JPH03236723A - Plant cultivation using thermal exhaust from thermal-power generation and system therefor - Google Patents

Plant cultivation using thermal exhaust from thermal-power generation and system therefor

Info

Publication number
JPH03236723A
JPH03236723A JP3141590A JP3141590A JPH03236723A JP H03236723 A JPH03236723 A JP H03236723A JP 3141590 A JP3141590 A JP 3141590A JP 3141590 A JP3141590 A JP 3141590A JP H03236723 A JPH03236723 A JP H03236723A
Authority
JP
Japan
Prior art keywords
plant cultivation
heat
thermal
exhaust
plant
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.)
Pending
Application number
JP3141590A
Other languages
Japanese (ja)
Inventor
Takayuki Torikai
鳥飼 高行
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Original Assignee
Toshiba Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Toshiba Corp filed Critical Toshiba Corp
Priority to JP3141590A priority Critical patent/JPH03236723A/en
Publication of JPH03236723A publication Critical patent/JPH03236723A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide the title system intended to prevent global warming and utilize the CO2-contg. waste heat from thermal-power generation, so designed that the CO2- contg. thermal exhaust produced by thermal-power generation is cooled to temperatures suitable for plant cultivation and introduced into plant cultivation site(s). CONSTITUTION:In the objective system 1, the thermal exhaust 3 released from a thermal power plant 2 is fed through a changeover valve 4a to an absorption refrigerating machine 5, passed through the heat sink (an evaporator) 5a of the refrigerating machine 5, and put to heat exchange with a refrigerant 6. The resulting exhaust 3 is introduced via a changeover valve 4b into a heat exchanger 7, where seawater 8 is flowing and the exhaust is put to heat exchange with the seawater 8. The resultant exhaust 3 is finally supplied to plant cultivation plant(s) 8. In the above processes, the refrigerating machine 5 is equipped with an air conditioning part 5b equivalent to a generator, and this conditioning part 5b is put into another plant cultivation plant 9. The refrigerant 6 is put to heat exchange with the thermal exhaust 3 at the heat sink 5a, vaporized and dissolved in a solution at an absorber 5c. Thence, the refrigerant takes heat from the ambient atmosphere at the air conditioning part 5b and evaporates again from the solution.

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) 本発明は、火力発電による廃熱を帯びかつ二酸化炭素を
多く含む熱排気を大気に放出しないで地球の温暖化を防
止し、かつこの排気をその熱と二酸化炭素を利用して植
物栽培に役立てる火力発電による熱排気利用植物栽培方
法およびそのシステムに関する。
[Detailed Description of the Invention] [Objective of the Invention] (Industrial Application Field) The present invention prevents global warming by not releasing into the atmosphere thermal exhaust gas that is charged with waste heat and contains a large amount of carbon dioxide from thermal power generation. The present invention also relates to a method and system for cultivating plants using heat exhaust from thermal power generation, in which the heat and carbon dioxide of the exhaust are utilized for plant cultivation.

(従来の技術) 現在地球的規模において二酸化炭素が増加しているが、
この二酸化炭素の増加は地球保温効果の原因となって地
球の気温を上昇させ、例えば南極での氷河溶解、海水の
彫版による海面の上昇、湿潤地域の砂漠化など様々な環
境問題を引き起こしていると考えられる。ところで、火
力発電所から放出される排気は、廃熱を帯びているため
、節炭器(エコノマイザ)等でその熱を利用しているが
、この排気は化石燃料の燃焼による二酸化炭素も多く含
有する。
(Prior art) Carbon dioxide is currently increasing on a global scale,
This increase in carbon dioxide causes a warming effect on the earth, raising the global temperature and causing various environmental problems such as melting of glaciers in Antarctica, rising sea levels due to engraving of seawater, and desertification of humid areas. It is thought that there are. By the way, the exhaust gas emitted from thermal power plants is tinged with waste heat, and that heat is used in economizers, etc., but this exhaust gas also contains a lot of carbon dioxide from the combustion of fossil fuels. do.

