JP2019122355A - Acid treatment ship of laver net - Google Patents

Acid treatment ship of laver net Download PDF

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JP2019122355A
JP2019122355A JP2018013437A JP2018013437A JP2019122355A JP 2019122355 A JP2019122355 A JP 2019122355A JP 2018013437 A JP2018013437 A JP 2018013437A JP 2018013437 A JP2018013437 A JP 2018013437A JP 2019122355 A JP2019122355 A JP 2019122355A
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acid treatment
acid
stock solution
treatment tank
discharge hole
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山本 哲也
Tetsuya Yamamoto
哲也 山本
久保田 哲也
Tetsuya Kubota
哲也 久保田
啓明 藤本
Keimei Fujimoto
啓明 藤本
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Daiichi Seimo Co Ltd
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Abstract

To provide an acid treatment ship for a laver net capable of efficiently performing sufficient acid treatment with minimum deviation of a set pH value and an actual pH value in an acid treatment tank.SOLUTION: An acid treatment ship A of a laver net comprises at least: an acid treatment tank 15 for storing an acid treatment liquid; an acid stock solution supply device 40 for supplying a stock solution of the acid treatment liquid into the acid treatment tank 15; and a control device 50 for detecting a pH value of the acid treatment liquid in the acid treatment tank 15, actuating the acid stock solution supply device 40 based on the detection value, and controlling a pH value of the acid treatment liquid into a constant pH value. The acid stock solution supply device 40 comprises at least one bottomed tubular member 60 comprising a plurality of discharge holes for jetting an acid stock solution on optional positions on the acid treatment tank 15, the tubular member 60 has an inner diameter of 3-8 mm, the number of the discharge holes is 3-10, and a hole diameter of the discharge hole is 1.0-2.0 mm.SELECTED DRAWING: Figure 1

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。   TECHNICAL FIELD The present invention relates to an acid-treated ship of a seaweed net, which acid-treats fungi such as diatoms and red rot bacteria adhering to a seaweed net during aquaculture 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, an acid treatment agent having a composition comprising a combination of diatoms, red rot fungus, and other fungi adhering to nori nets spread over the sea surface in nori fish farms and combinations of organic acids such as citric acid and malic acid There are many known types and configurations of acid treatment vessels in seaweed nets that effectively treat acid.

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 general, by soaking the seaweed network in an acid-treated solution having a constant pH value, the growth of seaweeds is accelerated and the growth of each seaweed net is kept constant, so that such seaweeds are treated with good quality. An acid treatment vessel of nori nets that can harvest nori seaweed.
In the acid treatment vessel of this nori net, an acid treatment tank of a fixed capacity, a pulling up device of nori net, an acid stock solution replenishment device for replenishing an acid stock solution in the acid treatment tank, and an inside of the acid treatment tank A control unit for detecting the pH value of the acid treatment liquid and operating the replenishing device based on the detected value to maintain the acid treatment liquid at a predetermined 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。
In addition, as a small-sized nori-line acid treatment vessel, an acid treatment vessel using a box-type vessel is known. For example, as an acid treatment vessel of this small nori net,
1) An acid treatment tank provided with a nori net winding device for winding up the nori net from the sea, a chemical circulation device for circulating the chemical, and a concentration detection for detecting the concentration of the chemical circulated by the chemical circulation device U.S. Pat. No. 6,075,015, which has an apparatus and
2) An active treatment agent tank containing an active treatment agent for activating treatment of nori nets placed in a nori fish farm, treated water in which the active treatment agent and water are mixed, is contained, and the nori net is contained An apparatus for supplying a seaweed network activation treatment agent, comprising: a treatment vessel in which the activation treatment is carried out; 3) See
3) As a box-type ship capable of maintaining the acid treatment liquid at a desired pH value, an acid treatment tank for storing the acid treatment liquid, and the acid treatment tank provided in the acid treatment tank and wound with a nori net attached to the seaweed It is a box type ship provided with a pair of take-up rolls to take, and it is provided in the above-mentioned acid treatment tank, pH sensor which detects pH of the above-mentioned acid treatment liquid, A stock solution discharge unit for discharging an acid stock solution, and a stock solution supply device for automatically adjusting the supply amount of the acid stock solution to be supplied to the stock solution discharge section based on the detection value of the pH sensor; The stock solution discharge unit is provided between the pair of winding rolls, and is provided with a rod-like member provided above the acid treatment tank so as to face the liquid surface of the acid treatment liquid, and the acid treatment from the rod-like member Sheet member hanging down toward the liquid surface, and the sheet member A box-shaped vessel (e.g., a tubular vessel provided on both sides of the rod-like member) and having a plurality of discharge holes formed at predetermined intervals for discharging the acid stock solution toward the sheet member; , Patent Document 4),
4) An acid treatment tank for storing the acid treatment solution diluted with the acid stock solution, 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 network A box type ship provided in the acid treatment tank and provided with a take-up roll for taking up a seaweed network to which the seaweed adheres, comprising: a flexible sheet which is separated from and suspended from the take-up roll; An acid stock solution discharge unit for discharging the acid stock solution on the surface of the acidity sheet, and an acid stock solution supply section for feeding the acid stock solution down the surface of the flexible sheet to the acid treatment tank; When the acid treatment tank is inclined such that the lower end of the flexible sheet approaches the winding roll, the acid stock solution supply unit is more than the lower end of the flexible sheet at the liquid surface of the acid treatment liquid. Supplying the acid stock solution at a position far from the winding roll A box-type ship characterized by (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 vessel of the seaweed net of the patent documents 1-5, the pH value of the acid treatment liquid in the acid treatment tank of a fixed capacity is detected, and the pump etc. of the supply device is operated based on the detected value. The acid treatment liquid (acid stock solution etc.) in the treatment tank is supplied to the acid treatment tank through a supply pipe or a tubular member having a discharge hole, and the acid treatment liquid in the acid treatment tank has a predetermined pH value, usually pH 2 .0 was to be kept around.
However, the feed pipes and tubular members used in the above-mentioned Patent Documents 1 to 5 mainly use water pipes made of vinyl chloride or the like, so the inner diameter is as large as 13 mm or more, and the feed pipes and The hole diameter of the discharge holes formed in the tubular member was the same, and the distance (distance) between the discharge holes was the same. Therefore, a part of the acid stock solution supplied from the supply pump remains in the supply pipe or tubular member and does not drop to the set pH value, and the set pH value and the actual pH value in the acid treatment tank And the problem that sufficient acid treatment can not be performed efficiently.

