JPS598552Y2 - Ripening gas supply device for citrus ripening processing equipment - Google Patents

Ripening gas supply device for citrus ripening processing equipment

Info

Publication number
JPS598552Y2
JPS598552Y2 JP19506981U JP19506981U JPS598552Y2 JP S598552 Y2 JPS598552 Y2 JP S598552Y2 JP 19506981 U JP19506981 U JP 19506981U JP 19506981 U JP19506981 U JP 19506981U JP S598552 Y2 JPS598552 Y2 JP S598552Y2
Authority
JP
Japan
Prior art keywords
ripening
gas
flow rate
valve body
valve
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
Application number
JP19506981U
Other languages
Japanese (ja)
Other versions
JPS58100595U (en
Inventor
倍敏 小谷
修 山本
Original Assignee
株式会社 愛知電機工作所
岩谷産業株式会社
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 株式会社 愛知電機工作所, 岩谷産業株式会社 filed Critical 株式会社 愛知電機工作所
Priority to JP19506981U priority Critical patent/JPS598552Y2/en
Publication of JPS58100595U publication Critical patent/JPS58100595U/en
Application granted granted Critical
Publication of JPS598552Y2 publication Critical patent/JPS598552Y2/en
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 本考案は柑橘類の追熟の追熟処理の際に使用する追熟ガ
スを処理室内に供給するガス供給装置の改良に関するも
のである。
[Detailed Description of the Invention] The present invention relates to an improvement of a gas supply device for supplying ripening gas into a processing chamber during the ripening process of citrus fruits.

従来より、未或熟の柑橘類を人為的に帝色させる手段と
して、エチレンガス雰囲気内において上記果実をさらす
ことが知られている。
BACKGROUND ART Conventionally, it has been known to expose unripe citrus fruits in an ethylene gas atmosphere as a means of artificially turning them yellow.

そして、追熟室に上記エチレンガス等の追熟ガスを供給
する装置は、第1図に示すように、ボンベソケット1に
ガス取出用の弁体2と水等の液体を正規位置まで注入し
た気泡式の流量観測器3とを順に直列接続し、取出され
るガスが上記観測器3の液体中を所定の大きさの気泡と
なって通過して図示しない追熟室に供給される方式のも
のが知られている。
As shown in Fig. 1, the apparatus for supplying the ripening gas such as ethylene gas to the ripening chamber has a gas extraction valve body 2 and a liquid such as water injected into the cylinder socket 1 to the proper position. A bubble-type flow rate observation device 3 is connected in series in order, and the extracted gas passes through the liquid of the observation device 3 as bubbles of a predetermined size and is supplied to a ripening chamber (not shown). something is known.

然るに、上記既知のものは、追熟室内が柑橘類の呼吸作
用が活発となる温度(約16℃)に達したとき、追熟処
理を良好に行なわせるために、最初は弁体2の二一ドル
弁4を操作して弁座5を大きく開口させて、追熟ガスを
追熟室内に大量に供給して追熟室内のガス濃度を所望値
まで、急速に上昇させ室内ガス濃度が所望値に達した後
は、再度二一ドル弁4を操作して弁座5の開口度を小さ
く絞って追熟ガスを柑橘類の追熟(;必要な量だけ定量
供給していたので、ガス供給量の調整は二一ドル弁4を
操作するだけでよいので、一見容易そうではあるが、追
熟処理の都度、最初は大量に、次は微少量と切換操作を
行う関係上、操作者は2系統のガス供給を切換える際は
、必ず観測器3により単位時間当りの気泡数を観測しな
がらガス供給を行なわないと、柑橘類の追熟処理に変調
をきたす虞れがあるため、上記二一ドル弁4の操作は細
心の注意をもって行う必要がった。
However, in the above-mentioned known method, when the temperature in the ripening chamber reaches a temperature (approximately 16°C) at which the respiration of citrus fruits becomes active, the second part of the valve body 2 is initially turned off in order to perform the ripening process well. Operate the dollar valve 4 to widen the valve seat 5, supply a large amount of ripening gas into the ripening chamber, and rapidly increase the gas concentration in the ripening chamber to the desired value, so that the indoor gas concentration reaches the desired value. After reaching this point, operate the 21 dollar valve 4 again to narrow the opening degree of the valve seat 5 to allow the ripening gas to ripen the citrus fruit. At first glance, it may seem easy to adjust the amount by simply operating the 21-dollar valve 4, but each time the ripening process is performed, the operator first has to switch between a large amount and then a very small amount. When switching the gas supply to the system, be sure to monitor the number of bubbles per unit time using the observation device 3 while supplying gas. Otherwise, there is a risk that the ripening process of citrus fruits will be affected. Valve 4 had to be operated with great care.

