JPH044849B2 - - Google Patents
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- Publication number
- JPH044849B2 JPH044849B2 JP61107189A JP10718986A JPH044849B2 JP H044849 B2 JPH044849 B2 JP H044849B2 JP 61107189 A JP61107189 A JP 61107189A JP 10718986 A JP10718986 A JP 10718986A JP H044849 B2 JPH044849 B2 JP H044849B2
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- stock solution
- concentration
- tank
- mixing
- solution
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Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、養液栽培などに用いる植物の栽培
養液調合装置に係り、特に、肥料などの栽培に必
要な養液の高濃度原液などの混合ならびに農業用
水などによる高濃度養液の希釈化に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a plant cultivation nutrient solution preparation device used for hydroponic cultivation, etc., and in particular, it relates to a plant cultivation nutrient solution preparation device for use in hydroponic cultivation, etc., and in particular, a highly concentrated undiluted solution of a nutrient solution necessary for cultivation such as fertilizer. and the dilution of highly concentrated nutrient solutions with agricultural water, etc.
植物の栽培には、土を用いて行う従来からの土
耕栽培に対して、繊維状物質などの人工的な培養
媒体に植物を植付けて、育成上必要な肥料などの
養分を水に溶かした養液を供給して栽培を行う培
地耕がある。
In contrast to conventional soil cultivation, which uses soil to cultivate plants, plants are planted in an artificial culture medium such as fibrous materials, and nutrients such as fertilizers necessary for growth are dissolved in water. There is culture cultivation in which cultivation is performed by supplying a nutrient solution.
培地耕は、土耕栽培に比較して衛生的で、栽培
植物ごとに育成上の最適条件を設定でき、また、
その栽培管理が行い易いなど、優れた特徴を有し
ているが、植物に対する養液の濃度などの管理が
極めて重要である。 Medium cultivation is more hygienic than soil cultivation, allows you to set optimal growth conditions for each cultivated plant, and
Although it has excellent characteristics such as easy cultivation management, it is extremely important to manage the concentration of the nutrient solution for the plants.
第2図は、植物の一般的な養液栽培装置の概要
を示す。この養液栽培装置は、養液混合希釈化装
置2に農業用水などの希釈水Wrとともに、養液
Wmの基礎としての肥料などを溶かした高濃度養
液(以下原液Mという)を原液タンク4から供給
し、この原液Mと希釈水Wrとを混合して原液M
を希釈化することにより、植物の栽培に適した肥
料濃度の養液Wmを得る。 FIG. 2 shows an outline of a general hydroponic apparatus for growing plants. This hydroponic cultivation device uses a nutrient solution mixing and diluting device 2 along with dilution water Wr such as agricultural water.
A highly concentrated nutrient solution (hereinafter referred to as undiluted solution M) containing dissolved fertilizer, etc. as the basis of Wm is supplied from the undiluted solution tank 4, and this undiluted solution M is mixed with dilution water Wr.
By diluting the nutrient solution Wm, a nutrient solution Wm with a fertilizer concentration suitable for growing plants is obtained.
そして、この養液Wmは、圧送ポンプや濾過器
などからなる養液供給装置6および供給管路8を
経て栽培地10に送られる。栽培地10では、供
給管路8に取り付けた複数の分岐管12を、植物
14を植付けたベツド16の近傍に配設し、各分
岐管12に対して植物単位ごとに供給ノズルとし
てのドリツプノズル18を設ける。したがつて、
供給管路8を通して圧送された養液Wmは、分岐
管12を経てドリツプノズル18から植物14の
近傍に滴下して供給される。 Then, this nutrient solution Wm is sent to the cultivation area 10 via a nutrient solution supply device 6 consisting of a pressure pump, a filter, etc., and a supply pipe line 8. In the cultivation area 10, a plurality of branch pipes 12 attached to the supply pipe line 8 are arranged near the bed 16 in which the plants 14 are planted, and a drip nozzle 18 as a supply nozzle is installed for each branch pipe 12 for each plant. will be established. Therefore,
The nutrient solution Wm pressure-fed through the supply pipe line 8 is dripped and supplied to the vicinity of the plants 14 from the drip nozzle 18 via the branch pipe 12.
このような養液栽培装置において、養液Wmの
調合は、植物14に対して最適な肥料配分および
濃度などに設定することが必要であり、その肥料
配分や濃度は、植物ごとに異なる上、その生育状
態や気象条件などによつても大きく異なつている
ので、その都度、生育データや気象データを参照
しながら、養液Wmの肥料配分や濃度を設定する
ことが必要である。
In such a hydroponic cultivation device, it is necessary to set the formulation of the nutrient solution Wm to the optimal fertilizer distribution and concentration for the plants 14, and the fertilizer distribution and concentration differ depending on the plant. Since it varies greatly depending on the growth state and weather conditions, it is necessary to set the fertilizer distribution and concentration of the nutrient solution Wm while referring to growth data and weather data each time.
