JPH04210522A - Storage device of fresh material - Google Patents
Storage device of fresh materialInfo
- Publication number
- JPH04210522A JPH04210522A JP2402797A JP40279790A JPH04210522A JP H04210522 A JPH04210522 A JP H04210522A JP 2402797 A JP2402797 A JP 2402797A JP 40279790 A JP40279790 A JP 40279790A JP H04210522 A JPH04210522 A JP H04210522A
- Authority
- JP
- Japan
- Prior art keywords
- storage
- gas
- carbon dioxide
- reserve
- combustion
- 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
Links
- 239000000463 material Substances 0.000 title description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 106
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 53
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 53
- 238000002485 combustion reaction Methods 0.000 claims abstract description 43
- 239000003463 adsorbent Substances 0.000 claims abstract description 16
- 239000000446 fuel Substances 0.000 claims abstract description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 7
- 238000001179 sorption measurement Methods 0.000 claims description 18
- 230000001105 regulatory effect Effects 0.000 claims description 9
- 239000007789 gas Substances 0.000 abstract description 95
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 abstract description 8
- 239000005977 Ethylene Substances 0.000 abstract description 8
- 238000004321 preservation Methods 0.000 abstract 4
- 238000012856 packing Methods 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 14
- 239000000567 combustion gas Substances 0.000 description 13
- 235000013305 food Nutrition 0.000 description 8
- 229910052757 nitrogen Inorganic materials 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 238000011049 filling Methods 0.000 description 4
- 239000004449 solid propellant Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 230000003750 conditioning effect Effects 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000029058 respiratory gaseous exchange Effects 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- -1 that is Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Landscapes
- Storage Of Fruits Or Vegetables (AREA)
- Storage Of Harvested Produce (AREA)
Abstract
Description
[0001] [0001]
【産業上の利用分野】本発明は、野菜、果実等の生鮮物
を生産地あるいは流通段階等において長期間の貯蔵を可
能とする生鮮物貯蔵装置に関する。
[0002]BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fresh produce storage device that allows fresh produce such as vegetables and fruits to be stored for a long period of time at the production site or at the distribution stage. [0002]
【従来の技術】生鮮物を貯蔵する手段としては冷蔵貯蔵
が一般的であるが、これに加えてより長期にわたる貯蔵
手段とじて、貯蔵庫内の空気成分を変える貯蔵がある。
つまり、貯蔵庫内の酸素濃度を減少せしめ、炭酸ガス濃
度を増加せしめることで生鮮物の呼吸作用を抑制し、ま
た微生物による変質9分解や酸化等の化学反応も防止す
ることができることが知られている。
[00031以下図面を参照しながら、上述した従来の
生鮮物貯蔵装置の一例について説明する。
[0004]図3は従来の生鮮物貯蔵装置の系統図を示
すものである。1′は貯蔵庫であり、蒸発器2′、コン
デンシングユニット3′から成る冷却装置4′を設けて
いる。5′はプロパンガスボンベであり、炭素ガス発生
装置6′で前記貯蔵庫1′より導入管7′で導入した空
気を供して燃焼させ発生した燃焼排ガスすなわち炭酸ガ
スを排出管8′で前記貯蔵庫1′に排出している。9′
は炭酸ガス吸着装置で、前記貯蔵庫1′より導入管10
′で導入し、過剰の炭酸ガスを吸着した後、排出管11
′で貯蔵庫1′に戻している。12′はガスモニターで
あり貯蔵庫1′内のガス濃度を検知して炭酸ガス発生装
置6′及び炭酸ガス吸着装置9′を適時コントロールし
ている。
[0005]2. Description of the Related Art Refrigerated storage is a common means of storing perishables, but in addition to this, there is storage that changes the air composition within the storage room as a longer-term storage means. In other words, it is known that by reducing the oxygen concentration and increasing the carbon dioxide concentration in the storage room, it is possible to suppress the respiration of fresh produce and also to prevent chemical reactions such as decomposition and oxidation caused by microorganisms. There is. [00031] An example of the above-mentioned conventional fresh food storage device will be described below with reference to the drawings. [0004] FIG. 3 shows a system diagram of a conventional fresh produce storage device. Reference numeral 1' denotes a storage, and a cooling device 4' consisting of an evaporator 2' and a condensing unit 3' is provided. Reference numeral 5' denotes a propane gas cylinder, in which the air introduced from the storage 1' through the introduction pipe 7' is combusted in the carbon gas generator 6', and the generated combustion exhaust gas, that is, carbon dioxide gas, is sent to the storage 1' through the discharge pipe 8'. is being discharged. 9′
is a carbon dioxide adsorption device, and an inlet pipe 10 is connected from the storage 1'.