又、この弁操作はガス供給量の変更毎に行なわなければ
ならないので非常に手間がかかり面倒であった。
Further, this valve operation must be performed every time the gas supply amount is changed, which is very time-consuming and troublesome.

本考案は上述の欠点を除去して、追熟ガスを、最初は追
熟室内が適正ガス濃度となるまで大量に供給し、次に追
熟処理に最小眼必要な量だけ供給することができるよう
にガス供給装置の供給体系を最初に調節することにより
以後、上記2系統に区分した追熟ガスの供給係を柑橘類
の追熟処理毎に調節することなく自動的に供給可能とし
た新規な追熟ガス供給装置を提供するもので、以下本考
案の実施例を第2図乃至第5図により説明すると、11
は追熟室で、ほぼ密閉自在にしてかつ断熱構造に形或さ
れ、内部の片側空所には電動ファン12とヒータ13と
からなる空気調節装置14が設置されている。
The present invention eliminates the above-mentioned drawbacks and makes it possible to first supply a large amount of ripening gas until the proper gas concentration is reached in the ripening chamber, and then to supply only the minimum amount necessary for the ripening process. By first adjusting the supply system of the gas supply device, we have developed a new system that allows the supply of ripening gas divided into the two systems described above to be automatically supplied without having to adjust it every time citrus fruits are ripened. It provides a ripening gas supply device, and the embodiments of the present invention will be explained below with reference to FIGS. 2 to 5.
is a ripening chamber, which is designed to be almost airtight and has a heat insulating structure, and an air conditioning device 14 consisting of an electric fan 12 and a heater 13 is installed in a space on one side of the interior.

15は追熟室11内に配置された室温又は柑橘類の品温
を検出する温度検出センサ16からの信号に応じて、上
記空気調節装置14と後述する追熟ガス供給装置(以下
ガス供給装置と称する)17とを運転制御を行う制御装
置で、ガス供給装置17を収容して追熟室11の壁体等
に突気調節装置14と近接して取付けられる。
Reference numeral 15 indicates the air conditioning device 14 and a ripening gas supply device (hereinafter referred to as gas supply device), which will be described later, in response to a signal from a temperature detection sensor 16 arranged in the ripening chamber 11 that detects the room temperature or the temperature of citrus fruits. This control device controls the operation of the gas supply device 17 and is installed on the wall of the ripening chamber 11 in close proximity to the gust adjustment device 14.

.そして上述したガス供給装置17の構造を第2
図により詳述すると、18はガスボンベで、そのソケッ
ト部19には圧力調整弁20が連結され、この圧力調整
弁20の出口には、制御装置15がらの指令によって開
閉する第1および第2の電磁弁■1,■2をそれぞれ先
端に取付けた分岐管21の基端が連結されている。
.. Then, the structure of the gas supply device 17 described above is changed to a second one.
To explain in detail with reference to the figure, 18 is a gas cylinder, a pressure regulating valve 20 is connected to its socket 19, and the outlet of this pressure regulating valve 20 has first and second valves that are opened and closed by commands from the control device 15. The proximal ends of branch pipes 21 each having electromagnetic valves (1) and (2) attached to their tips are connected.

22は手動の微少流量調節弁(例えば二一ドル弁)23
を備えた弁体で、この弁体22の小径なガス入口24側
には第1の電磁弁V1が連結管25を介して連結され、
又、弁体22の大径なガス出口26側には連結管25′
を介して第2の電磁弁V2が連結される。
22 is a manual minute flow control valve (e.g. 21 dollar valve) 23
A first electromagnetic valve V1 is connected to the small diameter gas inlet 24 side of the valve body 22 via a connecting pipe 25,
Further, a connecting pipe 25' is connected to the large diameter gas outlet 26 side of the valve body 22.
A second electromagnetic valve V2 is connected via.