従来、原液Mを希釈水Wrと混合して希釈化す
るための養液Wmの混合希釈化において、希釈水
Wrを吸入して引き込む希釈器では、希釈水Wrの
流量wrや圧力変動によつて原液Mの希釈倍率が
変動し、一定の養液Wmの濃度を得ることができ
ず、自由に濃度変更を行うことができないもので
あつた。そこで、希釈倍率が変動した場合、原液
Mの肥料濃度を変更して対応しなければならず、
非常に面倒な作業を必要としていた。 Conventionally, in mixing and diluting the nutrient solution Wm for diluting the stock solution M by mixing it with the dilution water Wr, the dilution water
In a diluter that sucks in Wr, the dilution ratio of the stock solution M fluctuates depending on the flow rate wr of the dilution water Wr and pressure fluctuations, making it impossible to obtain a constant concentration of the nutrient solution Wm, and the concentration can be changed freely. It was something that could not be done. Therefore, if the dilution ratio changes, it is necessary to respond by changing the fertilizer concentration of the stock solution M.
It required extremely tedious work.
また、従来の養液Wmの調合を自動化したもの
として、養液混合希釈化装置2に一定量の希釈水
Wrを込んだ後、その中に特定濃度の原液Mを
徐々に入れて養液Wmの濃度を濃度センサなどを
用いて監視しながら、必要な濃度を設定するもの
がある。これは、希釈水Wrを一定量単位で取り
込んで養液Wmを調合するので、濃度補正を連続
的に行う手数はないが、養液Wmの調合量が一定
量ごとに行われるので、調合した養液Wmの連続
的な供給制御を行うことができず、また、養液
Wmに一定の濃度を設定するためには、高価な濃
度センサを必要とするものであつた。 In addition, as a way to automate the conventional preparation of nutrient solution Wm, a certain amount of dilution water is added to the nutrient solution mixing and diluting device 2.
After adding Wr, a stock solution M of a specific concentration is gradually added therein, and the concentration of the nutrient solution Wm is monitored using a concentration sensor to set the required concentration. This is because the nutrient solution Wm is prepared by taking in the dilution water Wr in fixed amounts, so there is no need to continuously correct the concentration. Continuous supply control of the nutrient solution Wm cannot be performed, and the nutrient solution
In order to set a constant concentration for Wm, an expensive concentration sensor was required.
このため、濃度設定に対して希釈水Wrの流量
wrに応じた原液Mの供給量を連続的に制御して
養液Wmを得る植物の栽培養液調合方法が提案さ
れている。 For this reason, the flow rate of dilution water Wr for the concentration setting is
A method of preparing a nutrient solution for cultivating plants has been proposed in which a nutrient solution Wm is obtained by continuously controlling the supply amount of the stock solution M according to wr.
そこで、この発明は、濃度設定および希釈水の
流量に応じて調合された養液の濃度データを参酌
して適正な濃度管理を可能にした植物の栽培養液
調合装置の提供を目的とする。 SUMMARY OF THE INVENTION An object of the present invention is to provide a plant cultivation nutrient solution mixing device that enables appropriate concentration management by taking into account the concentration data of the nutrient solution prepared according to the concentration setting and the flow rate of dilution water.
この発明の植物の栽培養液調合装置は、希釈水
供給路(供給管路30)から希釈水Wrの供給を
受け、第1及び第2の原液Ma,Mbを希釈化し
て得られる養液Wmを溜める混合希釈化タンク2
2と、この混合希釈化タンクに供給すべき前記第
1の原液を溜める第1の原液タンク28Aと、前
記混合希釈化タンクに供給すべき前記第2の原液
を溜める第2の原液タンク28Bと、前記第1の
原液タンクと前記混合希釈化タンクとの間の原液
供給路に設置されて前記第1の原液を前記混合希
釈化タンクに供給する第1の定量吐出器26A
と、前記第2の原液タンクと前記混合希釈化タン
クとの間の原液供給路に設置されて前記第2の原
液を前記混合希釈化タンクに供給する第2の定量
吐出器26Bと、前記第1または第2の定量吐出
器を駆動する駆動手段(定量吐出器駆動回路3
2)と、前記希釈水供給路に設置されて前記希釈
水の流量を検出する流量センサ20と、前記混合
希釈化タンクの底部から前記養液ポンプ(撹拌ポ
ンプ27)で引いて前記混合希釈化タンク内に戻
して前記混合希釈化タンク内の養液を撹拌する撹
拌手段(撹拌管路25)と、前記混合希釈化タン
クに設置されて前記養液中のイオン量に基づく電
気伝導度を以て前記養液の濃度を検出する濃度セ
ンサ23と、前記流量センサからの流量データ
と、予め栽培条件によつて設定される濃度データ
とから前記混合希釈化タンクに供給すべき前記第
1または第2の原液の供給量を算出する原液量演
算部241が設置され、この原液量演算部で算出
された原液量を前記濃度センサで得られた濃度デ
ータで補正する原液量補正部242が設置され、
この原液量補正部で補正された補正原液量に基づ
く制御出力を発生し、この制御出力に応じて前記
駆動手段を通して前記第1または第2の定量吐出
器を動作させ、前記第1または第2の原液または
双方の原液を前記混合希釈化タンクに供給させる
原液量制御装置24とを備えたことを特徴とする
ものである。
The plant cultivation nutrient solution mixing device of the present invention receives dilution water Wr from a dilution water supply line (supply pipe line 30), and obtains a nutrient solution Wm by diluting the first and second stock solutions Ma and Mb. Mixing dilution tank 2 that stores
2, a first stock solution tank 28A that stores the first stock solution to be supplied to the mixed dilution tank, and a second stock solution tank 28B that stores the second stock solution that should be supplied to the mixing dilution tank. , a first quantitative discharger 26A installed in the stock solution supply path between the first stock solution tank and the mixing and diluting tank to supply the first stock solution to the mixing and diluting tank;