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。   Moreover, in the acid treatment vessel of the seaweed mesh of Patent Documents 4 and 5, since it is a method of discharging the acid stock solution toward the sheet member, the acid stock solution for the sheet member having a large surface area in addition to remaining in the tubular member. As some of the deposits adhere and remain, the difference between the set pH value and the actual pH value in the acid treatment tank is even greater, and there is a problem that sufficient acid treatment can not be performed efficiently. ing.

特開平5−95740号公報(特許請求の範囲、図1等)JP-A-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 (The scope of utility model registration request, FIG. 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 (The scope of utility model registration request, Fig. 1 etc.) 特許第6161016号公報(特許請求の範囲、図1,2等)Patent No. 6161016 (Claims, Figs. 1 and 2, etc.) 特許第6218984号公報(特許請求の範囲、図1〜図4等)Patent No. 6218984 (claims, FIGS. 1 to 4 and the like)

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 the like, and a seaweed which acid-treats fungi such as diatoms and red rot bacteria adhering to a seaweed network during aquaculture with an acid treatment agent (liquid) In the acid treatment vessel of net, sufficient acid treatment is carried out by minimizing the deviation between the set pH value and the actual pH value in the acid treatment tank and preventing the occurrence of uneven concentration in the acid treatment tank. An object of the present invention is to provide an acid treatment vessel 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 intensive studies on the above-mentioned conventional problems etc., the present inventors at least, an acid treatment tank containing 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 control unit for detecting the pH value of the acid treatment liquid in the acid treatment tank and operating the acid stock solution supply device based on the detected value to control the acid treatment liquid to a constant pH value The acid stock solution supply device includes at least one bottomed tubular tubular member having a plurality of discharge holes for ejecting the acid stock solution at any 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 hole, and the ratio of the hole diameter of the last discharge hole to the hole diameter of the first discharge hole in a specific range, respectively. It was found that an acid treatment vessel could be obtained, and the present invention was completed. .

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 following (1)-(6).
(1) At least an acid treatment tank containing an acid treatment liquid, an acid stock solution supply device for supplying a stock solution of the acid treatment liquid into the acid treatment tank, and detecting the pH value of the acid treatment liquid in the acid treatment tank And a control unit for operating the acid stock solution supply device based on the detected value to control the acid treatment solution to a constant pH value, wherein the acid stock solution supply system for the acid stock solution comprises: And at least one or more bottomed cylindrical tubular members having a plurality of discharge holes for discharging an acid stock solution at any position on the acid treatment tank, and the tubular members have an inner diameter of 3 to 8 mm. An acid-treated vessel of a seaweed net, 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 network according to the above (1), 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. Processing ship.
(3) When the number (a) of the discharge holes of the tubular member is four or more, a distance (X 1 ) between the first discharge hole and the second discharge hole 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 , where a is the number of discharge holes), and the discharge from the second discharge hole (X 2 ) to one before the last discharge hole hole above (X a-1) each interval is equal to or the same (X 2 = X 3 = ... ) (1) or (2) seaweed networks acid treatment vessel according.
(4) The acid-treated vessel of a seaweed net is provided with a take-up roll for winding up the seaweed net in the acid treatment tank, described in any one of the above (1) to (3) Acid treatment ship of Nori net.
(5) The acid-treated vessel of the seaweed network includes a support member suspended at a central portion of the acid treatment tank, and a sheet-like member suspended from the support member to the acid treatment liquid of the acid treatment tank. The acid-treated vessel of a seaweed net according to any one of the above (1) to (4), wherein the tubular member is provided on one side or both sides of the sheet-like member.
(6) The acid of the network according to any one of the above (1) to (5), 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 ratio of the diameter of the last discharge hole to the inner diameter of the tubular member for supplying the acid stock solution, the number of discharge holes, the diameter of the discharge hole and the diameter of the first discharge hole By setting each specific range, the deviation between the set pH value and the actual pH value in the acid treatment tank is minimized, and concentration unevenness in the acid treatment tank does not occur, which is sufficient. There is provided an acid treatment vessel of a seaweed net that can efficiently carry out acid treatment.
According to the invention of claim 3, the acid-treated vessel of the seaweed network which can perform sufficient acid treatment more efficiently by further minimizing the deviation between the set pH value and the actual pH value in the acid treatment tank. Provided.
According to the invention of claims 4 and 5, it is possible to efficiently carry out sufficient acid treatment even for an acid treatment vessel of a seaweed net having various devices (winding rolls, sheet-like members).
According to the invention of claim 6, it is possible to provide an acid treatment vessel of a seaweed mesh which can reliably supply an acid stock solution into an acid treatment tank and can perform sufficient acid treatment efficiently.

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。BRIEF DESCRIPTION OF THE DRAWINGS It is drawing of the acid treatment ship of the seaweed network 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 the figure seen from the bottom side which shows an example of the tubular member used for the acid treatment ship of the seaweed net of FIG. 1, (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 the figure seen from the bottom side which shows an example of the comparison form of the tubular member used for the acid treatment ship of the nori net of FIG. 1, (b)-(d) is an acid treatment of the nori net of FIG. It is each drawing seen from the bottom side which shows the other example of the tubular member used for ships. 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 vessel of the seaweed net which shows a 2nd embodiment of the present 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 diagram 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 drawing of the acid treatment ship of the seaweed net which shows 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 an acid treatment vessel of a nori net showing the fourth embodiment of the present 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 drawing of the acid treatment ship of the seaweed net which shows 5th Embodiment of this invention, (a) is a schematic plan view, (b) is a schematic side view which shows an example of an implementation state. 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。FIG. 6 is a layout drawing in which five handy pH meters for measurement in Test 2 are arranged so as to cover an acid treatment tank of an acid treatment vessel of a nori 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.
FIG. 1 is a drawing of an acid treatment vessel of a nori net showing the first embodiment of the present invention, where (a) is a schematic plan view, (b) is a schematic front view, and FIG. 2 (a) is a nori sea of FIG. The figure seen from the bottom side which shows an example of the tubular member used for the acid treatment ship of a net | network, (b) is a schematic side view of FIG.1 (b).
As shown in FIGS. 1 (a) and 1 (b), the acid-treated vessel A of the seaweed net of the first embodiment is at least provided in a resin-made vessel body 10 made of fiber reinforced plastic such as FRP. An acid treatment tank 15 for containing the acid treatment liquid 11, a take-up roll 20 for winding a mesh (not shown) provided in the acid treatment tank 15, and a central portion of the acid treatment tank 15. The support member 25, the sheet-like member 30 hanging down from the support member 25 toward the acid treatment liquid 11 of the acid treatment tank 15, and the acid stock solution Z of the acid treatment liquid 11 is supplied into the acid treatment tank 15. The pH value of the acid stock solution feeder 40 and the pH value of the acid treatment liquid 11 in the acid treatment tank 15 are detected, and the acid stock solution feeder 40 is operated based on the detected values to keep the acid treatment liquid 11 at a constant pH value. And a control unit 50 for controlling the