', and after adsorbing excess carbon dioxide gas, the discharge pipe 11
' is returned to storage 1'. Reference numeral 12' denotes a gas monitor which detects the gas concentration in the storage 1' and controls the carbon dioxide gas generator 6' and the carbon dioxide adsorption device 9' in a timely manner. [0005]
【発明が解決しようとする課題】しかしながら、上記の
ような構成では、炭酸ガス発生装置6′から発生するガ
スの成分としては炭酸ガス以外にエチレンやプロピレン
等の生鮮物の貯蔵に有害なガスが多量に含有されており
、そのガスが直接貯蔵庫1′内に放出されるため、貯蔵
物にしばしば悪影響を与えていた。また、貯蔵中に生鮮
物より発生するエチレン等のガスも悪影響を与えていた
。
[0006]本発明は、上記問題点に鑑み、貯蔵に有害
なガスを全て除去し得る生鮮物貯蔵装置を提供するもの
である。
[0007][Problems to be Solved by the Invention] However, in the above-described configuration, the gas generated from the carbon dioxide gas generator 6' contains gases other than carbon dioxide that are harmful to the storage of perishables, such as ethylene and propylene. Since the gas contained in large amounts is directly released into the storage chamber 1', it often has an adverse effect on the stored materials. In addition, gases such as ethylene generated from fresh produce during storage also had a negative impact. [0006] In view of the above problems, the present invention provides a fresh food storage device that can remove all gases harmful to storage. [0007]
【課題を解決するための手段】上記問題点を解決するた
め本発明の生鮮物貯蔵装置は、生鮮物を貯蔵する貯蔵庫
と、この貯蔵庫へ導入する調整ガスを貯める予備庫と、
予備庫と貯蔵庫を連通ずる連通管と、この連通管に設け
た送風機と、貯蔵庫の天面に設けた開放バルブと、この
予備庫内へ炭酸ガスを導入すべく炭素を含有する燃料を
燃焼させる燃焼炉と、この燃焼炉に前記燃料の燃焼に供
する空気を前記予備庫より循環せしめる送風機と、前記
燃焼炉から発生するガスの過剰な炭酸ガスを吸着すべく
吸着材を入れた吸着器とを備え、前記予備庫の下流に前
記燃焼炉を、前記燃料炉の下流に前記送風機を、前記送
風機の下流に前記吸着器を、前記吸着器の下流に前記予
備庫を配設してなるものである。
[0008][Means for Solving the Problems] In order to solve the above-mentioned problems, the perishables storage device of the present invention includes: a storage for storing perishables; a spare storage for storing a regulated gas to be introduced into the storage;
A communication pipe that communicates the reserve storage with the storage, a blower installed in this communication pipe, an open valve installed on the top of the storage, and a fuel containing carbon that is combusted to introduce carbon dioxide gas into the reserve. A combustion furnace, a blower that circulates air from the reserve storage to be used for combustion of the fuel in the combustion furnace, and an adsorber containing an adsorbent to adsorb excess carbon dioxide gas generated from the combustion furnace. The combustion furnace is provided downstream of the reserve storage, the blower is provided downstream of the fuel furnace, the adsorber is provided downstream of the blower, and the reserve storage is provided downstream of the adsorber. be. [0008]
【作用】本発明は、上記構成によって燃焼によって発生
するガスをすべて吸着器を通して予備庫に放出している
。この吸着器の中には、過剰な炭酸ガスを吸着するだけ
でなくエチレン等を吸着する吸着材を充填しているため
、貯蔵に有害なガスをすべて除去し得ることになる。
また、貯蔵庫には、貯蔵に適したガス濃度に調整したガ
スを、連通管を通じて送風機で予備庫より貯蔵庫内に導
入され、同時に貯蔵庫の天面の開放バルブが開放され、
貯蔵庫内の空気を貯蔵庫外に押出し、貯蔵に適したガス
環境にする。更に、貯蔵中も、貯蔵庫内に調整ガスを定
期的に充填し、貯蔵庫内のガスを開放バルブから貯蔵庫
外に押し出すことにより、貯蔵に有害なガスをすべて除
去し得ることになる。
[0009][Operation] According to the present invention, all the gases generated by combustion are discharged into the reserve storage through the adsorption device using the above-mentioned structure. This adsorber is filled with an adsorbent that not only adsorbs excess carbon dioxide gas but also adsorbs ethylene, etc., so all gases harmful to storage can be removed. In addition, gas adjusted to a gas concentration suitable for storage is introduced into the storage from the spare storage through a communication pipe using a blower, and at the same time, the release valve on the top of the storage is opened.