and a second quantitative discharger 26B installed in the stock solution supply path between the second stock solution tank and the mixing dilution tank and supplying the second stock solution to the mixing and dilution tank; Driving means for driving the first or second metering dispenser (metering dispenser drive circuit 3
2), a flow rate sensor 20 installed in the dilution water supply path to detect the flow rate of the dilution water, and a flow rate sensor 20 that is installed in the dilution water supply path to detect the flow rate of the dilution water; a stirring means (stirring pipe line 25) for returning the nutrient solution in the mixing and diluting tank to the tank; The concentration sensor 23 detects the concentration of the nutrient solution, the flow rate data from the flow rate sensor, and the concentration data set in advance according to the cultivation conditions are used to determine whether the first or second amount to be supplied to the mixing dilution tank is determined. A stock solution amount calculation unit 241 is installed to calculate the supply amount of the stock solution, and a stock solution amount correction unit 242 is installed to correct the stock solution amount calculated by the stock solution amount calculation unit using the concentration data obtained by the concentration sensor.
The stock solution amount correction unit generates a control output based on the corrected stock solution amount, and operates the first or second metering dispenser through the drive means in accordance with the control output, and The present invention is characterized by comprising a stock solution amount control device 24 for supplying the stock solution or both stock solutions to the mixing and dilution tank.
この栽培養液調合装置によれば、養液Wmの濃
度設定および希釈水Wrの流量wrに対して必要な
原液量mnが得られるが、この原液量mnを養液
Wmの濃度データを参酌して補正し、適正な原液
量moを設定し、この原液量moに設定された原液
Mと希釈水Wrとを混合するので、希釈水Wrの流
量変動に即応して原液量moが制御されるととも
に、最終出力の養液Wmの濃度を常に監視しつ
つ、設定された濃度の養液Wmの調合が連続的に
行われる。したがつて、このようにすれば、養液
Wmの濃度を精密に制御し、安定した濃度を維持
することができる。
According to this cultivation nutrient solution mixing device, the necessary stock solution amount mn can be obtained for the concentration setting of the nutrient solution Wm and the flow rate wr of the dilution water Wr.
The concentration data of Wm is taken into account and corrected, an appropriate stock solution volume mo is set, and the stock solution M set to this stock solution volume mo is mixed with the dilution water Wr, so it can immediately respond to fluctuations in the flow rate of the dilution water Wr. While the raw solution amount mo is controlled, the concentration of the final output nutrient solution Wm is constantly monitored, and the nutrient solution Wm having a set concentration is continuously prepared. Therefore, if you do this, the nutrient solution
It is possible to precisely control the concentration of Wm and maintain a stable concentration.
この場合、養液Wmの調合は、複数の原液Ma,
Mbを用いる場合には各原液Ma,Mbおよび希釈
水Wrの混合希釈化、また、単一の原液Mを用い
る場合にはその原液Mと希釈水Wrとの混合希釈
化をいう。 In this case, the preparation of the nutrient solution Wm consists of multiple stock solutions Ma,
When using Mb, this refers to mixing and diluting each of the stock solutions Ma, Mb and dilution water Wr, and when using a single stock solution M, mixing and diluting the stock solution M and dilution water Wr.
そして、この栽培養液調合装置では、原液Mと
希釈水Wrとを混合して原液Mを希釈化する混合
希釈化タンク22を設置し、この混合希釈化タン
ク22中の養液Wmを撹拌する撹拌手段(撹拌管
路25)を設置すれば、養液Wmを撹拌しつつ濃
度検出ができるので、濃度制御を精密に行うこと
ができる。 In this cultivation nutrient solution mixing device, a mixing and diluting tank 22 for diluting the stock solution M by mixing the stock solution M and dilution water Wr is installed, and the nutrient solution Wm in this mixing and dilution tank 22 is stirred. If a stirring means (stirring pipe 25) is installed, the concentration can be detected while stirring the nutrient solution Wm, so that the concentration can be precisely controlled.
第1図は、この発明の植物の栽培溶液調合装置
の実施例を示す。
FIG. 1 shows an embodiment of the plant cultivation solution preparation device of the present invention.