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 liquid 11 is an acid stock solution of an organic acid such as citric acid or malic acid [A commercially available acid treatment agent (liquid) if there is a commercial product, and in this embodiment, "Growgen" manufactured by Daiichi Sangyo Co., Ltd.] Z is an acid dilution liquid diluted with seawater or the like and having a predetermined pH value, for example, pH 1.7 to 2.3.
A constant amount (500 to 1,000 L) of the acid treatment solution 11 is contained in the acid treatment tank 15, and the nori seaweed network (not shown) which is taken up is attached to the nori seaweed network by the immersion treatment. Acid treatment.

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 formed at the center of the ship main body 10, and contains a predetermined amount of the acid treatment liquid 11. In the spaces 16, 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 winding roll, a battery (not shown) for driving these, etc. 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 rotating shaft for taking up a nori net, and has at least one, but in the present embodiment, a pair of take-up rolls 20 are disposed at a predetermined place in the acid treatment tank 15. The take-up rolls 20, 20 are rotatably attached, and one take-up roll 20 sequentially takes up the forward mesh network when the ship body 10 advances (upper side in FIG. 1). The other take-up roll 20 takes up the rear side mesh sequentially when the ship body 10 moves backward (lower side in FIG. 1). Moreover, in this embodiment, the delivery rolls 21 and 21 used as the rotating shaft which draws | feeds a nori net to the sea side are rotatably attached to the both-sides vicinity of the supporting member 25. As shown in FIG.
The pair of winding rolls 20 and the feeding rolls 21 disposed on both sides of the support member are driven by drive units 22 and 22 each 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 formed of a rod-like member and is suspended at the central portion in the width direction of the acid treatment tank 15, and the upper surface portions on both sides of the acid treatment tank 15 via attachment members (not shown). Or directly fixed.
A sheet-like member 30 made of resin, which is a sheet-like member 30 made of soft vinyl chloride in the present embodiment, is attached to the supporting member 25 so as to descend toward the acid treatment liquid 11 of the acid treatment tank 15. It is arranged to the vicinity of the bottom in the acid treatment liquid 11 of the tank 15. A rod-like member 31 to be a weight (sink) is attached to the bottom of the sheet-like member 30.
This sheet-like member 30 serves as a member (curtain) for preventing entanglement due to direct contact between the nori nets wound around the winding roll 20 or the delivery roll 21 disposed on both sides of the sheet-like member 30. . Therefore, it is preferable that the lower part of the sheet-like member 30 be disposed to the vicinity of the bottom 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. 1 (a), the acid stock solution supply device 40 is positioned at a suitable position in the space 16 of the acid treatment tank 15 (away from the acid treatment tank to such an extent that it does not interfere with winding and unwinding For example, it is disposed in the lower space of the operator easy seat, and supplies the acid stock solution Z of the acid treatment solution 11 into the acid treatment tank 15. In the present embodiment, the stock solution supply device 40 is connected with a stock solution tank 41 for storing the stock solution Z of the acid treatment solution 11 and a line 43 from the stock solution tank 41 via a pump 42.
The control unit 50 controls the acid treatment solution 11 at an appropriate position in the acid treatment tank 15 (at a central position where the average pH of the acid treatment tank can be detected and not interfered by the feed roll, for example, near the sheet-like member). A pH detector 51 for detecting a pH value is provided, and the pump 42 of the acid stock solution supply device 40 is operated based on the detection value detected by the pH detector 51 to convert the acid of the acid treatment solution into the acid treatment tank 15 It is an apparatus for supplying the undiluted | stock solution Z and controlling an acid treatment liquid to fixed 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-made tubular member 60, in this embodiment, a FRP-made tubular member 60 is attached to both upper portions of the sheet-like member 30 in the vicinity of the support member 25 by means of a fitting 26 such as a binding band.
As shown in FIGS. 1 (b) and 2 (a) and 2 (b), the stock acid solution Z is supplied from one opening 60a to the tubular member 60, and the other end 60b is a plug member 60c. A plurality of discharge holes 61a, 61b,..., 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 has acid resistance, weather resistance, durability and the like to the acid stock solution Z other than FRP-made, and it is made of vinyl chloride , Or “PVC”, etc., and either opaque (that can not confirm the acid stock solution with the naked eye) or having visibility (the acid stock solution can be checked with the naked eye) Also, if it is transparent and semi-transparent, it is possible to visually confirm the liquid delivery state of the acid stock solution.

