JPH0127695B2 - - Google Patents
Info
- Publication number
- JPH0127695B2 JPH0127695B2 JP59039776A JP3977684A JPH0127695B2 JP H0127695 B2 JPH0127695 B2 JP H0127695B2 JP 59039776 A JP59039776 A JP 59039776A JP 3977684 A JP3977684 A JP 3977684A JP H0127695 B2 JPH0127695 B2 JP H0127695B2
- Authority
- JP
- Japan
- Prior art keywords
- nutrient solution
- section
- tank
- sterilization
- hydroponic cultivation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- Y02P60/216—
Landscapes
- Hydroponics (AREA)
- Dairy Products (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は作物の養液栽培に用いられる栽培装置
に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to a cultivation device used for hydroponic cultivation of crops.
土壌を用いないで作物の栽培を行う養液栽培の
長所として(1)省力化及び自動化が容易である、(2)
連作障害がない、(3)土壌栽培に比べ収獲量が多
い、など数多くの長所があるが、反面、養液を循
環させているため、一度養液中に病原菌が混入し
た場合、病害の伝染速度が大きく被害が大きいと
いう欠点を有している。従つて、養液栽培におい
て養液の殺菌は最も重要な問題の1つである。
Advantages of hydroponic cultivation, which cultivates crops without using soil, are (1) easy labor-saving and automation; (2)
It has many advantages, such as no continuous cropping problems and (3) higher yields than soil cultivation, but on the other hand, because the nutrient solution is circulated, once pathogens are mixed into the nutrient solution, there is a risk of disease transmission. It has the disadvantage of high speed and great damage. Therefore, sterilization of the nutrient solution is one of the most important issues in hydroponic cultivation.
そこで、従来この種の殺菌装置として第1図A
に示すものがあつた。図において101は加温
部、102は冷却部、103はヒータ、104は
フイン、105は流体である。 Therefore, conventional sterilizers of this type are shown in Figure 1A.
I found the one shown here. In the figure, 101 is a heating section, 102 is a cooling section, 103 is a heater, 104 is a fin, and 105 is a fluid.
次に上記各部分の動作について説明する。流体
105は例えば食品加工業、養殖業、病院等にお
いて使用される牛乳、水、空気などであり、該流
体105の中には、各種の病源細菌、カビなどが
含まれている。そのため、それらの殺菌のため
に、流体105aは加温部101において、ヒー
タ103等により殺菌するに十分な温度まで昇温
され、その後、流体105bは冷却部102のフ
イン104などを介して、外気に放熱、冷却され
る。そして、上記流体105cは次のプロセスに
おいて使用される。 Next, the operation of each of the above parts will be explained. The fluid 105 is, for example, milk, water, air, etc. used in the food processing industry, aquaculture industry, hospitals, etc., and the fluid 105 contains various pathogenic bacteria, molds, and the like. Therefore, in order to sterilize them, the fluid 105a is heated to a temperature sufficient for sterilization by the heater 103 etc. in the heating section 101, and then the fluid 105b is passed through the fins 104 of the cooling section 102 to the outside air. Heat is dissipated and cooled. The fluid 105c is then used in the next process.
しかしながら、上記従来の殺菌装置は流体10
5が加熱された後、それに要したエネルギが単に
冷却部102において外気へ放熱されるために無
駄が多く、殺菌に要するエネルギは極めて大きい
などの欠点がある。 However, the conventional sterilizer described above has a fluid 10
5 is heated, the energy required for this is simply radiated to the outside air in the cooling section 102, which results in a lot of waste, and the energy required for sterilization is extremely large.
第1図Bが上記の加温殺菌機構を有する養液栽
培装置の構成図である。 FIG. 1B is a configuration diagram of a hydroponic cultivation apparatus having the above-mentioned heating sterilization mechanism.
図において1は作物、2は栽培槽、3は養液タ
ンク、4は養液、5は上記栽培槽2と養液タンク
3を連結する養液循環路、6は養液循環ポンプ、
7はヒータ、8は放熱器である。 In the figure, 1 is a crop, 2 is a cultivation tank, 3 is a nutrient solution tank, 4 is a nutrient solution, 5 is a nutrient solution circulation path connecting the cultivation tank 2 and the nutrient solution tank 3, 6 is a nutrient solution circulation pump,
7 is a heater, and 8 is a radiator.