Pushes the air inside the storage out of the storage to create a gas environment suitable for storage. Furthermore, even during storage, by periodically filling the storage with regulated gas and forcing the gas inside the storage out of the storage through the open valve, all gases harmful to storage can be removed. [0009]
【実施例】以下本発明の一実施例の生鮮物貯蔵装置につ
いて図面を参照しながら説明する。
[00101図1は、本発明の実施例における生鮮物貯
蔵装置の構成を示すものである。図1において、1は生
鮮物を貯蔵するプレファプ冷蔵庫の如き貯蔵庫であり、
圧縮機2.凝縮器3.蒸発器4.送風機5.6より成る
冷却装置7を上部に載架している。
[00111前記貯蔵庫1に調整ガスを導入するために
調整ガスを貯める予備庫7aから、予備庫7aと貯蔵庫
1を連通する連通管7bに設けた送風機7Cによって貯
蔵庫lに導入される。この時同時に貯蔵庫1内の空気を
貯蔵庫1外に押出すために、貯蔵庫1−の天面に開放バ
ルブ7dを設けている。
[0012]また、予備庫7aに炭酸ガスを充填するた
めの炭酸ガス発生装置8と、燃焼ガスの中の過剰な炭酸
ガスを吸着して除去する炭酸ガス吸着装置9が接続され
ている。炭酸ガス発生装置8は、貯蔵庫1内の空気を導
入する導入管10と、ここで発生した燃焼ガスを炭酸ガ
ス吸着装置9に導く連結管11との間に配置され、燃焼
炉12及び燃焼ガスの冷却器13で構成されている。
[0013]14は送風機であり冷却器13と炭酸ガス
吸着装置9との間の連結管11に設け、導入管10より
予備庫7a内の空気を燃焼炉12に導き、更に燃焼炉1
2で発生した燃焼ガスを冷却器13で冷却した後、連結
管11により炭酸ガス吸着装置9に導く。
[0014]燃焼炉12は内面に断熱管15を備えた内
ケーシング16と、燃焼2次空気を供給するために内ケ
ーシング16との間に風路17を形成した外ケーシング
18と、断熱管15内で固形燃料19を載置する火格子
20と、燃焼空気を加熱して固形燃料19を燃焼させる
ための着火用ヒータ21とより構成されている。
[0015]固形燃料19は、純度の高い炭素であり燃
焼により燃焼ガスは炭酸ガスと窒素になる。
[0016]一方炭酸ガス吸着装置9は、燃焼ガスの中
の過剰な炭酸ガスを吸着し、貯蔵庫1外に排出するため
のものである。2基の吸着器22.23に対し、燃焼ガ
スが交互に循環するように導入管24,25、排出管2
6.27、及び流れを切替る切替バルブ28.29で構
成されている。
[0017]吸着器22.23内には、吸着材30,3
1が充填さねており、炭酸ガスを吸着し吸着能力が低下
すると、送風機32によって外気を切替バルブ33.排
出管26.27に接続している導入管34あるいは35
を通して吸着器22あるいは23に送風し、炭酸ガスを
脱着し、導入管24あるいは25に接続している排出管
36.37、切替バルブ38を通して排気管39より大
気に排気されるよう構成している。
[0018]例えば、吸着器22が吸着作用、吸着器2
3が脱着作用をしている時は、切替バルブ28.29は
、燃焼ガス導入管24.吸着器22.排出管26を通過
して流れる方向に開いており、また、切替バルブ33.