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, by minimizing the residual leakage and void loss in the tubular member 60 of the acid stock solution, the response time difference between the start and stop of the discharge of the pump and the discharge hole is eliminated, and the set pH value and the actual acid treatment tank The inner diameter of the tubular member 60 needs to be 3 to 8 mm so that sufficient acid treatment can be efficiently performed with a minimum deviation from the pH value of 3 and the number of discharge holes is 3 It is necessary that the number of the holes is 10 and the 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 to further eliminate the concentration unevenness of the acid treatment tank, preferably, the inner diameter of the tubular member 60 is 3 to 5 mm, and the diameter of the first discharge hole 61a is set. On the other hand, it is desirable that the ratio of the hole diameter of the last discharge hole 61e be 1.08 to 1.27.
Here, the inner diameter of the tubular member 60 refers to the diameter of the portion through which the liquid (acid stock solution) actually flows by subtracting the thickness of the tube from the diameter (outer diameter) of the tubular member 60 [FIG. Illustrated code D of a). Moreover, it is preferable that the cross section perpendicular | vertical to the longitudinal direction of the tubular member 60 is circular. Also, when the vertical cross section is elliptical, the inner diameter of the tubular member 60 refers to the longest straight line drawn through the center of the vertical cross section of the tubular member. Preferably, the tubular member has a shape in which the inner diameter does not change in the longitudinal direction.
In addition, since the length of the tubular member 60 is disposed at an arbitrary position on the acid treatment tank 15 at a location that does not interfere with winding and unwinding of the nori net, the size of the acid treatment tank 15 etc. Although it varies, it is the same as the length of the acid treatment tank 15 in the width direction, or slightly longer or slightly shorter in consideration of the mounting mode. In the present embodiment, the length in the width direction of the acid treatment tank 15 is 210 cm, and the length of the tubular member 60 is 190 cm. 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 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 is more than 8 mm, the remaining leak and void volume of the acid stock solution in the tubular member 60 increase, so that the set pH value deviates from the actual pH value in the acid treatment tank. On the other hand, when the inner diameter is less than 3 mm, it is not preferable because it becomes difficult to reduce the jet amount (total amount) and to adjust the jet amount balance of the plural discharge holes.
Further, the number of discharge holes 61 formed in the tubular member 60 varies depending on the length of the tubular member 60, ie, the size of the acid treatment tank 15 because it is disposed on the acid treatment tank 15. It is desirable that the number is 3 to 10 (per one tubular member), preferably 3 to 6, and particularly preferably 5 to 6. When the number of the discharge holes 61 is two or less, the number of discharge (including dripping) locations to the acid treatment tank 15 is small, and dissolution in the acid treatment tank 15 takes time, resulting in uneven concentration, If the number exceeds 10, the adjustment of the ejection amount balance of the plurality of ejection holes becomes complicated, which is not preferable.
Furthermore, if the hole diameter of the discharge hole is less than 1.0 mm, the discharge amount (total amount) can not be reduced and can not be uniformly distributed to the discharge holes 61, 61 ... of the tubular member 60. It becomes a factor of concentration unevenness, and on the other hand, if the hole diameter of the discharge hole is more than 2.0 mm, the pressure in the pipe tends to be insufficient, and stable pressure can be distributed to each discharge hole 61, 61 ... of the tubular member 60 This is not preferable because it causes uneven concentration in the acid treatment tank.
The ratio of the diameter of the last discharge hole 61e to the diameter of the first discharge hole 61a may be the same, but if it is less than 1.08 times, the amount of jetted out of the last discharge hole 61e will be slightly smaller. On the other hand, when the ratio of the hole diameter is more than 1.27 times, the ejection amount of the last discharge hole 61e is slightly excessive.
The relationship among the inner diameter, the number of discharge holes and the hole diameter, the ratio of the hole diameter, and the like will be described in detail in the 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。
Between the discharge holes 61a, 61b ... of the tubular member 60 may be a predetermined distance, but when the number of discharge holes is four or more, the acid stock solution can be more uniformly discharged (including dripping) 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 intervals between the second discharge hole (X 2 ) and the discharge hole (X a-1 ) immediately before the last discharge hole are the same (X 2 = X 3 = ...) is preferred.
In this embodiment, as shown in FIG. 2 (a), the acid stock solution is made more uniform from each discharge hole 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 discharge (including dripping), and the distance (X 1 ) between the first discharge hole 61a and the second discharge hole 61b; The distance (X 4 ) between the discharge hole 61 d immediately before the last discharge hole and the last discharge hole 61 e is the same, and the discharge hole just before the last discharge hole from the second discharge hole (X 2 ) It is desirable that each interval of each interval (X 3 ) of 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 this embodiment, the tubular member 60 has a length of 190 cm (total length X: one end to the other end, the same applies hereinafter), an inner diameter of 3 mm, an outer diameter of 8 mm, and five discharge holes 61a to 61e. a discharge first discharge hole 61a (central, hereinafter the same) interval between (distance X 0) is 35 cm, the first discharge hole 61a and the interval to the next discharge hole 61b (distance X 1) is 40 cm, the following The distance (distance X 2 , distance X 3 ) to the holes 61 c and 61 d is 20 cm for each, the distance (distance X 4 ) to the next discharge hole 61 e is 40 cm, and the diameter of the discharge holes 61 a to 61 d is 1. The hole diameter of 5 mm and the last discharge hole 61 e is 1.9 mm (1.27 times).
The inner diameter of the tubular member 60, the distance (distance) between the discharge holes 61a to 61e, the hole diameter (size of the holes) of each discharge hole, the number thereof, etc. It can be varied in each of the above ranges depending on the species and the like. The length (X 0 ) from the end to be the inlet of the tubular member 60 to the first discharge hole varies depending on the size of the processing tank and the manner of attachment, but the total length X is 0.12X 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 operation of the nori net by the acid treatment vessel of the nori net according to the first embodiment configured as described above will be described below. In addition, since it is the same in the case where ship body 10 advances, and the case where it reverses, in this embodiment, only the case (upper side of Drawing 1) where ship body 10 advances is explained.
After moving the ship body 10 forward with the force to take up the nori net after moving the acid treatment vessel A of nori net to the sea on which the nori net is aquacultured, the nori net will be treated with acid as it advances. The lava net which has invaded from the front into the tank 15 and has invaded is taken up sequentially by the take-up roll 20 as the take-up roll 20 is rotated by the drive of the drive unit 22. The rolled-up nori net is dipped in the acid treatment liquid 11 contained in the acid treatment tank 15 to acid-treat the nori.
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 performs feedback control of the pump 42 of the acid stock solution supply device 40 based on the detection value input from the pH detector 51 and the control threshold value set in advance. The pump 42 sucks out a predetermined amount of acid stock solution Z corresponding to the operation signal from the acid stock solution tank 41 based on the operation signal input from the control unit 50 and supplies it to the tubular members 60 and 60 through the line 44. Further, the control unit 50 can automatically adjust the supply amount of the acid stock solution Z supplied to the acid treatment liquid 11 by controlling the pump 42 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 from the acid stock solution tank 41 by the pump 42 having 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. The holes 61a, 61b,... Are discharged (dropped) into the acid treatment liquid 11. The acid stock solution Z dropped into the acid treatment solution 11 dissolves immediately in the acid treatment solution 11. The solubility is such that the acid treatment solution 11 is in a stirring state due to the circulation of water generated in the acid treatment solution 11 by shaking of the ship body 10, rotation of the winding roll 20, etc. As a result, it dissolves and diffuses in the acid treatment liquid 11 diluted with seawater in the acid treatment, whereby the pH value which has fluctuated to a high value in the acid treatment liquid 11 can be made a predetermined pH value. In addition, the display of pH value can also be confirmed on the waterproof pH display liquid crystal screen etc. (not shown) with which the control part 50 was equipped.
The nourishing net to which the acid-treated cultured nori is attached is further taken up on the take-out roll 21 after taking up on the take-up roll 20, and after being acid-treated, the nori net being wound on the delivery roll 21 is As the ship body 10 moves forward, it will be installed at the place where the unwound net was taken out and taken out of the ship body 10.