27は弁体22内のガス流路28の途中に設けた弁座で
、その開口度は微少流量調節弁23により調節すること
により、第1の電磁弁V1を介して弁体22内に流入す
る追熟ガスの弁体22外への流出量が規制される。
Reference numeral 27 denotes a valve seat provided in the middle of the gas flow path 28 in the valve body 22, and its opening degree is adjusted by the minute flow rate control valve 23 to allow gas to flow into the valve body 22 via the first electromagnetic valve V1. The amount of ripening gas flowing out of the valve body 22 is regulated.

29は第2の電磁弁■2と連通する弁体22のガス出口
26側と対応させて上記弁体22の胴部に螺装した調節
ボルト等からなる大流量調節弁で、ガス出口26の開口
度を調節することにより、第2の電磁弁V2から弁体2
2を通って流出されるガスの流量を規制する。
Reference numeral 29 denotes a large flow rate control valve consisting of a control bolt or the like screwed onto the body of the valve body 22 in correspondence with the gas outlet 26 side of the valve body 22 that communicates with the second electromagnetic valve (2). By adjusting the opening degree, the valve body 2 can be removed from the second solenoid valve V2.
regulating the flow rate of gas flowing out through 2;

30は弁体22の頭部に螺合した微少流量調節弁23の
操作摘、31は弁体22の下端に気密に連結された筒状
の逆止室で、内部には弁体22の出口孔32に連結され
た逆止管33が垂設されている。
Reference numeral 30 denotes an operation knob for the minute flow control valve 23 screwed onto the head of the valve body 22, and 31 denotes a cylindrical check chamber airtightly connected to the lower end of the valve body 22, with an outlet of the valve body 22 inside. A check pipe 33 connected to the hole 32 is provided vertically.

34は内部に水等の液体を約半分ほど注入した気泡式の
流量観測器で、その底部は導出管35によって上記逆止
室31と連通している。
Reference numeral 34 denotes a bubble-type flow rate measuring device into which approximately half of a liquid such as water is filled, and its bottom communicates with the check chamber 31 through an outlet pipe 35 .

36は流量観測器34は流量観測器34と空気調節装置
14との間に配管されたガス供給管である。
Reference numeral 36 denotes a gas supply pipe that is connected between the flow rate observation device 34 and the air conditioning device 14 .

尚、第lおよび第2の電磁弁Vl,V2は、制御装置1
5からの指令により、最初は弁体22のガス出口26側
と連通ずる第2の電磁弁■2が、次にガス入口24側と
連通ずる第1の電磁弁■1が作動するように設定されて
いる。
Note that the first and second solenoid valves Vl and V2 are connected to the control device 1.
5, the second solenoid valve ■2 communicating with the gas outlet 26 side of the valve body 22 is set to operate first, and then the first solenoid valve ■1 communicating with the gas inlet 24 side is set to operate. has been done.

本考案は上述のような構戊をなし、次にその動作につい
て説明すると、先づ、弁体22の大径なガス出口26の
開口度の調節は、大流量調節弁29により徐々に大きく
しながら、第1の電磁弁V2弁体22一逆止室31を経
て流量観測器34内を通過する際に生ずる追熟ガスの単
位時間当りの気泡数を観測することによって設定する。
The present invention has the above-mentioned structure, and its operation will be explained next. First, the opening degree of the large-diameter gas outlet 26 of the valve body 22 is adjusted by gradually increasing the opening degree using the large-flow control valve 29. However, it is set by observing the number of bubbles per unit time of the ripening gas that is generated when passing through the first solenoid valve V2 valve body 22, the check chamber 31, and the inside of the flow rate observation device 34.

次に、弁体22の弁座27の開口度の調節は、第2の電
磁弁V2を一旦閉弁してから弁体22のガス人口24と
連通ずる第1の電磁弁V1を開弁したあと、操作摘30
を操作して微少量調節弁23により弁座27の開口度を
徐々に開き、前述同様に流量観測器34内に生ずる追熟
ガスの単位時間当りの気泡数を観測しながら設定する。
Next, the degree of opening of the valve seat 27 of the valve body 22 was adjusted by once closing the second solenoid valve V2 and then opening the first solenoid valve V1 communicating with the gas port 24 of the valve body 22. Also, 30 operations
The degree of opening of the valve seat 27 is gradually opened by operating the minute amount control valve 23, and the opening degree is set while observing the number of bubbles per unit time of the ripening gas generated in the flow rate observation device 34 as described above.