38は、外気が送風機32によって、導入管35゜吸着
器23.排出管37を通過して流れる方向に開いて、排
気管39より大気に排気される。
[0019]排気管40は、切替バルブ29と予備庫7
aを接続している。44は送風機14の風量を制御する
コントローラーであり、予備庫7a内のガス濃度を検知
するガスモニター45の信号によって風量は決定する。
46はチャンバーであり、導入管10に設けられた容器
であり、ガスモニター45のサンプリングチューブ47
を接続している。
[00201以上のように構成された生鮮物貯蔵装置に
ついて、図11図2を用いてその動作を説明する。予備
庫7a内の雰囲気は、最初窒素=79%、酸素=21%
であり、炭酸ガス発生装置8が運転されると、予備庫7
a内空気は、送風機14によって導入管10より、チャ
ンバー46を通って燃焼炉12へ導入され、着火用ヒー
タ21で加熱され固形燃料19の燃焼に供される。
[0021]燃焼ガスは炭酸ガスと窒素になって、冷却
器13で冷却した後、連結管11により、送風機1.4
を通過し、更に切替バルブ28.導入管24を通過して
吸着器22に入る。
[0022]ここで炭酸ガスは、吸着材30によって吸
着され窒素だけが、排出管26.切替バルブ29を通過
して排気管40により、予備庫7aへ循環する。一定時
間が経過すると、燃焼ガスが循環する吸着器が22から
23に切替わるべく、切替バルブ28.29が切替わり
、切替バルブ28.導入管25を通過して吸着器23に
入る。
[0023]そして、再び炭酸ガスは、吸着材31によ
って吸着され窒素だけが排出管27.切替バルブ29を
通過して排気管40により予備庫7aへ循環する。再び
一定時間が経過すると吸着器22.23が切替わり、交
互に燃焼ガスが循環する。この間に吸着器23.23の
中に充填された吸着材30.31は、炭酸ガスの吸着能
力の限界に達し、燃焼ガスの中の炭酸ガスは吸着しきれ
なくなり、排気管40を通って予備庫7a内に排気され
、予備庫7a内の炭酸ガス濃度は徐々に増加し始める。
75m2の大きさの予備庫7aで運転開始後約2時間の
状態である。
[0024]この間にも、予備庫7a内の酸素濃度は最
初21%より減少し続ける。予備庫7a内のガス濃度を
、酸素=5%、炭酸ガス=5%、窒素=90%を所定の
値とすると、予備庫7a内の炭酸ガスが増加して5%に
達したことを、ガスモニター45が、チャンバー46内
のガスサンプリングを行うことによって検知すると、炭
酸ガス吸着装置9の脱着用の送風機32が運転され、吸
着器内の吸着材の再生が開始される。
[0025]例えば、吸着器22が、燃焼ガスが循環し
て炭酸ガスを吸着していると、吸着器23は、送風機3
2によって外気が切替バルブ33.導入管35.排出管
27を通過し、吸着材31に送風されることによって炭
酸ガスが脱着され再生される。これが一定時間毎に交互
に行われるため、予備庫7a内の炭酸ガス濃度は所定の
5%を維持する。
[0026]一方酸素濃度は、その間も燃焼に供せられ
ているため、減少し続け、10時間後に所定の5%に達
し、これをガスモニター45が検知し、炭酸ガス発生装
置8及び炭酸ガス吸着装置9を停止させる。これで、予
備庫7a内が所定のガス濃度酸素=5%、炭酸ガス=5
%、窒素=90%となる。
[0027]それと同時に送風機7cが運転され、開放
バルブ7dが開放となり、予備庫7a内の調整ガスが貯
蔵庫1内に導入され、同時に貯蔵庫1内の空気が開放バ
ルブ7dより押出される。
[0028]予備庫7aの容積は、貯蔵庫1よりはるか
に大きいため、貯蔵庫1内の空気は、全量調整ガスに置
換され一定時間後に送風機7cは停止し、開放バルブ7
dは閉となる。
[00291これで、貯蔵庫1内は貯蔵に最適なガス環
境となった。これ以後、貯蔵庫1内に貯蔵している生鮮
物の呼吸作用によって発生する炭酸ガス及びエチレン等
のガスを除去するために定期的に予備庫7aより調整ガ
スが貯蔵庫1内に導入され、貯蔵庫]、内のガスは開放
バルブ7dより庫外に放出される。
[00301以上のように本発明は生鮮物を貯蔵する貯
蔵庫1と、この貯蔵庫1へ導入する調整ガスを貯める予
備庫7aと、予備庫7aと貯蔵庫1を連通する連通管7
aと、この連通管7bに設けた送風機7cと、貯蔵庫1
の天面に設けた開放バルブ7dと、この予備庫7a内へ
炭酸ガスを導入すべく炭素を含有する燃料19を燃焼さ
せる燃焼炉12と、この燃焼炉12に前記燃料19の燃
焼に供する空気を前記予備庫7aより循環せしめる送風
機14と、前記燃焼炉12から発生するガスの過剰な炭
酸ガスを吸着すべく吸着材30.31を入れた吸着器2
2.23とを備え、前記予備庫7aの下流に前記燃焼炉
12を、前記燃焼炉12の下流に前記送風機14を、前
記送風機14の下流に前記吸着器22.23を、前記吸
着器22.23の下流に前記予備庫7aを配設してなる
ものであるから、燃焼によって発生するガスをすべて吸
着器を通して予備庫に放出している。
[00311この吸着器の中には、過剰な炭酸ガスを吸
着するだけでなくエチレン等を吸着する吸着材を充填し
ているため、貯蔵に有害なガスをすべて除去し得ること
になる。
[0032]また、貯蔵庫には、貯蔵に適したガス濃度
に調整したガスを、連通管を通じて送風機で予備庫より
貯蔵庫内に導入され、同時に貯蔵庫の天面の開放バルブ
が開放され、貯蔵庫内の空気を貯蔵庫外に押出し、貯蔵
に適したガス環境にする。
[0033]更に、貯蔵中も、貯蔵庫内に調整ガスを定
期的に充填し、貯蔵庫内のガスを開放バルブから貯蔵庫
外に押し出すことにより、貯蔵に有害なガスをすべて除
去し得ることになる。
[0034]DESCRIPTION OF THE PREFERRED EMBODIMENTS A fresh produce storage apparatus according to an embodiment of the present invention will be described below with reference to the drawings. [00101 FIG. 1 shows the configuration of a fresh food storage device in an embodiment of the present invention. In FIG. 1, 1 is a storage such as a pre-fabricated refrigerator for storing perishables,