(発明が解決しようとする課題) ところが、この火力発電所からの排気が帯びる廃熱の利
用は、温度がせいぜい150℃を越える排気までに限ら
れ、それ以下の温度の排気については全く利用されるこ
となく大気に放出されている。したがって、現状では火
力発電所からの約150℃までの排気は、廃熱、すなわ
ち熱エネルギーが有効に利用されないだけでなく、それ
に含まれる二酸化炭素もなんら処理されないまま大気に
放出されるため、地球温暖化にも荷担していることにな
る。
(Problem to be solved by the invention) However, the use of waste heat in the exhaust gas from this thermal power plant is limited to exhaust gas whose temperature exceeds 150°C at most, and exhaust heat with a temperature lower than that cannot be used at all. is released into the atmosphere without any air pollution. Therefore, at present, exhaust heat up to approximately 150℃ from thermal power plants not only does not effectively utilize the waste heat, or thermal energy, but also releases the carbon dioxide contained in it into the atmosphere without being processed. This means that they are also contributing to global warming.

一方、植物は光合成によって二酸化炭素を費消し酸素を
放出するため、この二酸化炭素の費消を通して上述の地
球温暖化を抑制していると考えられる。そして、この植
物の栽培においては、二酸化炭素濃度の他に温度も大き
く関係する。
On the other hand, plants consume carbon dioxide and release oxygen through photosynthesis, so they are thought to suppress the above-mentioned global warming through the consumption of carbon dioxide. In addition to carbon dioxide concentration, temperature also plays a major role in cultivating this plant.

本発明は上記事情に鑑みてなされたもので、火力発電に
よる廃熱を帯びかつ二酸化炭素を多く含む排気を大気に
放出しないで地球の温暖化を防止する一方、その廃熱と
二酸化炭素をこれらが生長に必要な植物の栽培に役立て
、火力発電での燃焼による熱エネルギーの有効利用と二
酸化炭素の低減、酸素の増加等、火力発電の熱排気から
一挙に多くの効果を生み出すことが可能な方法およびシ
ステムを提供することを目的とする。
The present invention has been made in view of the above circumstances, and is intended to prevent global warming by not releasing exhaust heat and carbon dioxide-rich exhaust from thermal power generation into the atmosphere. It is possible to produce many effects at once from the heat exhaust from thermal power generation, such as useful for cultivating plants that are necessary for growth, effective use of thermal energy from combustion in thermal power generation, reduction of carbon dioxide, and increase in oxygen. The present invention aims to provide methods and systems.

〔発明の構成〕[Structure of the invention]

(課題を解決するための手段) 本発明は上記課題を解決するために、火力発電によって
生じる二酸化炭素を含む熱排気を植物栽培にふさわしい
温度に冷却する工程と、前記冷却された熱排気を植物の
栽培地に導く工程を含む火力発電による熱排気利用植物
栽培方法を提供する。
(Means for Solving the Problems) In order to solve the above problems, the present invention provides a step of cooling thermal exhaust gas containing carbon dioxide generated by thermal power generation to a temperature suitable for plant cultivation, and a step of cooling the thermal exhaust gas containing carbon dioxide generated by thermal power generation to a temperature suitable for cultivating plants. Provided is a method for cultivating plants using heat exhaust gas generated by thermal power generation, including a step of guiding the plant to a cultivation area.

本発明はまた、火力発電によって生じる二酸化炭素を含
む熱排気を植物栽培にふさわしい温度に冷却する熱交換
器と、植物栽培地を外気から隔離し、かつ前記熱交換器
で冷却された熱排気が導かれる植物栽培工場とを備える
火力発電による熱排気利用植物栽培システムを提供する
The present invention also provides a heat exchanger that cools thermal exhaust gas containing carbon dioxide generated by thermal power generation to a temperature suitable for plant cultivation; Provided is a plant cultivation system using thermal exhaust generated by thermal power generation, which is equipped with a guided plant cultivation factory.