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 network of the first embodiment configured as described above, the acid stock solution supply device 40 includes a plurality of discharge holes for discharging the acid stock solution Z provided in the vicinity of the support member 25. Are set by setting the inner diameter of the tubular member 60, the number of discharge holes 61a, and the hole diameter of the discharge holes 61a to the above specific ranges. The difference between the above pH value and the actual pH value in the acid treatment tank is minimized, and it is possible to obtain an acid treatment vessel of a seaweed net that can perform sufficient acid treatment efficiently. Preferably, in addition to the above conditions, the ratio of the diameter of the last discharge hole 61e to the diameter of the first discharge hole 61a is set to the range of the above specific ratio (1.08 to 1.27 times). Furthermore, the deviation between the set pH value and the actual pH value in the acid treatment tank is extremely minimized, and it is possible to obtain an acid treatment vessel of a seaweed net that can perform sufficient acid treatment more efficiently.

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. Further preferably, 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, whereby the remaining leak or void of the acid stock solution in the tubular member 60 is obtained. By minimizing the loss, the response time difference between the start and stop of the discharge from the pump and the discharge hole is eliminated, the deviation between the set pH value and the actual pH value in the acid treatment tank is minimized, and the inside of the acid treatment tank is minimized. Thus, sufficient acid treatment can be performed more efficiently by preventing the occurrence of uneven density.

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。
(B)-(d) of Drawing 3 are each drawing seen from the bottom side which shows other examples of tubular member 60 used for an acid treatment ship of a seaweed net of the above-mentioned embodiment. FIG. 3A is a drawing of a comparative embodiment.
In FIG. 3A, the tubular member 60 (FRP material) has a length of 200 cm, an inner diameter of 3 mm, an outer diameter of 8 mm, and has two discharge holes 61a and 61b, and the distance to the first discharge hole 61a. The distance (distance X 0 ) is 70 cm, the distance (distance X 1 ) between the first discharge hole 61 a and the next discharge hole 61 b is 60 cm, the hole diameter of the discharge hole 61 a is 1.2 mm, and the last discharge hole 61 b is The hole diameter is 1.5 mm (1.25 times).
In FIG. 3B, the tubular member 60 (FRP material) has a length of 200 cm, an inner diameter of 3 mm, an outer diameter of 8 mm, and has three discharge holes 61a to 61c, and the distance to the first discharge hole 61a. The distance (distance X 0 ) is 50 cm, the distance (distance X 1 ) between the first discharge hole 61 a and the next discharge hole 61 b is 50 cm, and the distance (distance X 2 ) to the next discharge hole 61 c is 50 cm, The diameter of the discharge holes 61a to 61b is 1.2 mm, and the diameter of the last discharge hole 61c is 1.5 mm (1.25 times).
In FIG. 3C, the tubular member 60 (FRP material) has a length of 200 cm, an inner diameter of 3 mm, an outer diameter of 5 mm, and has six discharge holes 61a to 61f, and the distance to the first discharge hole 61a. The distance (distance X 0 ) is 25 cm, the distance (distance X 1 ) between the first discharge hole 61 a and the next discharge hole 61 b is 30 cm, and the distance (distance X 2 , distance X 3 ) to the next discharge holes 61 c, 61 d, 61 e The distance (distance X 4 ) is 30 cm for each, the distance (distance X 5 ) to the next discharge hole 61 f is 30 cm, the hole diameter of the discharge holes 61 a to 61 e is 1.2 mm, and the hole diameter of the last discharge hole 61 f is 1 It has become .2 or 1.3 or 1.5 or 1.6 mm (1.00 or 1.08 or 1.25 or 1.33 times).
In FIG. 3D, the tubular member 60 (transparent polyvinyl chloride material) has a length of 200 cm, an inner diameter of 5 mm, an outer diameter of 10 mm, and has six discharge holes 61a to 61f up to the first discharge hole 61a. spacing (distance X 0) is 25 cm, the first discharge hole 61a and the interval to the next discharge hole 61b (distance X 1) is 30 cm, the next discharge hole 61c, 61d, distance to 61e (distance X 2, the distance The distance (distance X 5 ) to the next discharge hole 61 f is 30 cm, X 3 , distance X 4 ) is 30 cm, the hole diameter of the discharge holes 61 a to 61 e is 1.8 mm, and the hole diameter of the last discharge hole 61 f Is 2.0 or 2.1 [comparative embodiment] 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 the main part of a seaweed net acid treatment vessel according to a second embodiment of the present invention. In the following second to fifth embodiments, the same configuration as that of the first embodiment indicates the same reference numeral in the drawings, and the description thereof will be omitted.
The acid-treated vessel B of the seaweed net according to the second embodiment of the present invention has the acid-treated solution 11 which discharges the acid stock solution Z discharged from the discharge holes 61a to 61e to the discharge holes 61a to 61e of the tubular member 60. The flexible tubes 62, 62 ... made of resin, elastomer or rubber that lead to the liquid surface are fixed, welded, attached by attachment or the like.
When the length (distance) from the lower part of the tubular members 60, 60 to the liquid surface Y is W as shown in FIG. 4A, the lengths of the flexible tubes 62, 62 ... having visibility are as shown in FIG. The length of the tubes 62a, 62a ... in this embodiment is 2/3 W, and if it is this length, the acid stock solution Z discharged from the flexible tubes 62a, 62a ... having visibility is a sheet member It will be dripped in an acid treatment liquid, without adhering to 30 further.