このように、弁体22の2系統のガス流量を設定したあ
と、空気調節装置14を運転させ、この空気調節装置1
4で発生させた追熟用の加温空気を追熟室11内に循環
させる。
After setting the gas flow rates of the two systems of the valve body 22 in this way, the air conditioning device 14 is operated, and the air conditioning device 1
The heated air for ripening generated in step 4 is circulated inside the ripening chamber 11.

このようにして室内温度が徐々に上昇してゆき、予しめ
設定された値(約16℃)に達すると、温度検出センサ
16で検出され、その検出信号が制御装置15に送られ
て制御装置15が起動される。
In this way, the indoor temperature gradually rises, and when it reaches a preset value (approximately 16 degrees Celsius), it is detected by the temperature detection sensor 16, and the detection signal is sent to the control device 15. 15 is activated.

この結果、制御装置15からの指令により、第2の電磁
弁V2が開弁されて、ガスボンベ18内の追熟ガスは、
上記電磁弁V2一連結管25′一弁体22のガス出口2
6一逆止管33一逆止室31一導出管35一流量観測器
34−ガス供給管36を経て追熟室11内に連続的に給
送される。
As a result, the second solenoid valve V2 is opened in response to a command from the control device 15, and the ripening gas in the gas cylinder 18 is
The above solenoid valve V2 series connection pipe 25' - gas outlet 2 of the valve body 22
6 - Check pipe 33 - Check chamber 31 - Outlet pipe 35 - Flow rate observation device 34 - Gas supply pipe 36 and are continuously fed into the ripening chamber 11.

この際、弁体22の大径なガス出口26から流出される
追熟ガスの単位時間当りのガス流量q1は大流量調節弁
29により約400 〜500 cc/minに設定さ
れる。
At this time, the gas flow rate q1 per unit time of the ripening gas flowing out from the large-diameter gas outlet 26 of the valve body 22 is set to about 400 to 500 cc/min by the large flow rate control valve 29.

又、第2の電磁弁■2が制御されている時間T1は制御
装置15内に組込まれているタイマ等により任意(1〜
9分)に設定される。
Further, the time T1 during which the second solenoid valve 2 is controlled can be set arbitrarily (1 to 1) by a timer etc. built into the control device 15.
9 minutes).

この時間T1内で室内のガス濃度を所要値(3〜20p
pm)まで上げる。
Within this time T1, reduce the indoor gas concentration to the required value (3 to 20p).
pm).

上記設定時間T1が経過すると、制御装置15からの指
令により第2の電磁弁■2は閉弁され、代りに、第1の
電磁弁V1が制御装置15からの指令により開弁されて
、追熱ガスは連結管25一弁体22の小径なガス人口2
4一弁座27−ガス流通路28一逆止管33一逆止室3
1一導出管35一流量観測器34−ガス供給管36を経
て単位時間当りの流量q2が約1〜1.5cc mi
nに設定された状態で追熟室11に微少量連続的に供給
される。
When the set time T1 has elapsed, the second solenoid valve V2 is closed by a command from the control device 15, and instead, the first solenoid valve V1 is opened by a command from the control device 15. The hot gas is passed through a small diameter gas population 2 between the connecting pipe 25 and the valve body 22.
41 Valve seat 27 - Gas flow passage 28 - Check pipe 33 - Check chamber 3
The flow rate q2 per unit time is approximately 1 to 1.5 cc mi through the 1-output pipe 35-flow rate observation device 34-gas supply pipe 36.
A very small amount is continuously supplied to the ripening chamber 11 in a state where the temperature is set to n.

追熟ガスの微少量供給は、制御装置15からの指令によ
り追熟処理が終了するまで行なわれる。
The very small amount of ripening gas is supplied according to a command from the control device 15 until the ripening process is completed.