(作用) 本発明の方法によれば、火力発電によって生ずる排気が
帯びた廃熱は、植物の栽培、主に促成栽培に相応しい温
度(30〜40℃)に冷却される。そして、この適温に
冷却された排気は植物栽培地に導かれ、その熱と排気に
含まれる二酸化炭素が植物の栽培に役立てられる。
(Function) According to the method of the present invention, waste heat tinged with exhaust gas generated by thermal power generation is cooled to a temperature (30 to 40° C.) suitable for plant cultivation, mainly forced cultivation. This cooled exhaust air is then led to a plant cultivation area, where the heat and carbon dioxide contained in the exhaust air are used to grow plants.

また本発明の植物栽培システムは、火力発電によって生
じる熱排気を植物栽培にふさわしい温度に冷却する熱交
換器と、植物栽培地を外気から隔離し、かつ前記熱交換
器で冷却された熱排気が導かれる植物栽培工場とを備え
る。したがって、本発明のシステムは上記の方法を実現
することができ、火力発電による排気の熱と二酸化炭素
を有効に利用して地球温暖化の抑制に貢献する。
In addition, the plant cultivation system of the present invention includes a heat exchanger that cools the heat exhaust generated by thermal power generation to a temperature suitable for plant cultivation, and a heat exchanger that isolates the plant cultivation area from the outside air and that cools the heat exhaust that is cooled by the heat exchanger. It is equipped with a guided plant cultivation factory. Therefore, the system of the present invention can realize the above method, and contributes to suppressing global warming by effectively utilizing exhaust heat and carbon dioxide from thermal power generation.

(実施例) 以下添付の図面を参照して本発明の詳細な説明する。(Example) The present invention will be described in detail below with reference to the accompanying drawings.

第1図は本発明の植物栽培システムの一例を示す模式図
である。すなわち、本実施例のシステム1においては、
火力発電所2から放出された熱排気3は、切換弁4aを
経て吸収式冷凍機5に送られ、この冷凍機5の冷熱源(
蒸発器)5aを通過して冷媒6との間で熱交換する。そ
の後、この排気3は切換弁4bを経由して熱交換器7に
導入される。熱交換器7には海水8が通っており、この
海水8との間で熱交換が行われる。最後に、この熱排気
3は植物栽培工場8に送られる。
FIG. 1 is a schematic diagram showing an example of the plant cultivation system of the present invention. That is, in the system 1 of this embodiment,
Thermal exhaust gas 3 released from the thermal power plant 2 is sent to the absorption chiller 5 via the switching valve 4a, and is used as the cold source of the chiller 5 (
It passes through the evaporator) 5a and exchanges heat with the refrigerant 6. Thereafter, this exhaust gas 3 is introduced into the heat exchanger 7 via the switching valve 4b. Seawater 8 passes through the heat exchanger 7, and heat exchange is performed with the seawater 8. Finally, this hot exhaust gas 3 is sent to a plant cultivation factory 8.

本実施例においては、熱交換器7における熱交換媒体と
して海水を用いるため、人工的な冷却媒体を用いる場合
に比べ、熱交換に掛かるコストを低減できる。
In this embodiment, since seawater is used as the heat exchange medium in the heat exchanger 7, the cost for heat exchange can be reduced compared to the case where an artificial cooling medium is used.

ところで、吸収式冷凍機5は発生器に相当する空調部5
bを有するが、この空調部5bは植物栽培工場9内に引
き込まれる。冷媒6は、冷熱源5aで熱排気3と熱交換
を行い気化した後、吸収器5cで溶液に溶解する。その
後空調部5bで周囲の雰囲気から熱を奪って再び溶液か
ら蒸発する。
By the way, the absorption refrigerator 5 has an air conditioning unit 5 which corresponds to a generator.
b, but this air conditioning unit 5b is drawn into the plant cultivation factory 9. The refrigerant 6 exchanges heat with the heat exhaust 3 in the cold heat source 5a and is vaporized, and then is dissolved into a solution in the absorber 5c. Thereafter, the air conditioner 5b removes heat from the surrounding atmosphere and evaporates from the solution again.