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。   In addition, the flexible tubes 62, 62, ... may be any one having visibility (the acid stock solution can be confirmed with the naked eye), and may be either transparent or translucent, and flexible if it is transparent or translucent. The dripping of the acid stock solution Z in the sexing tube can be visually confirmed. In addition, the flexible hole diameter (inner diameter) having visibility is the same as or larger than the hole diameter of the discharge holes 61a to 61e 61, and in the present embodiment, the inner diameter is 6 mm and transparent visual recognition made of vinyl chloride It consists of a flexible tube having elasticity.

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 treatment liquid which has been changed to a high value by the acid treatment operation is set to a predetermined pH by the operation of the acid stock solution supply device 40, the control unit 50 and the like. The inner diameter of the tubular member 60, the number of the discharge holes 61a, the diameter of the discharge holes 61a, and the diameter of the last discharge hole 61e with respect to the diameter of the first discharge hole 61a. By setting the ratio of the pore diameter to each of the above specific ranges, the difference between the set pH value and the actual pH value in the acid treatment tank is minimized, and concentration unevenness in the acid treatment tank does not occur. Therefore, sufficient acid treatment can be performed efficiently. Furthermore, in the present embodiment, since the acid stock solution Z is not discharged to the sheet-like member 30, the undiluted solution Z does not adhere to the sheet-like member 30, and the rolled-up seaweed mesh does not adhere to the sheet-like member 30. There is no contact with the remaining acid stock solution, there is no splash of acid stock solution, the acid treatment solution can reliably treat the seaweed network with the acid treatment solution, and there is no consumption of waste acid stock solution. It will be obtained.
In the second embodiment, although the length of the flexible tubes 62a, 62a... Having visibility is set to 2 / 3W, the acid stock solution in which the attachment position of the tubular members 60, 60 is discharged to the sheet member 30 If it is attached to a place where Z can not be attached, 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 is The length until contact with the liquid surface, or the length which penetrates into the acid treatment liquid 11 which is lower than the liquid level Y may be used.

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 the main part of a seaweed net acid treatment vessel according to a third embodiment of the present invention.
In the acid treatment vessel C of the seaweed net showing 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 at an upper portion of 1 to 15 cm from the liquid level Y. In this embodiment, it is provided in the upper part of 5 cm from the liquid level Y.
Also in the third embodiment, as in the first embodiment, the pH value of the acid treatment liquid which has been changed to a high value by the acid treatment operation is set to a predetermined pH by the operation of the acid stock solution supply device 40, the control unit 50 and the like. The inner diameter of the tubular member 60, the number of the discharge holes 61a, the diameter of the discharge holes 61a, and the diameter of the first discharge hole 61a are the last discharge holes 61e. By setting the ratio of the pore diameter of each to the above specific range, the difference 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. As a result, an acid treatment vessel of a seaweed net that can perform sufficient acid treatment efficiently can be obtained. Furthermore, 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-like member 30, and the rolled-up nori net does not contact the acid stock solution remaining on the sheet-like member 30, An acid treatment vessel of a seaweed net which can be acid treated with an acid treatment solution can be obtained.

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 the main part of a seaweed net acid treatment vessel according to a fourth embodiment of the present invention.
The acid treatment vessel D of the nori net according to the fourth embodiment of the present invention has a form in which the sheet-like member 30 does not exist, and the supporting members 26, 26 provided at both ends of the acid treating tank 15 The tubular members 60, 60 having the discharge holes 61a to 61e similar to those of the first embodiment are attached, which are different from the first embodiment.
Also in the fourth embodiment, it is possible to automatically adjust the pH value of the acid treatment liquid, which has been changed to a high value by the acid treatment operation, to a predetermined pH value by the operation of the acid stock solution supply device 40, the control unit 50, etc. The inner diameter of the tubular member 60, the number of the discharge holes 61a, the hole diameter of the discharge holes 61a, and the ratio of the hole diameter of the last discharge hole 61e to the hole diameter of the first discharge hole 61a are the first embodiment. By setting each specific range described in detail, the difference 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. As a result, it is possible to obtain an acid treatment vessel of a nori net which can carry out sufficient acid treatment efficiently.

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 the main part of a seaweed net acid treatment vessel according to a fifth embodiment of the present invention.
The acid treatment vessel E of the seaweed net according to the fifth embodiment of the present invention is applied to a pure-through acid treatment vessel not provided with a winding roll, and a support member 26 provided at the advancing side end of the acid treatment tank 15 The tubular member 60 [Fig. 2 (a), Fig. 3 (b) to (d), etc.] having the discharge holes 61a, 61b ... similar to those of the first embodiment is attached thereto.
Also in the fifth embodiment, it is possible to automatically adjust the pH value of the acid treatment liquid, which has been changed to a high value by the acid treatment operation, to a predetermined pH value by the operation of the acid stock solution supply device 40, the control unit 50, etc. The inner diameter of the tubular member 60, the number of discharge holes 61a, the hole diameter of the discharge holes 61a, and the ratio of the hole diameter of the last discharge hole 61c or f to the hole diameter of the first discharge hole 61a By setting each specific range described in detail in the embodiment, deviation between the set pH value and the actual pH value in the acid treatment tank is minimized, and concentration unevenness in the acid treatment tank does not occur. As a result, an acid treatment vessel of a seaweed net that can perform sufficient acid treatment efficiently 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 (penetration treatment) of the nori net by the acid treatment vessel of the nori net according to the fifth embodiment configured as described above will be described below (Fig. 7 (b)).
After moving the acid treatment vessel E of the nori net to the sea where the nori net N cultivating fish is moved, the nori net guide 71 is made to underlie the nori net N, and the ship body 10 is shown (progress When moving forward by the driving force of the outboard motor 70, as it moves forward, the seaweed net N intrudes into the acid treatment tank 15 from the front, and the invaded seaweed net N has a cylindrical shape with both ends closed, such as polyvinyl chloride. It passes under the floating body (commonly known as "Koro") 72 and is dipped in the acid treatment liquid 11 contained in the acid treatment tank 15, whereby 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 performs feedback control of the pump 42 of the acid stock solution supply device 40 based on the detection value input from the pH detector 51 and the control threshold value set in advance. The pump 42 sucks out the acid stock solution Z of a predetermined amount according to the operation signal based on the operation signal input from the control unit 50 and supplies the acid stock solution tank 41 to the tubular member 60 through the line 44. Further, the control unit 50 can automatically adjust the supply amount of the acid stock solution Z supplied to the acid treatment liquid 11 by controlling the pump 42 based on the detection value of the pH detector 51.
The acid stock solution Z sucked from the acid stock solution tank 41 by the pump 42 having received the operation signal from the pH detector 51 is supplied to the tubular member 60, and a plurality of discharge holes 61a, 61b provided in the tubular member 60. .. Are discharged (dropped) into the acid treatment liquid 11. The acid stock solution Z dropped into the acid treatment solution 11 dissolves immediately in the acid treatment solution 11. With regard to the solubility, the acid stock solution Z is water-soluble, and the acid treatment liquid 11 is produced by the circulation, etc. generated in the acid treatment liquid 11 by the propulsion of the ship main body 10, the passage of the nori net and the rotation of the roller 72. By being in a state of stirring, it dissolves and diffuses in the acid treatment liquid 11 diluted with seawater in the acid treatment, thereby setting the pH value fluctuated to a high value in the acid treatment liquid 11 to a predetermined pH value. Can. In addition, the display of pH value can also be confirmed on the waterproof pH display liquid crystal screen etc. (not shown) with which the control part 50 was equipped.
The ridged network N to which the acid-treated cultured nori is adhered passes below the roller 72 and is acid-treated, and as the ship body 10 further moves forward, it is positioned outside the ship body 10 and to the ship rear side. N will return to the original aquaculture sea level.