特定濃度の養液Wmを得るための希釈水Wrに
は、たとえば、地下水、雨水などの農業用水を用
いる。この希釈水Wrは、図示していないタンク
などから希釈水供給路としての供給管路30を通
して連続的に供給されるが、供給管路30の途上
に、希釈水Wrの流量wrを検出する流量検出手段
として流量センサ20が設置され、この流量セン
サ20によつて希釈水Wrの流量wrが電気的に検
出される。 For example, agricultural water such as groundwater or rainwater is used as the dilution water Wr for obtaining the nutrient solution Wm of a specific concentration. This dilution water Wr is continuously supplied from a tank or the like (not shown) through a supply pipe line 30 serving as a dilution water supply line. A flow rate sensor 20 is installed as a detection means, and the flow rate wr of the dilution water Wr is electrically detected by this flow rate sensor 20.
Vwrは、希釈水Wrの流量wrを表わす流量信号
を示す。 Vwr indicates a flow rate signal representing the flow rate wr of the dilution water Wr.
この希釈水Wrは、第1および第2の原液Ma,
Mbと混合するための混合希釈器として設置され
た混合希釈化タンク22に供給される。そして、
この混合希釈化タンク22には、その内部の養液
Wmを底側から取り出して再び混合希釈化タンク
22に戻すことにより、養液Wmを撹拌する撹拌
手段としての撹拌管路25が設けられている。撹
拌管路25には養液Wmを循環させる撹拌ポンプ
27が設置されており、養液Wmは混合希釈化タ
ンク22から取り出されてその上方から落下し撹
拌される。この結果、原液Ma,Mbと希釈水Wr
とが混合されて、希釈水Wrによる原液Ma,Mb
の希釈化が速やかに行われる。 This dilution water Wr contains the first and second stock solutions Ma,
It is supplied to a mixing dilution tank 22 installed as a mixing diluter for mixing with Mb. and,
This mixed dilution tank 22 has a nutrient solution inside it.
A stirring pipe line 25 is provided as a stirring means for stirring the nutrient solution Wm by taking out Wm from the bottom side and returning it to the mixing dilution tank 22 again. A stirring pump 27 for circulating the nutrient solution Wm is installed in the stirring pipe 25, and the nutrient solution Wm is taken out from the mixing and dilution tank 22, falls from above, and is stirred. As a result, the stock solutions Ma, Mb and dilution water Wr
are mixed, and the stock solution Ma, Mb with dilution water Wr
dilution takes place quickly.
混合希釈化タンク22に供給するための第1お
よび第2の肥料原液を溜める原液貯留手段として
の第1および第2の原液タンク28A,28Bが
設置されており、これら原液タンク28A,28
Bの原液Ma,Mbは、電気的に制御される原液
供給手段としての第1および第2の定量吐出器2
6A,26Bを介して混合希釈化タンク22に供
給される。原液Ma,Mbの混合希釈化タンク2
2への供給は、たとえば、定量吐出器26A,2
6Bを通して必要な量の原液MaまたはMbが重
力または特定の圧力によつて滴下するように設定
する。 First and second stock solution tanks 28A, 28B are installed as stock solution storage means for storing first and second fertilizer stock solutions to be supplied to the mixing dilution tank 22, and these stock solution tanks 28A, 28
The stock solutions Ma and Mb of B are supplied to first and second metering dispensers 2 as electrically controlled stock solution supply means.
It is supplied to the mixing dilution tank 22 via 6A and 26B. Mixing dilution tank 2 for stock solutions Ma and Mb
The supply to 2 is, for example, by metering dispenser 26A, 2
Set the required amount of stock solution Ma or Mb to drip through 6B by gravity or a specific pressure.
また、混合希釈化タンク22には、養液Wmの
濃度を検出するための濃度検出手段として養液
Wmの濃度を電気的に検出する濃度センサ23が
設置されている。周知のように、養液Wm中のイ
オン量が肥料濃度に依存し、それが電気伝導度に
比例していることから、養液Wm中に電極を浸
し、その電極間に流れる電流値を測定する手段と
して濃度センサ23が用いられる。肥料等を水に
溶かすと、イオン化し、水の電気伝導度が変化す
る。この電気伝導度によつて肥料濃度を測定する
ことができるが、電気伝導度は温度が上昇すると
高くなるので、実際には温度補正によつて養液
Wmの濃度を算出する。 The mixing dilution tank 22 also includes a nutrient solution as a concentration detection means for detecting the concentration of the nutrient solution Wm.
A concentration sensor 23 is installed to electrically detect the concentration of Wm. As is well known, the amount of ions in the nutrient solution Wm depends on the fertilizer concentration, which is proportional to the electrical conductivity. Therefore, an electrode is immersed in the nutrient solution Wm and the value of the current flowing between the electrodes is measured. A concentration sensor 23 is used as a means to do this. When fertilizers are dissolved in water, they become ionized and the electrical conductivity of the water changes. Fertilizer concentration can be measured by this electrical conductivity, but since electrical conductivity increases as the temperature rises, it is actually possible to measure the fertilizer concentration by temperature correction.