そして凝縮器5Cにおいて周囲に熱を放出して液化する
。したがって、植物栽培工場8内の熱排気3がなお高温
のときは、空調部5bにおいて熱排気3との間でさらに
熱交換が行われる。
Then, in the condenser 5C, it emits heat to the surroundings and liquefies it. Therefore, when the heat exhaust gas 3 in the plant cultivation factory 8 is still at a high temperature, heat exchange is further performed with the heat exhaust gas 3 in the air conditioning section 5b.

熱排気3を冷却する冷凍機として吸収式冷凍機5を用い
るのは、動力を用いないため経済的で、かつ150℃以
下の低い温度の排気でも熱源として使用できるためであ
る。約150℃の排気は、熱交換器7を通過した時点で
45〜60℃になり、植物栽培工場9においては促成栽
培用に30〜40℃に維持される。
The absorption refrigerator 5 is used as a refrigerator for cooling the thermal exhaust gas 3 because it is economical because no power is used, and even exhaust gas at a low temperature of 150° C. or lower can be used as a heat source. The exhaust gas at about 150°C becomes 45 to 60°C after passing through the heat exchanger 7, and is maintained at 30 to 40°C in the plant cultivation factory 9 for forced cultivation.

本実施例のシステムにおいて空調部5aを有する吸収式
冷凍機5は、熱交換器7の冷却能力を補うものであるが
、海水8の温度が低い寒冷期には熱交換器7だけでも十
分に熱排気3の温度を低くできるため、この時期には切
換弁4a、4bを切換えて、火力発電所2から放出され
た熱排気3を吸収式冷凍機5に送らず、バイパス管10
を介して直ちに熱交換器7に送る。
In the system of this embodiment, the absorption chiller 5 having the air conditioning section 5a supplements the cooling capacity of the heat exchanger 7, but in the cold season when the temperature of the seawater 8 is low, the heat exchanger 7 alone is sufficient. Since the temperature of the thermal exhaust gas 3 can be lowered, the switching valves 4a and 4b are switched at this time to prevent the thermal exhaust gas 3 released from the thermal power plant 2 from being sent to the absorption chiller 5, and to bypass the bypass pipe 10.
immediately sent to the heat exchanger 7 via the

第2図は、植物栽培工場9の模式透視図である。FIG. 2 is a schematic perspective view of the plant cultivation factory 9.

植物栽培工場9は植物栽培地11を天井9aと側壁9b
で外気12から隔離した構造物であるが、天井9aには
吸収式冷凍機の空調部5bが設置される。また栽培地1
1のわずか上方には、熱排気3と植物栽培用の水12が
流れる散水送気併用パイプ13が枝分れ状に敷設される
。植物栽培地11には、食糧、観賞用、砂防、雨水の蓄
積など種々の目的で使用される植物を栽培することがで
きる。
The plant cultivation factory 9 has a plant cultivation area 11 with a ceiling 9a and side walls 9b.
Although the structure is isolated from the outside air 12, an air conditioning section 5b of an absorption refrigerator is installed on the ceiling 9a. Also cultivation area 1
Slightly above the pipe 1, a watering and air supply pipe 13 through which the heat exhaust 3 and water 12 for plant cultivation flow is laid in a branched manner. In the plant cultivation area 11, plants used for various purposes such as food, ornamentation, erosion control, and rainwater accumulation can be cultivated.

第3図は、散水送気併用パイプ13の断面斜視図である
。この散水送気併用パイプ13は内管13aと外管13
bの二重管構造となっており、内管13aには熱排気3
が、また外管13bには散布用の水12が通される。そ
して、熱排気3は、多数枝分れした散水送気併用パイプ
13の各終端から排出されて植物栽培工場9内に充満す
るが、散布用の水12は外管13bの管壁に多数設けら
れた小径の散水孔14から少量づつ散布されて、植物栽
培地11に万遍なく行き渡る。
FIG. 3 is a cross-sectional perspective view of the pipe 13 for supplying water and air. This watering and air supply pipe 13 includes an inner pipe 13a and an outer pipe 13.
It has a double pipe structure as shown in b, and the inner pipe 13a has a heat exhaust 3.
However, water 12 for spraying is also passed through the outer tube 13b. The heat exhaust gas 3 is discharged from each end of the multi-branched watering and air supply pipe 13 and fills the plant cultivation factory 9, but a large number of water 12 for spraying are provided on the wall of the outer pipe 13b. The water is sprayed little by little from the small-diameter watering holes 14, and evenly distributed over the plant cultivation area 11.