Compressor 2. Condenser 3. Evaporator 4. A cooling device 7 consisting of a blower 5.6 is mounted on the top. [00111] In order to introduce the regulated gas into the storage 1, the regulated gas is introduced into the storage 1 from the reserve 7a where the regulated gas is stored, by the blower 7C provided on the communication pipe 7b that communicates the reserve 7a and the storage 1. At this time, a release valve 7d is provided on the top surface of the storage 1- in order to push out the air inside the storage 1 to the outside of the storage 1. [0012] Further, a carbon dioxide gas generating device 8 for filling the reserve storage 7a with carbon dioxide gas and a carbon dioxide gas adsorption device 9 for adsorbing and removing excess carbon dioxide gas in the combustion gas are connected. The carbon dioxide gas generator 8 is arranged between an introduction pipe 10 that introduces air in the storage 1 and a connecting pipe 11 that leads the combustion gas generated here to the carbon dioxide adsorption device 9, and connects the combustion furnace 12 and the combustion gas. It is composed of a cooler 13. [0013] Reference numeral 14 denotes a blower, which is installed in the connecting pipe 11 between the cooler 13 and the carbon dioxide adsorption device 9, guides the air in the reserve storage 7a to the combustion furnace 12 through the introduction pipe 10, and further connects the combustion furnace 1 to the combustion furnace 1.
After the combustion gas generated in step 2 is cooled by a cooler 13, it is led to a carbon dioxide adsorption device 9 through a connecting pipe 11. [0014] The combustion furnace 12 includes an inner casing 16 having a heat insulating pipe 15 on its inner surface, an outer casing 18 having an air passage 17 formed between the inner casing 16 and the inner casing 16 for supplying secondary combustion air, and a heat insulating pipe 15. It is comprised of a grate 20 on which the solid fuel 19 is placed, and an ignition heater 21 for heating the combustion air to combust the solid fuel 19. [0015] The solid fuel 19 is highly pure carbon, and upon combustion, the combustion gas becomes carbon dioxide and nitrogen. [0016] On the other hand, the carbon dioxide adsorption device 9 is for adsorbing excess carbon dioxide in the combustion gas and discharging it outside the storage 1. The inlet pipes 24, 25 and the exhaust pipe 2 are connected to the two adsorbers 22 and 23 so that the combustion gas alternately circulates.
6.27, and a switching valve 28.29 for switching the flow. [0017] In the adsorber 22.23, the adsorbent 30, 3
1 is not fully filled and adsorbs carbon dioxide gas and the adsorption capacity decreases, the blower 32 switches the outside air to the switching valve 33. Inlet pipe 34 or 35 connected to outlet pipe 26.27
It is configured so that air is blown to the adsorber 22 or 23 through the inlet pipe 24 or 23, desorbs the carbon dioxide gas, and exhausts it to the atmosphere from the exhaust pipe 39 through the exhaust pipe 36, 37 connected to the inlet pipe 24 or 25 and the switching valve 38. . [0018] For example, the adsorber 22 has an adsorption effect, the adsorber 2
When the switching valves 28 and 29 are operating the combustion gas inlet pipes 24 and 24. Adsorber 22. It is open in the flow direction passing through the discharge pipe 26, and also has a switching valve 33.