Calculate the concentration of Wm.
そして、流量センサ20で得られた流量信号
Vwrは、原液量制御手段として設置された原液
量制御装置24の原液量演算部241に加えられ
る。原液量演算部241は、刻々と変化する流量
信号Vwrによつて得られる流量データと、必要
に応じて設定された濃度Xnを表わす濃度データ
とから、その濃度Xnを得るのに必要な原液量mn
を算出する。たとえば、この原液量演算部241
は、流量データと濃度データに対して、流量デー
タに応じた原液量データを記憶した記憶手段を設
置しておき、流量データと濃度データの入力によ
つて、必要な原液量データを読み出すようにす
る。 Then, the flow rate signal obtained by the flow rate sensor 20
Vwr is applied to the stock solution amount calculation section 241 of the stock solution amount control device 24 installed as a stock solution amount control means. The stock solution amount calculation unit 241 calculates the stock solution amount necessary to obtain the concentration Xn from the flow rate data obtained by the constantly changing flow rate signal Vwr and the concentration data representing the concentration Xn set as necessary. mn
Calculate. For example, this stock solution amount calculation section 241
For the flow rate data and concentration data, a storage means is installed that stores the raw solution volume data according to the flow rate data, and the necessary raw solution volume data is read out by inputting the flow rate data and concentration data. do.
この原液量演算部241によつて算出された原
液量mnを表わす原液量信号Vmnは、養液Wmの
濃度に応じて適正な原液量moに補正する原液量
補正部242に加えられる。原液量補正部242
は、濃度センサ23からの濃度信号Vnと設定濃
度信号Xnとを比較してその偏差を求め、その偏
差を用いて原液量演算部241からの原液量mn
を表わす原液量信号Vmnを補正して、適正な原
液量moを表わす原液量信号Vmoを出力する。 The stock solution amount signal Vmn representing the stock solution amount mn calculated by the stock solution amount calculation unit 241 is applied to the stock solution amount correction unit 242 which corrects the stock solution amount mo to an appropriate stock solution amount according to the concentration of the nutrient solution Wm. Stock solution amount correction section 242
compares the concentration signal Vn from the concentration sensor 23 and the set concentration signal
The stock solution amount signal Vmn representing the stock solution amount is corrected to output the stock solution amount signal Vmo representing the appropriate stock solution amount mo.
また、原液量補正部242は、原液量補正を特
定時間行つても、設定濃度と実際の養液Wmの濃
度との間の誤差が大きくなり、その補正が行われ
ない場合には、その誤差が一定値以上となつたと
きに濃度異常信号Vxを発生する。このような濃
度異常は、たとえば、原液Ma,Mbの不足や定
量吐出器26A,26Bの故障などによつて生じ
る。この濃度異常信号Vxを取り出して濃度異常
警報器31を駆動し、その濃度異常を告知させる
ことができる。濃度異常警報器31は、ランプな
どの光学的手段、ブザーなどの音響発生手段など
で構成できる。 In addition, even if the stock solution amount correction unit 242 corrects the stock solution amount for a specific period of time, the error between the set concentration and the actual concentration of the nutrient solution Wm becomes large, and if the correction is not performed, the error When the concentration exceeds a certain value, a concentration abnormality signal Vx is generated. Such a concentration abnormality occurs, for example, due to a shortage of the stock solutions Ma and Mb, a failure of the metering dispensers 26A and 26B, and the like. This concentration abnormality signal Vx can be extracted to drive the concentration abnormality alarm 31 to notify the concentration abnormality. The concentration abnormality alarm 31 can be configured with optical means such as a lamp, sound generating means such as a buzzer, and the like.
そして、原液量補正部242で得られた原液量
moを表わす原液量信号Vmoは、原液量供給制御
部243に加えられて、必要な原液量moを供給
するための原液制御信号Vcmを発生する。この
場合、たとえば、原液量信号Vmoに基づいて原
液Ma,Mbの配合比率も同時に演算し、たとえ
ば、濃度データに応じて自動的に各原液Ma,
Mbの配合比率を設定すれば、濃度の決定に対し
て配合比が得られる。したがつて、原液制御信号
Vcmは、必要な濃度を設定するための原液Ma,
Mbの量と、その配合比率を表わすデータ信号で
ある。 Then, the amount of stock solution obtained by the stock solution amount correction unit 242
The stock solution amount signal Vmo representing mo is applied to the stock solution amount supply control section 243 to generate the stock solution control signal Vcm for supplying the necessary stock solution amount mo. In this case, for example, the blending ratio of the stock solutions Ma and Mb is calculated simultaneously based on the stock solution volume signal Vmo, and for example, each stock solution Ma, Mb is automatically calculated according to the concentration data.
By setting the blending ratio of Mb, the blending ratio can be obtained for determining the concentration. Therefore, the stock control signal
Vcm is the stock solution Ma for setting the required concentration,
This is a data signal representing the amount of Mb and its blending ratio.