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 network of the present invention comprises at least an acid treatment tank for containing an acid treatment solution, an acid stock solution supply device for supplying a stock solution of the acid treatment solution into the acid treatment tank, and an acid treatment tank in the acid treatment tank. A control unit for detecting a pH value of a processing solution and operating the acid stock solution supply device based on the detected value to control the acid processing solution to a constant pH value. The acid stock solution supply device includes at least one or more bottomed cylindrical tubular members having a plurality of discharge holes for spouting the acid stock solution at any position on the acid treatment tank, and the tubular member The gist of the present invention is not limited to the first embodiment to the fifth embodiment described above, because the inner diameter, the number of discharge holes, and the hole diameter of the discharge holes are specified ranges. In the range which does not change, the embodiment of each of the following modifications can be adopted.
For example, in the case of an acid treatment vessel of a nori net having the various devices (winding rolls, sheet-like members, etc.) of the first to fourth embodiments, two tubular members are provided on both sides of the sheet-like members. , Optional components on the acid treatment tank at locations that do not interfere with winding and unwinding of the nori net like the take-up roll of the fifth embodiment and the no acid sheet ship (liner) of nori sheet having no sheet-like member It may be only one (one side) at any position as long as it is disposed at the position, and the winding of the nori net by the form of the acid treatment tank to be applied, the presence or absence of the winding roll and the sheet-like member, etc. A plurality of three or more may be provided at any position on the acid treatment tank, which is a location that does not interfere with feeding and the like.
Furthermore, the manner of attachment may be vertical or oblique as well as horizontal with respect to the acid treatment vessel.

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 by way of examples and comparative examples, but the present invention is not limited by 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 device of the seaweed mesh acid treatment vessel of the following configuration, for the inner diameter of each tubular member (tubular members 1 to 32) shown in Table 1 below, the number of discharge holes, the diameter of discharge holes, the diameter of the first discharge holes On the other hand, tests were conducted on the balance between the ejection amount of the acid stock solution from each ejection hole and the response time difference between the pump and the ejection according to the following test method using the one in which the ratio of the hole diameter of the last ejection hole 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 the test equipment of Nori fish net acid treatment vessel)
Acid stock solution Z: manufactured by Daiichi Sangyo Co., Ltd. "Glogen"
Pump 42: Electromagnetic drive metering pump EHN, manufactured by Iwaki (discharge volume: 1000 ± 50 ml / min)
Size, etc. of tubular member 60: 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 fed to the tubular member 60, the tube was previously filled with the acid stock solution, and the pump 42 was stopped. After that, the pump 42 was started and stopped for 1 minute, and the stock solutions ejected from the discharge holes of the tubular members were collected, respectively, and the amount of discharge from the discharge holes was measured (divided into two tubular members If the sum of the two holes in each case). The relative difference between the ejection amounts of the first ejection hole and the last ejection hole, the second ejection hole and the ejection hole immediately before the last, the ejection holes in the first half and the ejection holes in the second half Balance was calculated.
In addition, the time of pump start and the start of ejection from all discharge holes of the tubular member, and the time of pump stop and the stop of ejection from all discharge holes of the tubular member were measured, and the response time difference between the pump and discharge was calculated.
The indication of each evaluation of these ejection amount balance and pump / ejection response time difference is shown below, and the evaluation result is shown in the following Table 2.

〔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。
[Indication of evaluation]
The ejection amount balance is preferably 50% or less, more preferably 35% or less, more preferably less than 20%, particularly preferably less than 10%.
The pump / jet response time difference is preferably less than 3 seconds, more preferably 2 seconds or less, 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]
1 and 2 and using the acid treatment vessel of the seaweed net of 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 diameter of the discharge holes, first The test was conducted on the deviation between the set pH value and the actual pH value in the acid treatment tank by the following test method using the ratio of the diameter of the last discharge hole to the diameter of the last discharge hole was varied. went.