38, outside air is supplied by the blower 32 to the inlet pipe 35° adsorber 23. It passes through the exhaust pipe 37, opens in the flow direction, and is exhausted to the atmosphere through the exhaust pipe 39. [0019] The exhaust pipe 40 is connected to the switching valve 29 and the reserve storage 7.
A is connected. 44 is a controller that controls the air volume of the blower 14, and the air volume is determined by a signal from a gas monitor 45 that detects the gas concentration in the reserve storage 7a. 46 is a chamber, which is a container provided in the introduction pipe 10, and a sampling tube 47 of the gas monitor 45.
are connected. [00201 The operation of the fresh food storage device configured as above will be explained using FIGS. 11 and 2. Initially, the atmosphere in the reserve storage 7a was nitrogen = 79% and oxygen = 21%.
When the carbon dioxide generator 8 is operated, the reserve storage 7
The air inside a is introduced into the combustion furnace 12 from the introduction pipe 10 through the chamber 46 by the blower 14, heated by the ignition heater 21, and used for combustion of the solid fuel 19. [0021] The combustion gas becomes carbon dioxide and nitrogen, and after being cooled by the cooler 13, it is sent to the blower 1.4 through the connecting pipe 11.
and further passes through the switching valve 28. It passes through the introduction pipe 24 and enters the adsorber 22. [0022] Here, carbon dioxide gas is adsorbed by the adsorbent 30, and only nitrogen is discharged from the exhaust pipe 26. It passes through the switching valve 29 and circulates through the exhaust pipe 40 to the reserve storage 7a. After a certain period of time has passed, the switching valves 28 and 29 are switched so that the adsorber through which the combustion gas circulates is switched from 22 to 23. It passes through the introduction pipe 25 and enters the adsorber 23. [0023] Then, carbon dioxide gas is adsorbed again by the adsorbent 31 and only nitrogen is discharged from the exhaust pipe 27. It passes through the switching valve 29 and circulates through the exhaust pipe 40 to the reserve storage 7a. After a certain period of time has elapsed again, the adsorbers 22 and 23 are switched, and the combustion gas is alternately circulated. During this time, the adsorbents 30 and 31 filled in the adsorbers 23 and 23 reach the limit of their adsorption capacity for carbon dioxide gas, and the carbon dioxide gas in the combustion gas is no longer able to be adsorbed. The gas is exhausted into the storage 7a, and the carbon dioxide concentration in the reserve storage 7a begins to gradually increase. The reserve storage 7a has a size of 75 m2 and has been in operation for about 2 hours since the start of operation. [0024] During this time, the oxygen concentration in the reserve storage 7a continues to decrease from the initial 21%. If the gas concentration in the reserve storage 7a is set to the predetermined values of oxygen = 5%, carbon dioxide = 5%, and nitrogen = 90%, then the carbon dioxide gas in the reserve storage 7a has increased to reach 5%. When the gas monitor 45 detects this by sampling the gas in the chamber 46, the blower 32 for desorption of the carbon dioxide adsorption device 9 is operated, and regeneration of the adsorbent in the adsorption device is started. [0025] For example, when the adsorber 22 is adsorbing carbon dioxide gas through circulation of combustion gas, the adsorber 23 is adsorbed by the blower 3
2, the outside air is switched off by the switching valve 33. Introductory tube 35. The carbon dioxide gas is desorbed and regenerated by passing through the exhaust pipe 27 and being blown onto the adsorbent 31 . Since this is performed alternately at regular intervals, the carbon dioxide concentration in the reserve storage 7a is maintained at a predetermined 5%. [0026] On the other hand, the oxygen concentration continues to decrease because it is being used for combustion during that time, and reaches the predetermined 5% after 10 hours.The gas monitor 45 detects this, and the carbon dioxide gas generator 8 and the carbon dioxide gas The adsorption device 9 is stopped. Now, the predetermined gas concentration in the reserve storage 7a is set to oxygen = 5% and carbon dioxide = 5%.