次に動作について説明する。養液4が養液循環
ポンプ6によつて養液タンク3と栽培槽2の間を
循環路5を通つて連続的、あるいは間欠的に循環
する。その際、養液4がポンプ6によつて養液タ
ンク3からくみ上げられ、その後ヒータ7によつ
て殺菌するに十分な温度まで加温され、その後、
放熱器8により周囲に放熱し、作物栽培に適した
温度まで冷却され栽培槽2に至る。以後養液4は
上記循環を繰り返す。 Next, the operation will be explained. The nutrient solution 4 is continuously or intermittently circulated between the nutrient solution tank 3 and the cultivation tank 2 through the circulation path 5 by the nutrient solution circulation pump 6. At that time, the nutrient solution 4 is pumped up from the nutrient solution tank 3 by the pump 6, then heated to a temperature sufficient for sterilization by the heater 7, and then,
Heat is radiated to the surroundings by a radiator 8, and the temperature is cooled to a temperature suitable for crop cultivation and reaches the cultivation tank 2. Thereafter, the nutrient solution 4 repeats the above circulation.
従来の加温殺菌機構を有する養液栽培装置は以
上のように構成されているので、養液の加温に要
するエネルギが大きく、かつ加温殺菌後に養液を
冷却しても、養液の温度を周囲温度以下には下げ
られないという欠点があつた。 Conventional hydroponic cultivation equipment with a heating sterilization mechanism is configured as described above, so it requires a large amount of energy to heat the nutrient solution, and even if the nutrient solution is cooled after heating and sterilization, the nutrient solution is The drawback was that the temperature could not be lowered below ambient temperature.
本発明は上記のような従来の加熱殺菌機構を有
する養液栽培装置の欠点を除去するためになされ
たもので、養液加温をヒートポンプの放熱部で行
い、かつ養液の冷却を同一ヒートポンプの吸熱部
で行うことにより、養液加温に要するエネルギを
小さくし、また冷却後の養液の温度を周囲温度以
下にすることも可能な養液栽培装置を提供するこ
とを目的としている。
The present invention was made in order to eliminate the drawbacks of the conventional hydroponic cultivation apparatus having a heat sterilization mechanism as described above. It is an object of the present invention to provide a hydroponic cultivation apparatus that can reduce the energy required for heating the nutrient solution and also lower the temperature of the nutrient solution after cooling to below the ambient temperature by heating the nutrient solution in the endothermic part of the nutrient solution.
養液の殺菌には加温殺菌、紫外線殺菌、オゾン
殺菌など種々の方法が提案されているが、本発明
の養液栽培装置はそれらの内最も確実で安全性が
高い加温殺菌機構により構成されている。
Various methods have been proposed for sterilizing the nutrient solution, such as heating sterilization, ultraviolet sterilization, and ozone sterilization, but the hydroponic cultivation apparatus of the present invention is constructed using a heating sterilization mechanism that is the most reliable and safest among them. has been done.
以下、この発明の一実施例を第2図に基づき説
明する。図中、1〜6は第1図Bの同一符号のも
のと同様の構成要素を示す。 An embodiment of the present invention will be described below with reference to FIG. In the figure, numerals 1 to 6 indicate the same components as those with the same reference numerals in FIG. 1B.
第2図において9は養液加熱殺菌部、10は養
液冷却部、11は機械圧縮式のヒートポンプ、1
2は上記ヒートポンプの放熱部、13は上記ヒー
トポンプの吸熱部、14は圧縮機、15は減圧
弁、16は冷媒循環路である。 In Fig. 2, 9 is a nutrient solution heating sterilization section, 10 is a nutrient solution cooling section, 11 is a mechanical compression type heat pump, 1
Reference numeral 2 denotes a heat radiation section of the heat pump, 13 a heat absorption section of the heat pump, 14 a compressor, 15 a pressure reducing valve, and 16 a refrigerant circulation path.
