特徴とする請求項1に記載の海苔網の酸処理船。 When the number of discharge holes (a) of the tubular member is four or more, the distance (X1) between the first discharge hole and the second discharge hole, and the discharge hole immediately before and last of the last discharge hole. The intervals between the discharge holes are the same (X1 = Xa-1, a is the number of discharge holes), and the discharge holes (Xa-1) immediately before the last discharge hole from the second discharge hole (X2) The acid-treated seaweed net according to claim 1, wherein the intervals are the same (X2 = X3 = ...). 海苔網の酸処理船には、酸処理槽内に海苔網を巻き取る巻取ロールが設けられていることを特徴とする請求項1又は2に記載の海苔網の酸処理船。 The acid treatment vessel for seaweed nets according to claim 1 or 2 , wherein the acid treatment vessel for seaweed nets is provided with a take-up roll for winding the seaweed nets in the acid treatment tank. 前記海苔網の酸処理船には、前記酸処理槽の中央部に懸架された支持部材と、該支持部材から前記酸処理槽の酸処理液に垂下するシート状部材とを有し、該シート状部材の片側又は両側に前記管状部材を備えたことを特徴とする請求項1~何れか一つに記載の海苔網の酸処理船。 The acid treatment ship of the seaweed net has a support member suspended from the central portion of the acid treatment tank and a sheet-like member hanging from the support member to the acid treatment liquid of the acid treatment tank. The acid-treated seaweed net according to any one of claims 1 to 3 , wherein the tubular member is provided on one side or both sides of the shaped member. 前記管状部材の各吐出孔には、可撓性チューブが取り付けられると共に、該可撓性チューブは、チューブ内に滴下される酸原液を視認することができるものから構成されていることを特徴とする請求項1~の何れか一つに記載の海苔網の酸処理船。 A flexible tube is attached to each discharge hole of the tubular member, and the flexible tube is characterized in that the acid stock solution dropped in the tube can be visually recognized . The acid treatment ship for seaweed net according to any one of claims 1 to 4 .
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