%, nitrogen = 90%. [0027] At the same time, the blower 7c is operated, the open valve 7d is opened, the regulated gas in the spare compartment 7a is introduced into the storage compartment 1, and at the same time, the air in the storage compartment 1 is pushed out through the open valve 7d. [0028] Since the volume of the reserve storage 7a is much larger than that of the storage 1, the air in the storage 1 is replaced with the full amount adjustment gas, and after a certain period of time, the blower 7c is stopped, and the open valve 7
d is closed. [00291 Now, the inside of the storage 1 has become the optimal gas environment for storage. From then on, in order to remove gases such as carbon dioxide and ethylene generated by the respiration of fresh foods stored in the storage 1, adjustment gas is periodically introduced into the storage 1 from the reserve storage 7a. , the gas inside is released to the outside of the refrigerator from the open valve 7d. [00301 As described above, the present invention provides a storage 1 for storing perishables, a reserve 7a for storing a regulated gas to be introduced into the storage 1, and a communication pipe 7 for communicating the reserve 7a and the storage 1.
a, the blower 7c provided in this communication pipe 7b, and the storage 1
a combustion furnace 12 for burning fuel 19 containing carbon to introduce carbon dioxide gas into the reserve storage 7a; and an air supply for combustion of the fuel 19 in the combustion furnace 12. a blower 14 that circulates carbon dioxide from the reserve storage 7a, and an adsorber 2 containing adsorbent 30, 31 to adsorb excess carbon dioxide gas generated from the combustion furnace 12.
2.23, the combustion furnace 12 is downstream of the reserve storage 7a, the blower 14 is downstream of the combustion furnace 12, the adsorbers 22 and 23 are downstream of the blower 14, and the adsorber 22 .23, the reserve storage 7a is disposed downstream of the combustion engine, so that all the gases generated by combustion are discharged into the reserve storage through the adsorption device. [00311 Since this adsorber is filled with an adsorbent that not only adsorbs excess carbon dioxide gas but also adsorbs ethylene, etc., all gases harmful to storage can be removed. [0032] In addition, gas adjusted to a gas concentration suitable for storage is introduced into the storage from the spare storage through a communication pipe with a blower, and at the same time, the open valve on the top of the storage is opened, and the gas inside the storage is opened. Pushes air out of the storage chamber to create a gas environment suitable for storage. [0033] Furthermore, even during storage, by periodically filling the storage with conditioning gas and forcing the gas in the storage out of the storage through the open valve, all gases harmful to storage can be removed. [0034]
【発明の効果】以上のように本発明は、生鮮物を貯蔵す
る貯蔵庫と、この貯蔵庫へ導入する調整ガスを貯める予
備庫と、予備庫と貯蔵庫を連通ずる連通管と、この連通
管に設けた送風機と、貯蔵庫の天面に設けた開放バルブ
と、この予備庫内へ炭酸ガスを導入すべく炭素を含有す
る燃料を燃焼させる燃焼炉と、この燃焼炉に前記燃料の
燃焼に供する空気を前記予備庫より循環せしめる送風機
と、前記燃焼炉から発生するガスの過剰な炭酸ガスを吸
着すべく吸着材を入れた吸着器とを備え、前記予備庫の
下流に前記燃焼炉を、前記燃焼炉の下流に前記送風機を
、前記送風機の下流に前記吸着器を、前記吸着器の下流
に前記予備庫を配設してなるものであるから、燃焼によ
って発生するガスをすべて吸着器を通して予備庫に放出
している。
[0035]この吸着器の中には、過剰な炭酸ガスを吸
着するだけでなくエチレン等を吸着する吸着材を充填し
ているため、貯蔵に有害なガスをすべて除去し得ること
になる。
[0036]また、貯蔵庫には、貯蔵に適したガス濃度
に調整したガスを、連通管を通じて送風機で予備庫より
貯蔵庫内に導入され、同時に貯蔵庫の天面の開放バルブ
が開放され、貯蔵庫内の空気を貯蔵庫外に押出し、貯蔵
に適したガス環境にする。
[0037]更に、貯蔵中も、貯蔵庫内に調整ガスを定
期的に充填し、貯蔵庫内のガスを開放バルブから貯蔵庫
外に押し出すことにより、貯蔵に有害なガスをすべて除
去し得ることになる。As described above, the present invention provides a storage for storing perishables, a reserve for storing the regulated gas to be introduced into the storage, a communication pipe for communicating the reserve and the storage, and a system provided in the communication pipe. an open valve installed on the top of the storage, a combustion furnace that burns fuel containing carbon to introduce carbon dioxide into the reserve storage, and a combustion furnace that supplies air for combustion of the fuel. The combustion furnace is equipped with a blower that circulates air from the reserve storage, and an absorber containing an adsorbent to adsorb excess carbon dioxide gas generated from the combustion furnace. The blower is installed downstream of the blower, the adsorber is placed downstream of the blower, and the reserve storage is provided downstream of the adsorber, so that all the gas generated by combustion passes through the adsorber to the reserve storage. It is emitting. [0035] Since this adsorber is filled with an adsorbent that not only adsorbs excess carbon dioxide gas but also adsorbs ethylene and the like, it is possible to remove all gases harmful to storage. [0036] In addition, gas adjusted to a gas concentration suitable for storage is introduced into the storage from the spare storage through a communication pipe with a blower, and at the same time, the open valve on the top of the storage is opened, and the gas inside the storage is opened. Pushes air out of the storage chamber to create a gas environment suitable for storage. [0037] Furthermore, even during storage, by periodically filling the storage with conditioning gas and forcing the gas in the storage out of the storage through the open valve, all gases harmful to storage can be removed.