次に動作を説明する。養液4が養液タンク3か
らポンプ6によつて吸上げられ、養液加熱殺菌部
9でヒートポンプ11の放熱部12と熱交換し、
加温される。その後養液冷却部10でヒートポン
プ11の吸熱部13と熱交換し、作物栽培に適し
た温度まで冷却され、栽培槽2に至る。栽培槽2
での余剰養液は養液循環路5を経て、養液タンク
3に戻る。 Next, the operation will be explained. The nutrient solution 4 is sucked up from the nutrient solution tank 3 by the pump 6, and exchanges heat with the heat radiation section 12 of the heat pump 11 in the nutrient solution heating sterilization section 9.
It is heated. Thereafter, the nutrient solution cooling section 10 exchanges heat with the endothermic section 13 of the heat pump 11 and is cooled to a temperature suitable for crop cultivation, and reaches the cultivation tank 2. Cultivation tank 2
The surplus nutrient solution is returned to the nutrient solution tank 3 via the nutrient solution circulation path 5.
一般に作物の地下部を侵す病菌は約60℃程度の
温度で死減する。そのため養液加熱殺菌部9は養
液4を上記約60℃程度の温度まで加温する。養液
加温殺菌および養液冷却に用いられるエネルギは
圧縮機14の動力のみでよく、第1図Bに示した
改良装置より省エネルギ的である。また、ヒート
ポンプの冷媒蒸発温度を周囲温度より低く設定す
ることにより、栽培槽2に入る養液の温度を周囲
温度より下げることも可能となる。 In general, pathogens that attack the underground parts of crops die at a temperature of about 60°C. Therefore, the nutrient solution heating sterilization section 9 heats the nutrient solution 4 to the above-mentioned temperature of approximately 60°C. The energy used for heating and sterilizing the nutrient solution and cooling the nutrient solution requires only the power of the compressor 14, which is more energy-saving than the improved device shown in FIG. 1B. Furthermore, by setting the refrigerant evaporation temperature of the heat pump lower than the ambient temperature, it is also possible to lower the temperature of the nutrient solution entering the cultivation tank 2 below the ambient temperature.
なお、上記実施例では養液加温殺菌部9、およ
び養液冷却部10を養液タンク3から栽培槽2へ
至る経路内に設置したが、これらは循環系の如何
なる位置に設置しても良く、また、第3図に示し
た他の実施例を示す構成図のように、養液タンク
3から同養液タンク3に至る別の養液循環路5a
の途中に養液加温殺菌部9、養液冷却部10を設
置しても良い。図中6aは上記別養液循環路5a
用の養液循環ポンプである。 In the above embodiment, the nutrient solution heating sterilization section 9 and the nutrient solution cooling section 10 were installed in the path from the nutrient solution tank 3 to the cultivation tank 2, but they can be installed at any position in the circulation system. Furthermore, as shown in the configuration diagram of another embodiment shown in FIG.
A nutrient solution heating sterilization section 9 and a nutrient solution cooling section 10 may be installed in the middle. In the figure, 6a is the separate nutrient solution circulation path 5a.
This is a nutrient solution circulation pump for use.
第4図は二段式ヒートポンプを用いた場合の他
の実施例を示す構成図であり、14a,14bは
夫々低温段圧縮機および高温段圧縮機、15a,
15bは夫々低温段減圧弁、高温段減圧弁、16
a,16bは低温段冷媒循環路、高温段冷媒循環
路、17aは低温段放熱部、17bは高温段吸熱
部である。 FIG. 4 is a configuration diagram showing another embodiment in which a two-stage heat pump is used, in which 14a and 14b are a low-temperature stage compressor and a high-temperature stage compressor, respectively;
15b are a low temperature stage pressure reducing valve, a high temperature stage pressure reducing valve, 16
a and 16b are a low temperature stage refrigerant circulation path, a high temperature stage refrigerant circulation path, 17a is a low temperature stage heat dissipation section, and 17b is a high temperature stage heat absorption section.