このように、追熟ガスを微少量追熟室11内に供給して
いる間も、空気調節装置14によって加温された空気に
より追熟室11内の温度を徐々に上昇させ、目標温度(
約22℃)に達した以降は、この温度を維持させるため
に空気調節装置14を制御装置15の指令により断続運
転させる。
In this way, even while supplying a small amount of ripening gas into the ripening chamber 11, the temperature inside the ripening chamber 11 is gradually increased by the air heated by the air conditioning device 14, and the target temperature (
After reaching approximately 22° C., the air conditioning device 14 is operated intermittently according to a command from the control device 15 in order to maintain this temperature.

そして、この目標温度を約一昼夜保持させて柑橘類の追
熟処理を行う。
Then, this target temperature is maintained for about a day and night to ripen the citrus fruits.

追熟処理が終了すれば、制御装置15からの指令により
第1の電磁弁V1は閉弁されて追熟ガスの供給を停止さ
せる。
When the ripening process is completed, the first electromagnetic valve V1 is closed by a command from the control device 15, and the supply of the ripening gas is stopped.

併せて、空気調節装置14のヒータも通電が停止され、
電動ファン12のみ運転されて、追熟室11内の空気の
循環を行なわせる。
At the same time, the heater of the air conditioning device 14 is also de-energized,
Only the electric fan 12 is operated to circulate the air inside the ripening chamber 11.

次に、別の柑橘類を追熟処理する際は、前記同様にして
行うが、その際、追熟ガスの供給は、既に、大量系およ
び微少量系ともガス流量は最初に、弁体22の微少流量
調節弁23,大流量調節弁29によりそれぞれ調節設定
されているため、追熟室11へのガス供給は特別に弁体
22から流出量を調節することなく自動的に行うことが
できる。
Next, when another citrus fruit is ripened, it is carried out in the same manner as described above, but at that time, the supply of ripening gas has already started at the gas flow rate of the valve body 22 in both the large-volume system and the very small-quantity system. Since the small flow rate control valve 23 and the large flow rate control valve 29 are adjusted and set, the gas supply to the ripening chamber 11 can be automatically performed without specifically adjusting the flow rate from the valve body 22.

以上説明したように、本考案による追熟ガス供給装置は
、ガスボンベと弁体との間に、追熟ガスの大量供給系と
微少量供給系とのそれぞれの流路を開閉せしめる第1お
よび第2の電磁弁を配設し、上記弁体には、大量供給系
と微少量供給系の各流出量を所要値に設定するための大
流量調節弁と微少流量調節弁を上記弁体のガス流通路に
流量調節作動可能に配置し、これら大流量調節弁および
微少流量調節弁を追熟ガスが所要量流出するように最初
に調節設定するだけで、以後、柑橘類の追熟処理毎に上
記弁体の微少量調節弁と大流量調節弁とを調節すること
なく追熟ガスを常に2系統に区分した状態で追熟室に供
給可能としたもので、従来のように、柑橘類の追熟処理
の都度、最初は室内を適正なガス濃度にするために追熟
ガスを大量に供給し、次は柑橘類の追熟に消費される量
だけ追熟ガスを微少量供給するための操作をガスボンベ
と連結する弁体の二一ドル弁によって行うものとは全く
異なり、本案は大量供給系と、微少量供給系との二つの
ガス流通路によってガスボンベと弁体との間を、各供給
系統の途中に電磁弁を配設させて接続し、弁体には各供
給系における弁体からのガス流量を調節する大流量調節
弁と微少量調節弁とを個々に備えているため、追熟ガス
の供給に際しては、最初に、上記2系統のガスの流量を
弁体に個々に設けた調節弁により調節設定するだけで、
あとは追熟処理毎に上記2系統のガス流量を調節する必
要は全くないので、追熟処理毎にガスの供給量ガスが不
安定となって追熟むらが生じたり、追熟処理の都度ガス
流量を調節する手間やわずらわしさを一掃することがで
きる利点がある。
As explained above, the ripening gas supply device according to the present invention has a first and a second passageway between the gas cylinder and the valve body that open and close the passages for the large quantity supply system and the very small quantity supply system of the ripening gas. 2 electromagnetic valves are installed on the valve body, and a large flow rate control valve and a minute flow rate control valve are installed on the valve body to set the respective outflow rates of the large volume supply system and the small volume supply system to the required values. Simply place the large flow rate control valve and small flow rate control valve in the flow path so that the required amount of ripening gas flows out. This system enables the ripening gas to be constantly divided into two systems and supplied to the ripening chamber without adjusting the micro-volume control valve and large-flow control valve on the valve body. Each time a process is carried out, a large amount of ripening gas is first supplied to bring the room to the appropriate gas concentration, and then a small amount of ripening gas is supplied in the amount consumed for ripening the citrus fruits using a gas cylinder. This is completely different from the method using a 21-dollar valve with a valve body connected to the gas cylinder, and this proposal uses two gas flow paths, a large quantity supply system and a minute quantity supply system, to connect the gas cylinder and the valve body to each supply system. A solenoid valve is installed in the middle of the connection, and each valve body is equipped with a large flow rate control valve and a small amount control valve that adjust the gas flow rate from the valve body in each supply system, so that the aging gas can be easily controlled. When supplying gas, first, simply adjust and set the flow rates of the two gases using individual control valves installed on the valve body.
There is no need to adjust the gas flow rate of the two systems mentioned above for each ripening process, so the gas supply amount becomes unstable for each ripening process, causing uneven ripening. This has the advantage of eliminating the hassle and hassle of adjusting the gas flow rate.