(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 the acid treatment vessel of nori net)
Acid stock solution Z: manufactured by Daiichi Sangyo Co., Ltd. "Glogen"
Sea water contained in the acid treatment tank 15: 800 L (Sea water collected from Ariake Sea, Arao City, Kumamoto Prefecture, and so on)
Pump 42: Electromagnetic drive metering pump EHN, manufactured by Iwaki (discharge volume: 1000 ± 50 ml / min)
Control unit 50: A device for automatically adjusting 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, manufactured by Sem Corporation, size of tubular member 60, etc .: each dimension shown in Table 1 below: pH meter for measurement: handy pH meter "TPX-999", manufactured by Toko Chemical Laboratory 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 solution in the acid treatment tank 15 of the acid treatment vessel of the seaweed mesh was adjusted to 2.00 in advance using Grogen (treatment solution temperature: 18 ° C.). The set pH of the control unit 50 is 2.00. The acid treatment tank 15 is continuously supplied with 30 L / min of seawater (for dilution) while being stirred by rotating the take-up roll of the acid treatment vessel, and the treatment liquid of the same volume is continuously supplied to the outside of the treatment tank. It was drained. The control unit 50 is operated for 10 minutes in a situation where the treatment liquid in the acid treatment tank 15 is continuously diluted (simulating the acid treatment of a nori fish farm) and displayed on the monitor of the pH detector 51. The pH was measured to calculate the difference (difference) in pH from the set pH and the fluctuation of control (maximum value minus minimum value).
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 (<1>, <2>, <3>, <4>, <4 from the side closest to the first discharge hole) The arrangement was made in the order of 5>, see FIG. 8), and pH variation in the acid treatment tank 15 (value obtained by subtracting the minimum value from the maximum value in each point average) 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 evaluations of the pH deviation, the control fluctuation range, and the pH fluctuation which are the evaluations of these tests 2 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。
[Indication of evaluation]
0.03 or less is preferable and, as for pH deviation, 0.02 or less are especially preferable (all are absolute values).
The control deviation 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 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 1 second or less, pH deviation 0.02 or less, control fluctuation width 0.05 or less, pH variation 0.04 or less ○: relative of ejection amount Difference (balance) 20% or less, Pump / jet response time difference 2 seconds or less, pH deviation 0.02 or less, control fluctuation width 0.06 or less, pH variation 0.06 or less Δ〜: Relative difference of jet amount (balance) 50% or less, pump / jet response time difference 2 seconds or less, pH deviation 0.03 or less, control fluctuation width 0.06 or less, pH variation 0.10 or less Δ: relative difference (balance) of ejection amount 60% or less, pump / Difference in ejection response time 2 seconds or less, pH deviation 0.05 or less, control fluctuation width 0.10 or less, pH variation 0.15 or less ×: In each evaluation standard of the above Δ, at least 2 or more are the reference of Δ I do not meet.

Figure 2019122355
Figure 2019122355

Figure 2019122355
Figure 2019122355

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), each of the discharge holes of the tubular member according to Examples 1 to 21 of the present invention is compared with Comparative Examples 1 to 11 falling outside the scope of the present invention. It is confirmed that the relative difference of the ejection amount is small and the ejection amount balance of the tubular member is good, the time difference between the pump start / stop and the ejection start / stop is extremely small, and the pump / ejection response is good. confirmed. Further, according to Test 2, the tubular member of the scope of the present invention is such that the difference between the set pH value and the actual pH value in the acid treatment tank is minimized and that the concentration unevenness in the acid treatment tank does not occur. It has been confirmed that the use of No. 1 can provide an acid treatment vessel of nori net which can perform sufficient acid treatment efficiently. From these results, it is apparent 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. Furthermore, in addition to the above conditions, a tubular member 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 (Examples 2, 4, 5, 7, 10, 11, 17) proved to be 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 use suitably for the acid treatment ship of the seaweed net which can acid-treat efficiently fungi, such as diatoms and red-rot fungi adhering to a seaweed net during aquaculture, with an acid treatment agent (liquid).

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 Acid Treating Ship of A-Line Mesh 10 Ship Body 11 Acid Treating Solution 15 Acid Treating Tank 20 Winding Roll 25 Support Member 30 Sheet-like Member 40 Acidic Liquid Supply Device 50 Control Unit 60 Tubular Member 61a to 61e Discharge Hole 62 Having Visibility Flexible tube

Claims (6)

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。   At least an acid treatment tank containing an acid treatment solution, an acid stock solution supply device for supplying a stock solution of the acid treatment solution into the acid treatment tank, and a pH value of the acid treatment solution in the acid treatment tank are detected. An acid treatment vessel of a nori net comprising: a control unit which operates the acid stock solution supply device based on a detected value to control the acid treatment liquid to a constant pH value, the acid stock solution supply device comprising While providing at least one bottomed cylindrical tubular member having a plurality of discharge holes for discharging an acid stock solution at any position on the acid treatment tank, the tubular member has an inner diameter of 3 to 8 mm, and discharge An acid-treated vessel for a seaweed mesh, characterized in that the number of holes is 3 to 10 and the diameter of the discharge holes is 1.0 to 2.0 mm. 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請求項1記載の海苔網の酸処理船。 The ratio of the hole diameter of the last discharge hole is 1.08 to 1.27 times the hole diameter of the first discharge hole of the said tubular member, The acid-treated ship of the seaweed network of Claim 1 characterized by the above-mentioned. 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請求項1又は2記載の海苔網の酸処理船。 When the number (a) of the discharge holes of the tubular member is four or more, the interval (X 1 ) between the first discharge hole and the second discharge hole, and the discharge hole one before the last discharge hole The distance between the last discharge holes is the same (X 1 = X a−1 , where a is the number of discharge holes), and the second discharge hole (X 2 ) to the discharge hole (X one before the last discharge hole) a-1) according to claim 1 or 2 nori network acid treatment vessel according each interval is equal to or the same (X 2 = X 3 = ... ) of. 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1〜3のいずれか一つに記載の海苔網の酸処理船。   The acid treatment vessel of a seaweed mesh is provided with a take-up roll for winding the seaweed mesh in an acid treatment tank, The acid treatment of the seaweed mesh according to any one of claims 1 to 3 boat. 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1〜4のいずれか一つに記載の海苔網の酸処理船。   The acid-treated vessel of the seaweed mesh has a support member suspended at a central portion of the acid treatment tank, and a sheet-like member suspended from the support member to the acid treatment liquid of the acid treatment tank, the sheet The said tubular member was provided in the one side or both sides of the rod-like member, The acid-treated ship of the seaweed network as described in any one of Claims 1-4 characterized by the above-mentioned. 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請求項1〜5の何れか一つに記載の海苔網の酸処理船。   A flexible tube having visibility is attached to each discharge hole of the tubular member, The acid-treated ship of seaweed mesh according to any one of claims 1 to 5.
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CN105379613A (en) 2015-11-28 2016-03-09 王谷安 Laver culturing rope capable of preventing laver culturing raft frame from being attached with hybrid algae
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JP2019201617A (en) * 2018-05-25 2019-11-28 光洋通商株式会社 Laver net treatment ship
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