ところで、上記説明はヒートポンプとして機械
圧縮式ヒートポンプを用いた場合について述べた
が、その他の原理に基く、例えば吸収式ヒートポ
ンプ、電子式ヒートポンプ等を用いてもよいこと
は言うまでもない。 Incidentally, although the above description has been made regarding the case where a mechanical compression type heat pump is used as the heat pump, it goes without saying that it is also possible to use an absorption type heat pump, an electronic type heat pump, etc. based on other principles.
以上のように、この発明によれば養液の加熱殺
菌および冷却を同一のヒートポンプで行うように
構成としたので、加熱殺菌に要するエネルギを非
常に少なくでき、また、養液温度を周囲温度より
下げ得るという理想的な養液栽培装置を得られる
という効果が得られる。
As described above, according to the present invention, the heat sterilization and cooling of the nutrient solution are performed using the same heat pump, so the energy required for heat sterilization can be extremely reduced, and the temperature of the nutrient solution can be kept lower than the ambient temperature. This has the effect of providing an ideal hydroponic system that can be lowered.
第1図Aは従来の殺菌機構の構成図、第1図B
は第1図Aの殺菌機構を有する養液栽培装置を示
す構成図、第2図はこの発明の一実施例を示す養
液栽培装置の構成図、第3図、第4図はこの発明
の他の実施例を示す養液栽培装置の構成図であ
る。
1……作物、2……栽培槽、3……養液タン
ク、9……養液、5,5a……養液循環路、6,
6a……養液循環ポンプ、7……ヒータ、8……
放熱器、9……養液加温殺菌部、10……養液冷
却部、11……ヒートポンプ、12……放熱部、
13……吸熱部、14,14a,14b……圧縮
機、15,15a,15b……減圧弁、16,1
6a,16b……冷媒循環路、17a……低温段
放熱部、17b……高温段吸熱部。なお、図中、
同一符号は同一、または相当部分を示す。
Figure 1A is a configuration diagram of a conventional sterilization mechanism, Figure 1B
1 is a block diagram showing a hydroponic cultivation apparatus having the sterilization mechanism shown in FIG. It is a block diagram of the hydroponic cultivation apparatus which shows another Example. 1... Crop, 2... Cultivation tank, 3... Nutrient solution tank, 9... Nutrient solution, 5, 5a... Nutrient solution circulation path, 6,
6a... Nutrient circulation pump, 7... Heater, 8...
Heat radiator, 9... Nutrient solution heating sterilization section, 10... Nutrient solution cooling section, 11... Heat pump, 12... Heat radiating section,
13... Endothermic part, 14, 14a, 14b... Compressor, 15, 15a, 15b... Pressure reducing valve, 16, 1
6a, 16b...refrigerant circulation path, 17a...low temperature stage heat radiation section, 17b...high temperature stage heat absorption section. In addition, in the figure,
The same reference numerals indicate the same or equivalent parts.
Claims (1)
殺菌部で加温された養液を作物栽培に適した温度
まで冷却する冷却部とを備え、上記加温殺菌部で
の養液の加温と冷却部での養液の冷却とを夫々同
一のヒートポンプの放熱部および吸熱部で行うこ
とを特徴とする養液栽培装置。 2 養液栽培装置内の作物を栽培する栽培槽及び
養液を収容する養液タンクの間に養液を循環させ
る養液循環路中に加温殺菌部と冷却部とを備えた
ことを特徴とする特許請求の範囲第1項記載の養
液栽培装置。 3 作物を栽培する栽培槽及び養液を収容する養
液タンクの間で養液を循環させる養液タンクにお
いて、該養液タンクの内部養液をとり出して加温
殺菌、および冷却してしかる後、再び上記タンク
内に戻すように働く機構を設けたことを特徴とす
る特許請求の範囲第1項記載の養液栽培装置。 4 ヒートポンプが多段式ヒートポンプであるこ
とを特徴とする特許請求の範囲第1項乃至第3項
記載の養液栽培装置。[Scope of Claims] 1. A heating sterilization section that heats and sterilizes a nutrient solution, and a cooling section that cools the nutrient solution heated in the heat sterilization section to a temperature suitable for crop cultivation. A hydroponic cultivation apparatus characterized in that heating of the nutrient solution in the thermal sterilization section and cooling of the nutrient solution in the cooling section are performed by the same heat radiating section and endothermic section of the same heat pump, respectively. 2. The hydroponic cultivation device is characterized by having a heating sterilization section and a cooling section in the nutrient solution circulation path that circulates the nutrient solution between the cultivation tank for cultivating crops and the nutrient solution tank for storing the nutrient solution. A hydroponic cultivation apparatus according to claim 1. 