この散水送気併用パイプ13によれば、内管13aを流
通する熱排気3は、外筒13bを流通する水12によっ
て冷却されるため、散水送気併用パイプ13は熱交換器
7および吸収式冷凍機5の冷却作用を補う役割を果たす
。したがって、熱排気3は植物を傷めるような温度で植
物栽培工場9内に導入されることはない。
According to this pipe 13, the heat exhaust gas 3 flowing through the inner tube 13a is cooled by the water 12 flowing through the outer tube 13b. It plays a role of supplementing the cooling action of the refrigerator 5. Therefore, the heated exhaust gas 3 will not be introduced into the plant cultivation factory 9 at a temperature that would damage the plants.

よって本実施例においては、散水送気併用パイプ13を
採用することによって熱交換器7の機能を一部代替して
熱交換器7を小型化することができ、熱交換器7の設置
にかかる費用を安価にすることができる。また散水送気
併用パイプ13は、散水管と送気管を別々に設置するの
に比べ設置工事を省力化できる。
Therefore, in this embodiment, by employing the pipe 13 for water sprinkling and air supply, the function of the heat exchanger 7 can be partially replaced and the heat exchanger 7 can be made smaller, and the installation cost of the heat exchanger 7 can be reduced. Costs can be reduced. Furthermore, the water and air supply pipe 13 can save labor in installation work compared to installing a water supply pipe and an air supply pipe separately.

そして、もし植物栽培工場9内における熱排気3の温度
が、促成栽培の適温30〜40℃を上回る場合は、温度
が高くて比重の軽い熱排気3が上昇したとき、天井9a
において吸収式冷凍機の空調部5bを通る冷媒6との間
で熱交換が行われる。
If the temperature of the heat exhaust 3 in the plant cultivation factory 9 exceeds the optimum temperature of 30 to 40°C for forced cultivation, when the heat exhaust 3 with high temperature and light specific gravity rises, the ceiling 9a
Heat exchange is performed with the refrigerant 6 passing through the air conditioning section 5b of the absorption refrigerator.

本実施例の植物栽培工場9においては、吸収式冷凍機の
空調部5bを散水送気併用パイプ13より上方に設置す
ることにより、空気の対流を利用して内部の温度を適正
に保つことができる。
In the plant cultivation factory 9 of this embodiment, by installing the air conditioning unit 5b of the absorption chiller above the watering and air supply pipe 13, it is possible to maintain an appropriate internal temperature using air convection. can.

本実施例においては、熱排気3の最終的な冷却は植物栽
培工場9内で行う。このため、植物栽培工場9外で冷却
しすぎて排気に含まれる水分が飽和蒸気圧に達して凝縮
し、その後植物栽培工場9内で暖めたときに、植物に必
要な水分の少ない雰囲気になるというおそれはない。
In this embodiment, the final cooling of the heat exhaust 3 is performed within the plant cultivation factory 9. For this reason, when the plant cultivation factory 9 is cooled too much, the moisture contained in the exhaust air reaches saturated vapor pressure and condenses, and when it is then heated inside the plant cultivation factory 9, it becomes an atmosphere with less moisture necessary for plants. There is no fear that this will happen.