【図1】本発明の一実施例における生鮮物貯蔵装置の構
成図FIG. 1 is a configuration diagram of a fresh food storage device according to an embodiment of the present invention.
【図2】図1の生鮮物貯蔵装置による庫内ガス成分の変
化図[Figure 2] Diagram of changes in internal gas components due to the fresh food storage device in Figure 1
【図3】従来の生鮮物貯蔵装置の系統図[Figure 3] System diagram of conventional fresh food storage equipment
1 貯蔵庫 12 燃焼炉 14 送風機 19 燃料 22、 23 吸着器 30.31 吸着材 7a 予備庫 7b 連通管 7c 送風機 7d 開放バルブ 1 Storage 12 Combustion furnace 14 Blower 19 Fuel 22, 23 Adsorption device 30.31 Adsorbent 7a Reserve storage 7b Communication pipe 7c Blower 7d Open valve
【図1】[Figure 1]
Claims (1)
へ導入する調整ガスを貯める予備庫と、予備庫と貯蔵庫
を連通する連通管と、この連通管に設けた送風機と、貯
蔵庫の天面に設けた開放バルブと、この予備庫内へ炭酸
ガスを導入すべく炭素を含有する燃料を燃焼させる燃焼
炉と、この燃焼炉に前記燃料の燃焼に供する空気を前記
予備庫より循環せしめる送風機と、前記燃焼炉から発生
するガスの過剰な炭酸ガスを吸着すべく吸着材を入れた
吸着器とを備え、前記予備庫の下流に前記燃焼炉を、前
記燃焼炉の下流に前記送風機を、前記送風機の下流に前
記吸着器を、前記吸着器の下流に前記予備庫を配設した
ことを特徴とする生鮮物貯蔵装置。Claim 1: A storage for storing perishables, a reserve for storing regulated gas to be introduced into the storage, a communication pipe for communicating the reserve and the storage, a blower installed in the communication pipe, and a ceiling for the storage. An open valve provided on the surface, a combustion furnace that burns fuel containing carbon to introduce carbon dioxide gas into the reserve storage, and a blower that circulates air from the reserve storage to the combustion furnace for combustion of the fuel. and an adsorber containing an adsorbent to adsorb excess carbon dioxide gas generated from the combustion furnace, the combustion furnace downstream of the reserve storage, the blower downstream of the combustion furnace, A fresh produce storage device characterized in that the adsorption device is provided downstream of the blower, and the reserve storage is provided downstream of the adsorption device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2402797A JPH04210522A (en) | 1990-12-17 | 1990-12-17 | Storage device of fresh material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2402797A JPH04210522A (en) | 1990-12-17 | 1990-12-17 | Storage device of fresh material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04210522A true JPH04210522A (en) | 1992-07-31 |
Family
ID=18512587
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2402797A Pending JPH04210522A (en) | 1990-12-17 | 1990-12-17 | Storage device of fresh material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04210522A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100457901B1 (en) * | 1995-06-28 | 2005-01-31 | 더 비오씨 그룹 피엘씨 | Atmosphere control system in the vessel |
-
1990
- 1990-12-17 JP JP2402797A patent/JPH04210522A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100457901B1 (en) * | 1995-06-28 | 2005-01-31 | 더 비오씨 그룹 피엘씨 | Atmosphere control system in the vessel |
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