又、追熟ガスの供給系統を大量系と微少量系とに区分し
たので、追熟処理の過程においてガスの供給量を変更す
る必要はなく、シかも、各供給系統には、温度検出セン
サの検出信号により作動する制御装置の指令によって開
閉する電磁弁が個々に配設されているので、追熟ガスは
各供給系統において追熟室内がガス噴出温度まで上昇す
ると、自動的に開弁じて所要量の追熟ガスを自動供給す
ることができ、しかも、ガスの供給開始は電磁弁が予じ
め定められた温度検出センサによって検出される温度に
応じて行い得るので、追熟ガスが低温時に供給されるこ
とによって柑橘類かへ夕枯れ等をおこす虞れは全くない
In addition, since the ripening gas supply system is divided into a large amount system and a very small amount system, there is no need to change the gas supply amount during the ripening process, and each supply system is equipped with a temperature detection sensor. Since the solenoid valves are individually installed to open and close according to the commands of the control device activated by the detection signal of The required amount of ripening gas can be automatically supplied, and the gas supply can be started according to the temperature detected by the solenoid valve by a predetermined temperature detection sensor. There is no risk that citrus fruits will suffer from wilt due to frequent supply.

更に、追熟ガスは必要時に必要量連続して供給すること
ができるので追熟ガスの供給をむだなく能率的に行うこ
とができる等実用上幾多のすぐれた効果を有するもので
ある。
Furthermore, since the ripening gas can be continuously supplied in the required amount when necessary, the ripening gas can be supplied efficiently without waste, and has many excellent practical effects.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は従来の追熟ガス供給装置の一部切欠縦断正面図
、第2図は本考案の追熟ガス供給装置の要部を縦断した
正面図、第3図は本考案装置を備えた柑橘類追熟装置の
概略図、第4図は本案装置の使用状態を説明する説明図
、第5図はガス供給作動特性を示す線図である。 18・・・・・・ガスボンベ、22・・・・・・弁体、
23・・・・・・微少流量調節弁、29・・・・・・大
流量調節弁、34・・・・・・流量観測器、Vl,V2
・・・・・・電磁弁。
Fig. 1 is a partially cutaway longitudinal front view of a conventional ripening gas supply device, Fig. 2 is a longitudinal sectional front view of the main part of the ripening gas supply device of the present invention, and Fig. 3 is a longitudinal sectional front view of a conventional ripening gas supply device. FIG. 4 is a schematic diagram of the citrus ripening device, FIG. 4 is an explanatory diagram illustrating the usage state of the device, and FIG. 5 is a diagram showing gas supply operating characteristics. 18... Gas cylinder, 22... Valve body,
23...Minor flow rate control valve, 29...Large flow rate control valve, 34...Flow rate observation device, Vl, V2
······solenoid valve.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] ガスボンベに追熟ガス取出用の弁体と気泡式の流量観測
器とを順に直列接続し、取出されるガスが流量観測器の
流体中を気泡どなって通過する上記気泡数を観測してガ
スの流量を調節して追熟室に追熟ガスを供給するようは
した追熟ガス供給装置において、上記ガスボンベと弁体
との間に追熟ガスの大量供給系と微少量供給系との2系
統のガス流通路を形或し、上記各紙給系統の配管途中に
は追熟室内の温度に応じて開閉作動する電磁弁を配設し
、上記弁体には大量供給系の流量を調節する大流量調節
弁と、微少量系の流量を調節する微少量調節弁とをそれ
ぞれ上記弁体内のガス流路に流量調節作動可能に取付け
て或る柑橘類の追熟処理装置における追熟ガス供給装置
A valve body for extracting ripening gas and a bubble-type flow rate observation device are connected in series to the gas cylinder, and the number of bubbles is observed as the gas to be extracted passes through the fluid of the flow rate observation unit. In a ripening gas supply device that supplies ripening gas to a ripening chamber by adjusting the flow rate of the ripening gas, there are two systems, a large amount supply system and a very small amount supply