原液制御信号Vcmは、原液供給駆動手段とし
て設置された定量吐出器駆動回路32に加えら
れ、定量吐出器駆動回路32は原液制御信号
Vcmに応じた駆動信号Va,Vbを出力して各定量
吐出器26A,26Bに加える。定量吐出器26
A,26Bは、原液制御信号Vcmに設定された
原液Ma,Mbの供給比率に対して定量吐出器2
6A,26Bの動作時間が制御されて、希釈水
Wrの流量wrに対して設定濃度Xnを得るに必要
な量の原液Maまたは原液Mbあるいは双方が混
合希釈化タンク22に供給される。 The stock solution control signal Vcm is applied to a metering dispenser drive circuit 32 installed as a stock solution supply drive means, and the metering dispenser drive circuit 32 receives the stock solution control signal.
Drive signals Va and Vb corresponding to Vcm are output and applied to each metering dispenser 26A and 26B. Fixed amount dispenser 26
A, 26B indicate the fixed quantity dispenser 2 for the supply ratio of the stock solutions Ma, Mb set in the stock solution control signal Vcm.
The operation time of 6A and 26B is controlled, and the dilution water
An amount of stock solution Ma or stock solution Mb, or both, necessary to obtain the set concentration Xn with respect to the flow rate wr of Wr is supplied to the mixing dilution tank 22.
供給された原液Ma,Mbは、混合希釈化タン
ク22の内部で希釈水Wrと撹拌されて必要な濃
度の養液Wmが得られ、栽培地10側に供給路3
4を通して供給される。その場合、養液Wmは、
第2図に示したように、養液供給装置6によつて
栽培地に必要な圧送圧力を以て送られる。 The supplied stock solutions Ma and Mb are stirred with the dilution water Wr inside the mixing and dilution tank 22 to obtain the nutrient solution Wm of the required concentration, and the supply channel 3 is passed to the cultivation area 10 side.
Supplied through 4. In that case, the nutrient solution Wm is
As shown in FIG. 2, the nutrient solution is sent to the cultivation area with the necessary pressure by the nutrient solution supply device 6.
したがつて、このような養液調合装置によれ
ば、養液Wmの原液濃度が設定されると、希釈水
Wrの流量wrに応じて必要な量の原液Ma,Mbを
供給して調合し、希釈水Wrの流量変動に即応し
て必要な原液Ma,Mbの供給量を制御するとと
もに、設定濃度と養液Wmの濃度とを比較してそ
の偏差を求め、その偏差に応じて原液量mnを適
正な原液量moに補正するので、常に安定した濃
度の養液Wmが得られる。そして、原液量制御装
置24は、マイクロコンピユータなどの演算処理
装置によつて構成し、原液量の制御を行うことが
できる。 Therefore, according to such a nutrient solution mixing device, once the concentration of the nutrient solution Wm is set, the dilution water is
The required amount of stock solutions Ma and Mb is supplied and mixed according to the flow rate wr of Wr, and the supply amount of the necessary stock solutions Ma and Mb is controlled immediately in response to fluctuations in the flow rate of dilution water Wr. Since the concentration of the solution Wm is compared with the concentration of the solution Wm to find the deviation, and the stock solution amount mn is corrected to the appropriate stock solution amount mo according to the deviation, the nutrient solution Wm with a stable concentration can always be obtained. The stock solution amount control device 24 is constituted by an arithmetic processing device such as a microcomputer, and can control the stock solution amount.
ところで、この植物の栽培養液の調合におい
て、原液を希釈する方法は、先ず希釈水の流量を
検出し、設定された濃度になるように理論値を出
し、定量吐出器をフイード・フオワード制御を行
つている。この関係は、濃度データに応じた駆動
信号Va,Vbを得ていることから明らかである。
即ち、この制御を行う場合、流量計、定量突出
器、肥料原液濃度に誤差があるため、設定された
濃度に希釈できるとは限らない。このため、希釈
された養液濃度を濃度センサで測定し、その測定
値と設定濃度とを比較し、その差を算出すること
が必要となる。このような差の算出は、次回の希
釈動作に参酌され、前回の誤差を補正するように
理論値を補正してフイード・フオワード制御を行
うのである。植物の栽培では、迅速な制御は不要
であり、多少の誤差があつても、それが枯死等に
繋がるものではなく、このような緩やかな制御が
可能である。そして、このような理論値の補正を
繰り返すことで、誤差の無い理想的な希釈が可能
になる。この栽培養液の調合は、基本的にはフイ
ード・フオワード制御を行つているが、用いられ
ている機器の誤差をフイードバツクして理論値即
ち、目標値を補正している点で一種の学習制御を
行つているのである。 By the way, in preparing this plant cultivation nutrient solution, the method of diluting the stock solution is to first detect the flow rate of the dilution water, calculate the theoretical value so that the set concentration is achieved, and then control the metering discharge device using feed forward control. I'm going. This relationship is clear from the fact that drive signals Va and Vb are obtained according to the density data.