このように、本実施例のシステム1によれば、今まで火
力発電所2から大気中に放出されていた150℃以下の
熱排気3を吸収式冷凍機5の冷熱源5 a s熱交換器
7および散水送気併用パイプ13と3段階の冷却を経て
植物栽培工場9に導入され、さらに吸収式冷凍機5の空
調部5bでも冷却が行われる。このため、火力発電によ
って生じる熱排気3は無駄なく冷却されて植物の栽培に
ふさわしい雰囲気温度を提供する。また熱排気3は地球
温暖化の元凶である二酸化炭素を多量に含有するが、こ
の二酸化炭素も植物の生長に必要な要素として有効に利
用される。
As described above, according to the system 1 of the present embodiment, the heat exhaust gas 3 of 150° C. or lower, which has been released into the atmosphere from the thermal power plant 2, is transferred to the cold heat source 5 a s heat exchanger of the absorption chiller 5. 7 and the water-sprinkling air supply pipe 13 to be introduced into the plant cultivation factory 9 through three stages of cooling, and further cooled in the air conditioning section 5b of the absorption chiller 5. Therefore, the heat exhaust gas 3 generated by thermal power generation is cooled without waste, providing an ambient temperature suitable for cultivating plants. Furthermore, although the thermal exhaust gas 3 contains a large amount of carbon dioxide, which is the cause of global warming, this carbon dioxide is also effectively used as an element necessary for plant growth.

〔発明の効果〕〔Effect of the invention〕

以上説明したように、本発明の方法とシステムによれば
、火力発電によって生ずる熱排気をそのまま大気に放出
したのでは環境に悪影響を与える廃熱と二酸化炭素を植
物の栽培に利用することによっt1環境保全にとどまら
ず、植物という人類と環境にとって有益な存在を育てる
ことができる。
As explained above, according to the method and system of the present invention, waste heat and carbon dioxide, which would have a negative impact on the environment if the thermal exhaust generated by thermal power generation were released directly into the atmosphere, can be used for plant cultivation. t1In addition to environmental conservation, it is possible to grow plants, which are beneficial to humans and the environment.

第1図は本発明の実施例に係る植物栽培システムの模式
図、第2図は前記実施例に係る植物栽培工場の模式透視
図、第3図は前記実施例に係る散水送気併用パイプの断
面斜視図である。
FIG. 1 is a schematic diagram of a plant cultivation system according to an embodiment of the present invention, FIG. 2 is a schematic perspective view of a plant cultivation factory according to the embodiment, and FIG. 3 is a diagram of a water supply and air supply pipe according to the embodiment. It is a cross-sectional perspective view.

3・・・熱排気、5・・・吸収式冷凍機、5a・・・空
調部、7・・・熱交換器、8・・・海水、9・・・植物
栽培工場、13・・・散水送気併用パイプ。
3... Heat exhaust, 5... Absorption chiller, 5a... Air conditioner, 7... Heat exchanger, 8... Seawater, 9... Plant cultivation factory, 13... Watering Air supply pipe.

Claims (1)

【特許請求の範囲】 1、(1)火力発電によって生じる二酸化炭素を含む熱
排気を植物栽培にふさわしい温度に冷却する工程と、(
2)前記冷却された熱排気を植物の栽培地に導く工程を
含む火力発電による熱排気利用植物栽培方法。 2、火力発電によって生じる二酸化炭素を含む熱排気を
植物栽培にふさわしい温度に冷却する熱交換器と、植物
栽培地を外気から隔離し、かつ前記熱交換器で冷却され
た熱排気が導かれる植物栽培工場とを備える火力発電に
よる熱排気利用植物栽培システム。 3、前記熱交換器は、前記熱排気を海水との間で熱交換
させる請求項2記載の植物栽培システム。 4、前記熱排気を前記熱交換器で熱交換する前に冷却し
、かつ前記植物工場内を空気を冷却する空調部を有する
吸収式冷凍機を備える請求項2ないし請求項3のいずれ
か一項記載の植物栽培システム。 5、前記植物栽培工場は、前記熱排気を通す送気管を植
物に散水する散水管で覆った二重管構造の散水送気併用
パイプを備える請求項2ないし請求項4のいずれか一項
記載の植物栽培システム。 6、前記植物栽培工場内において前記散水送気併用パイ
プは前記吸収式冷凍機の空調部より下方に設置される請
求項5記載の植物栽培システム。
[Claims] 1. (1) A step of cooling thermal exhaust gas containing carbon dioxide generated by thermal power generation to a temperature suitable for plant cultivation;
2) A method for cultivating plants using thermal exhaust gas generated by thermal power generation, including the step of guiding the cooled thermal exhaust gas to a plant cultivation area. 2. A heat exchanger that cools the heat exhaust gas containing carbon dioxide produced by thermal power generation to a temperature suitable for plant cultivation, and a plant that isolates the plant cultivation area from the outside air and to which the heat exhaust air cooled by the heat exchanger is guided. A plant cultivation system that utilizes heat exhaust from thermal power generation and is equipped with a cultivation factory. 3. The plant cultivation system according to claim 2, wherein the heat exchanger exchanges heat between the heat exhaust and seawater. 4. Any one of claims 2 to 3, further comprising an absorption refrigerator having an air conditioning unit that cools the heat exhaust gas before exchanging heat with the heat exchanger and cools air inside the plant factory. Plant cultivation system as described in section. 5. The plant cultivation factory includes a watering and air supply pipe having a double pipe structure in which the air supply pipe for passing the heat exhaust gas is covered with a watering pipe for watering the plants. plant cultivation system. 6. The plant cultivation system according to claim 5, wherein the watering and air supply pipe is installed below the air conditioning section of the absorption refrigerator in the plant cultivation factory.
JP3141590A 1990-02-14 1990-02-14 Plant cultivation using thermal exhaust from thermal-power generation and system therefor Pending JPH03236723A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3141590A JPH03236723A (en) 1990-02-14 1990-02-14 Plant cultivation using thermal exhaust from thermal-power generation and system therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3141590A JPH03236723A (en) 1990-02-14 1990-02-14 Plant cultivation using thermal exhaust from thermal-power generation and system therefor