3. In a nutrient solution tank that circulates nutrient solution between a cultivation tank in which crops are grown and a nutrient solution tank that stores nutrient solution, the nutrient solution inside the nutrient solution tank is taken out, heated, sterilized, and cooled. 2. The hydroponic cultivation apparatus according to claim 1, further comprising a mechanism for returning the water to the tank. 4. The hydroponic cultivation apparatus according to claims 1 to 3, wherein the heat pump is a multistage heat pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59039776A JPS60184331A (en) | 1984-03-02 | 1984-03-02 | Nutritive solution culture apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59039776A JPS60184331A (en) | 1984-03-02 | 1984-03-02 | Nutritive solution culture apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60184331A JPS60184331A (en) | 1985-09-19 |
| JPH0127695B2 true JPH0127695B2 (en) | 1989-05-30 |
Family
ID=12562331
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59039776A Granted JPS60184331A (en) | 1984-03-02 | 1984-03-02 | Nutritive solution culture apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60184331A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016135961A1 (en) * | 2015-02-27 | 2016-09-01 | 株式会社タムロン | Plant cultivation device, plant, plant cultivation method and medium |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4760743B2 (en) * | 2007-03-23 | 2011-08-31 | 株式会社富士通ゼネラル | Sterilizer |
-
1984
- 1984-03-02 JP JP59039776A patent/JPS60184331A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016135961A1 (en) * | 2015-02-27 | 2016-09-01 | 株式会社タムロン | Plant cultivation device, plant, plant cultivation method and medium |
| JP2016158526A (en) * | 2015-02-27 | 2016-09-05 | 株式会社タムロン | Plant cultivation method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60184331A (en) | 1985-09-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| SE8004161L (en) | SET AND DEVICE FOR CULTURE AND TISSUE CULTIVATION | |
| US7152664B2 (en) | Incubation and storage device, in particular for specimens of organic material | |
| KR20220020797A (en) | Smart farm heating and cooling system using heat pump | |
| JP2760377B2 (en) | Sterilizer | |
| JP3778900B2 (en) | Sterilizer and hydroponics system using the same | |
| JPH0127695B2 (en) | ||
| JPS60184333A (en) | Nutritive solution culture apparatus | |
| JPS60184332A (en) | Nutritive solution culture apparatus | |
| JP2512033Y2 (en) | Hydroponics equipment | |
| CN214950027U (en) | Medicine refrigerated transport case that poultry animal doctor used | |
| JP7471582B2 (en) | Plant Cultivation System | |
| JPH01184093A (en) | Heat pump type thermal sterilizer and thermal sterilizing method | |
| JPH046554Y2 (en) | ||
| US2093334A (en) | Sterilizer | |
| JP6309738B2 (en) | Cheese ripening equipment | |
| JP2002281828A (en) | Culture device | |
| JP2909194B2 (en) | Hydroponic method for promoting flower bud differentiation and cultivation of strawberry seedlings | |
| KR102122301B1 (en) | Greenhouse control system controlling temperature of greenhouse using dual pipe | |
| CN210045261U (en) | A new type of biological safety cabinet | |
| CN216018764U (en) | Fat preservation equipment for autologous fat filling | |
| CN214333171U (en) | An intelligent constant temperature device for drug storehouses | |
| CN220756395U (en) | Sterilization equipment is used in processing of bovine coloctrum production | |
| CN219108634U (en) | Fresh milk pasteurization temperature control unit | |
| CN223564786U (en) | High-efficient condensing equipment of vertical pressure steam sterilizer | |
| GB1163372A (en) | Improvements in or relating to Methods and Apparatus for Continuously Sterilising Liquids by Heat Treatment |