That is, when performing this control, it is not always possible to dilute to the set concentration because there is an error in the flow meter, metering ejector, and concentration of the undiluted fertilizer solution. Therefore, it is necessary to measure the concentration of the diluted nutrient solution with a concentration sensor, compare the measured value with a set concentration, and calculate the difference. Calculation of such a difference is taken into account in the next dilution operation, and the theoretical value is corrected to correct the previous error to perform feed forward control. In the cultivation of plants, rapid control is not necessary, and even if there is some error, it will not lead to withering or death, and such gentle control is possible. By repeating such correction of the theoretical value, ideal dilution without error becomes possible. The preparation of this cultivation nutrient solution basically uses feed-forward control, but it is also a kind of learning control in that the theoretical value, that is, the target value, is corrected by feeding back the errors of the equipment used. This is what we are doing.
なお、実施例では、第1および第2の原液タン
ク28A,28Bを設置して二種の原液Ma,
Mbを用いた場合について説明したが、予め必要
な成分の肥料を配合して必要な原液タンクを設定
し、または、肥料間の化合による不都合を回避す
るために肥料ごとに原液タンクを設置して、肥料
を濃度設定に応じて配合してもよい。 In the embodiment, the first and second stock solution tanks 28A and 28B are installed to store two types of stock solutions Ma,
We have explained the case of using Mb, but it is possible to mix fertilizers with the necessary ingredients in advance and set up the necessary stock solution tank, or to install a stock solution tank for each fertilizer to avoid inconveniences caused by combinations of fertilizers. , fertilizer may be mixed according to the concentration setting.
また、この発明は、第1の原液タンク28Aに
肥料原液を貯留し、第2の原液タンク28BにPH
濃度補正原液を貯留すれば、PH濃度の補正に利用
できる。 Further, in this invention, the fertilizer stock solution is stored in the first stock solution tank 28A, and the PH is stored in the second stock solution tank 28B.
If the concentration correction stock solution is stored, it can be used to correct the PH concentration.
以上説明したように、この発明によれば、養液
の濃度設定に応じて希釈水の流量に対して必要な
原液量が演算され、その演算結果に基づいて混合
希釈化タンクに供給する原液量を制御するので、
希釈水の流量の変動に即応して原液量を制御でき
るとともに、設定濃度の養液濃度とを比較してそ
の誤差によつて原液量を補正するので、設定され
た原液濃度の養液を混合、希釈化して連続的に調
合して培地に供給でき、しかも、養液濃度の適正
化を図ることができ、植物の育成を図ることがで
きる。
As explained above, according to the present invention, the amount of stock solution required for the flow rate of dilution water is calculated according to the concentration setting of the nutrient solution, and the amount of stock solution to be supplied to the mixing and dilution tank based on the calculation result. Since we control
The amount of stock solution can be controlled immediately in response to fluctuations in the flow rate of dilution water, and the amount of stock solution is compared with the set concentration of nutrient solution and corrected according to the error, so it is possible to mix nutrient solution with the set concentration of stock solution. The nutrient solution can be diluted and continuously prepared and supplied to the culture medium, and the concentration of the nutrient solution can be optimized, thereby facilitating the growth of plants.
第1図はこの発明の植物の栽培養液調合装置の
実施例を示すブロツク図、第2図は植物の一般的
な養液栽培装置の概要を示すブロツク図である。
Wm……養液、Wr……希釈水、Ma……第1の
原液、Mb……第2の原液、20……流量セン
サ、22……混合希釈化タンク、23……濃度セ
ンサ、24……原液量制御装置、25……撹拌管
路(撹拌手段)、26A……第1の定量吐出器、
26B……第2の定量吐出器、27……撹拌ポン
プ(撹拌手段)、28A……第1の原液タンク、
28B……第2の原液タンク、30……供給管路
(希釈水供給路)、31……濃度異常警報器、32
……定量吐出器駆動回路(駆動手段)、34……
供給路(養液供給路)、241……原液量演算部、
242……原液量補正部。
FIG. 1 is a block diagram showing an embodiment of the plant cultivation nutrient solution mixing device of the present invention, and FIG. 2 is a block diagram showing an outline of a general plant nutrient solution mixing device. Wm... Nutrient solution, Wr... Dilution water, Ma... First stock solution, Mb... Second stock solution, 20... Flow rate sensor, 22... Mixing dilution tank, 23... Concentration sensor, 24... ...Natural liquid amount control device, 25...Stirring pipe line (stirring means), 26A...First metering dispenser,
26B...Second quantitative discharge device, 27...Stirring pump (stirring means), 28A...First stock solution tank,
28B... Second stock solution tank, 30... Supply pipe line (dilution water supply line), 31... Concentration abnormality alarm, 32
...Quantitative dispenser drive circuit (drive means), 34...
Supply path (nutrient solution supply path), 241... Raw solution amount calculation section,
242...Standard solution amount correction section.