Publications (1)

Publication Number Publication Date
JPH03236723A true JPH03236723A (en) 1991-10-22

Family

ID=12330627

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3141590A Pending JPH03236723A (en) 1990-02-14 1990-02-14 Plant cultivation using thermal exhaust from thermal-power generation and system therefor

Country Status (1)

Country Link
JP (1) JPH03236723A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05168349A (en) * 1991-12-20 1993-07-02 Agency Of Ind Science & Technol Production of vegetable resource using carbon dioxide as raw material
JP2006061127A (en) * 2004-08-30 2006-03-09 Kansai Electric Power Co Inc:The Method for providing carbonic acid gas in greenhouse culture
JP2013004757A (en) * 2011-06-17 2013-01-07 Toshiba Corp Transformation system and substation or switchyard with transformation system installed therein
WO2014010561A1 (en) * 2012-07-10 2014-01-16 株式会社デンソー Carbon dioxide supply device
JP2014516247A (en) * 2011-04-02 2014-07-10 ▲陽▼光▲凱▼迪新能源集▲団▼有限公司 Method and apparatus for supplying heat and carbon dioxide to vegetables and / or algae using power plant flue gas
JP2016007163A (en) * 2014-06-24 2016-01-18 ネポン株式会社 Carbon dioxide generation system

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH05168349A (en) * 1991-12-20 1993-07-02 Agency Of Ind Science & Technol Production of vegetable resource using carbon dioxide as raw material
JP2006061127A (en) * 2004-08-30 2006-03-09 Kansai Electric Power Co Inc:The Method for providing carbonic acid gas in greenhouse culture
JP4489536B2 (en) * 2004-08-30 2010-06-23 関西電力株式会社 Carbon dioxide gas application method for greenhouse cultivation
JP2014516247A (en) * 2011-04-02 2014-07-10 ▲陽▼光▲凱▼迪新能源集▲団▼有限公司 Method and apparatus for supplying heat and carbon dioxide to vegetables and / or algae using power plant flue gas
JP2013004757A (en) * 2011-06-17 2013-01-07 Toshiba Corp Transformation system and substation or switchyard with transformation system installed therein
WO2014010561A1 (en) * 2012-07-10 2014-01-16 株式会社デンソー Carbon dioxide supply device
CN104427858A (en) * 2012-07-10 2015-03-18 株式会社电装 Carbon dioxide supply device
JPWO2014010561A1 (en) * 2012-07-10 2016-06-23 株式会社デンソー Carbon dioxide supply device
JP2016007163A (en) * 2014-06-24 2016-01-18 ネポン株式会社 Carbon dioxide generation system

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