system, of the ripening gas between the gas cylinder and the valve body. A solenoid valve that opens and closes depending on the temperature in the ripening chamber is installed in the middle of the piping of each paper feeding system, and the valve body is used to adjust the flow rate of the mass supply system. A ripening gas supply device in a certain citrus fruit ripening processing apparatus, in which a large flow rate control valve and a minute amount control valve for adjusting the flow rate of a minute amount system are respectively attached to the gas passages in the valve body so as to be operable to adjust the flow rate. .
JP19506981U 1981-12-29 1981-12-29 Ripening gas supply device for citrus ripening processing equipment Expired JPS598552Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19506981U JPS598552Y2 (en) 1981-12-29 1981-12-29 Ripening gas supply device for citrus ripening processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19506981U JPS598552Y2 (en) 1981-12-29 1981-12-29 Ripening gas supply device for citrus ripening processing equipment

Publications (2)

Publication Number Publication Date
JPS58100595U JPS58100595U (en) 1983-07-08
JPS598552Y2 true JPS598552Y2 (en) 1984-03-16

Family

ID=30108357

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19506981U Expired JPS598552Y2 (en) 1981-12-29 1981-12-29 Ripening gas supply device for citrus ripening processing equipment

Country Status (1)

Country Link
JP (1) JPS598552Y2 (en)

Also Published As

Publication number Publication date
JPS58100595U (en) 1983-07-08

Similar Documents

Publication Publication Date Title
KR102609383B1 (en) Coffee-based beverage manufacturing machine and its manufacturing method and program
GB1212527A (en) Improvements in or relating to lung ventilating apparatus
US20070125374A1 (en) Gas blender with auxiliary mixed gas outlet
JPS598552Y2 (en) Ripening gas supply device for citrus ripening processing equipment
SU738566A1 (en) Apparatus for keeping aquatic organisms
RU2163862C2 (en) Automatically controlled apparatus for feeding cutting fluid to cutting zone
JP2884757B2 (en) Constant flow device
JP2709639B2 (en) Heater device with cooler
JPS5898916A (en) Manufacturing device of semiconductor
US373400A (en) hamilton
CN219090718U (en) Nasal oxygen cannula humidifier
CN212646418U (en) Water vapor generator assembly
US3040742A (en) Inhalation therapy apparatus
GB1381458A (en) Process of and apparatus for texturing yarn
US6050132A (en) Method and apparatus for hyperbaric chamber gas discharge and pressure management
SU1711884A1 (en) Microclimatic chamber
JPH1137520A (en) Moisture supplying control device
JP3064226B2 (en) Automatic sterilization method and apparatus for pure water supply device
JPH028140Y2 (en)
JPS5869363A (en) Solar heat collector
SU1205914A1 (en) Apparatus for sterilization of diaphragmatic oxygenerator
US1476699A (en) Apparatus for producing local anaesthesia
JPH03284389A (en) Temperature controller of sterilizer
JPS63169984A (en) Cultivation apparatus
SU848510A1 (en) Device for moisture and heat treatment of sewn articles