Claims (1)
及び第2の原液を希釈化して得られる養液を溜め
る混合希釈化タンクと、 この混合希釈化タンクに供給すべき前記第1の
原液を溜める第1の原液タンクと、 前記混合希釈化タンクに供給すべき前記第2の
原液を溜める第2の原液タンクと、 前記第1の原液タンクと前記混合希釈化タンク
との間の原液供給路に設置されて前記第1の原液
を前記混合希釈化タンクに供給する第1の定量吐
出器と、 前記第2の原液タンクと前記混合希釈化タンク
との間の原液供給路に設置されて前記第2の原液
を前記混合希釈化タンクに供給する第2の定量吐
出器と、 前記第1または第2の定量吐出器を駆動する駆
動手段と、 前記希釈水供給路に設置されて前記希釈水の流
量を検出する流量センサと、 前記混合希釈化タンクの底部から前記養液をポ
ンプで引いて前記混合希釈化タンク内に戻して前
記混合希釈化タンク内の前記養液を撹拌する撹拌
手段と、 前記混合希釈化タンクに設置されて前記養液中
のイオン量に基づく電気伝導度を以て前記養液の
濃度を検出する濃度センサと、 前記流量センサからの流量データと、予め栽培
条件によつて設定される濃度データとから前記混
合希釈化タンクに供給すべき前記第1または第2
の原液の供給量を算出する原液量演算部が設置さ
れ、この原液量演算部で算出された原液量を前記
濃度センサで得られた濃度データで補正する原液
量補正部が設置され、この原液量補正部で補正さ
れた補正原液量に基づく制御出力を発生し、この
制御出力に応じて前記駆動手段を通して前記第1
または第2の定量吐出器を動作させ、前記第1ま
たは第2の原液または双方の原液を前記混合希釈
化タンクに供給される原液量制御装置と、 を備えたことを特徴とする植物の栽培養液調合装
置。 2 前記原液量制御装置は、設定濃度に対して養
液濃度の誤差が大きくなつたとき、濃度異常信号
を発生するように構成し、前記濃度異常信号によ
つて警報器を動作させるようにしたことを特徴と
する特許請求の範囲第1項に記載の植物の栽培養
液調合装置。[Claims] 1. Receiving dilution water from the dilution water supply path,
and a mixing dilution tank that stores a nutrient solution obtained by diluting a second stock solution; a first stock solution tank that stores the first stock solution to be supplied to the mixing and dilution tank; a second stock solution tank for storing the second stock solution to be supplied; and a stock solution supply path between the first stock solution tank and the mixing and dilution tank for mixing and diluting the first stock solution. a first fixed-rate dispenser for supplying the liquid to the tank; and a second liquid dispensing device installed in the liquid supply path between the second liquid liquid tank and the mixing and diluting tank to supply the second liquid liquid to the mixing and diluting tank. 2, a driving means for driving the first or second fixed quantity dispenser, a flow rate sensor installed in the dilution water supply path to detect the flow rate of the dilution water, and the mixing dilution tank. stirring means for stirring the nutrient solution in the mixing and diluting tank by pulling the nutrient solution from the bottom of the mixing and diluting tank with a pump, and stirring the nutrient solution in the mixing and diluting tank; a concentration sensor that detects the concentration of the nutrient solution using electrical conductivity based on the amount of ions; and a concentration sensor that supplies the nutrient solution to the mixed dilution tank from the flow rate data from the flow rate sensor and the concentration data set in advance according to the cultivation conditions. Should the first or second
A stock solution amount calculation section is installed to calculate the supply amount of the stock solution, and a stock solution amount correction section is installed to correct the stock solution amount calculated by the stock solution amount calculation section using the concentration data obtained by the concentration sensor. A control output is generated based on the corrected stock solution amount corrected by the amount correction section, and the first
or a stock solution amount control device that operates a second quantitative discharger to supply the first stock solution, the second stock solution, or both stock solutions to the mixing dilution tank. Nutrient solution mixing device. 2. The stock solution amount control device is configured to generate an abnormal concentration signal when the error in the concentration of the nutrient solution becomes large with respect to the set concentration, and the alarm is activated by the abnormal concentration signal. A plant cultivation nutrient solution preparation device according to claim 1, characterized in that:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61107189A JPS62262922A (en) | 1986-05-10 | 1986-05-10 | Preparation of plant culture nutrient solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61107189A JPS62262922A (en) | 1986-05-10 | 1986-05-10 | Preparation of plant culture nutrient solution |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62262922A JPS62262922A (en) | 1987-11-16 |
| JPH044849B2 true JPH044849B2 (en) | 1992-01-29 |
Family
ID=14452724
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61107189A Granted JPS62262922A (en) | 1986-05-10 | 1986-05-10 | Preparation of plant culture nutrient solution |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62262922A (en) |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5068821A (en) * | 1973-10-20 | 1975-06-09 | ||
| JPS5118840A (en) * | 1974-08-07 | 1976-02-14 | Mitsubishi Electric Corp | |
| JPS5840455A (en) * | 1981-09-01 | 1983-03-09 | アイシン精機株式会社 | Cryogenic refrigerator |
-
1986
- 1986-05-10 JP JP61107189A patent/JPS62262922A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62262922A (en) | 1987-11-16 |
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