JPH051024B2 - - Google Patents
Info
- Publication number
- JPH051024B2 JPH051024B2 JP2009446A JP944690A JPH051024B2 JP H051024 B2 JPH051024 B2 JP H051024B2 JP 2009446 A JP2009446 A JP 2009446A JP 944690 A JP944690 A JP 944690A JP H051024 B2 JPH051024 B2 JP H051024B2
- Authority
- JP
- Japan
- Prior art keywords
- nitrogen gas
- nitrogen
- liquefied
- liquefied nitrogen
- heat exchanger
- 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 - Lifetime
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/85—Food storage or conservation, e.g. cooling or drying
Landscapes
- Freezing, Cooling And Drying Of Foods (AREA)
Description
【発明の詳細な説明】
<産業上の利用分野>
本発明は、液化窒素を用いた薬剤などの無菌化
凍結装置に関し、主にバイアル瓶などに充填する
凍結薬剤を微生物、塵埃などの汚染から防護し
て、安全に凍結できるものを提供する。[Detailed Description of the Invention] <Industrial Application Field> The present invention relates to a device for sterilizing and freezing drugs and the like using liquefied nitrogen, and is mainly used to protect frozen drugs filled into vials from contamination by microorganisms, dust, etc. Provide something that can be protected and safely frozen.
<従来技術>
従来、液化窒素を用いた薬剤などの凍結粉末化
は、液化窒素ガスボンベから導出した液化窒素の
極低温液の中に、対象となる薬剤を直接的に浸漬
して行つていた。<Prior art> Conventionally, the freezing and powdering of drugs using liquefied nitrogen was carried out by directly immersing the target drug into a cryogenic liquid of liquefied nitrogen extracted from a liquefied nitrogen gas cylinder. .
<発明が解決しようとする課題>
しかしながら、上記従来技術では、元来、液化
窒素中に微量の塵埃や雑菌が混入していることは
避けられず、液化窒素を接触させて被処理物を凍
結する場合、通常の畜肉、魚肉などの食品では比
較的問題が少ないが、バイアル瓶充填用、或は、
注射器充填用の薬剤では人体への影響を考慮すれ
ば問題は大きい。<Problems to be Solved by the Invention> However, in the above-mentioned conventional technology, it is unavoidable that trace amounts of dust and germs are mixed into the liquefied nitrogen, and the object to be treated is frozen by bringing the liquefied nitrogen into contact with it. There are relatively few problems with normal foods such as meat and fish, but for filling vials or
Medications for filling syringes pose a serious problem when considering the effects on the human body.
本発明は、液化窒素を用いて被処理物を凍結す
る場合、雑菌や塵埃などの汚染を円滑に除去する
ことを技術的課題とする。 A technical problem of the present invention is to smoothly remove contamination such as germs and dust when freezing a processed object using liquefied nitrogen.
<課題を解決するための手段>
上記課題を解消する手段を、実施例に対応する
図面を用いて以下に説明する。<Means for Solving the Problems> Means for solving the above problems will be described below using drawings corresponding to embodiments.
即ち、本第1発明は、液化窒素供給源7を気化
手段8を介して過装置3に接続し、過装置3
を窒素ガス供給路4で凍結室5に接続して、液化
窒素を気化手段8で気化して窒素ガスとし、窒素
ガスを過装置3に通し、極低温状態の窒素ガス
を窒素ガス供給路4で凍結室5に送り、凍結室5
に収容した被処理物に当該窒素ガスを接触させ
て、被処理物を極低温の窒素ガスで凍結するよう
に構成したことを特徴とする液化窒素を用いた無
菌化凍結装置である。 That is, the first invention connects the liquefied nitrogen supply source 7 to the filter device 3 via the vaporization means 8, and
is connected to the freezing chamber 5 through the nitrogen gas supply path 4, the liquefied nitrogen is vaporized by the vaporization means 8 to form nitrogen gas, the nitrogen gas is passed through the filtration device 3, and the nitrogen gas in a cryogenic state is passed through the nitrogen gas supply path 4. and send it to freezing chamber 5.
This is a sterilization freezing apparatus using liquefied nitrogen, characterized in that the object to be processed is brought into contact with the nitrogen gas and the object to be processed is frozen with extremely low temperature nitrogen gas.
また、第2発明は、上記第1発明において、窒
素ガス供給路4に熱交換器15を介在させ、窒素
ガス供給路4を通る窒素ガスと、液化窒素供給源
7から導出された液化窒素とを熱交換器15内に
熱交換可能に流し、当該液化窒素を熱交換器15
から気化手段8に流すように構成して、
気化手段8での気化により高温になつた上記窒
素ガスに液化窒素の冷熱を付与して、熱交換器1
5内で高温の窒素ガスを極低温に冷却するように
構成したものである。 Further, in a second invention, in the first invention, a heat exchanger 15 is interposed in the nitrogen gas supply path 4, and the nitrogen gas passing through the nitrogen gas supply path 4 and the liquefied nitrogen derived from the liquefied nitrogen supply source 7 are combined. is passed through the heat exchanger 15 in a heat exchangeable manner, and the liquefied nitrogen is passed through the heat exchanger 15.
The nitrogen gas, which has become high in temperature due to vaporization in the vaporization means 8, is supplied with the cold heat of the liquefied nitrogen, and is then passed through the heat exchanger 1.
5, the high-temperature nitrogen gas is cooled to an extremely low temperature.
上記被処理物とは、バイアル瓶に充填した薬
剤、或は、注射器に充填するための薬剤を初めと
して、畜肉や魚肉などの生肉、その他の食品をも
包含する。 The above-mentioned objects to be processed include not only medicines filled into vials or medicines to be filled into syringes, but also raw meat such as livestock meat and fish meat, and other foods.
上記気化手段とは、加熱器、熱交換器などのベ
イパライザをいう。 The vaporizer means a vaporizer such as a heater or a heat exchanger.
上記過装置とは、例えば、除菌フイルターな
どであつて、微生物、塵埃などの微細物を過・
除去するものをいう。 The above-mentioned filtration device is, for example, a sterilization filter, which filters microorganisms, dust, and other microscopic substances.
Refers to what is removed.
上記凍結室に供給する窒素ガスは、
気化により高温化した窒素ガスを、上記第2
発明に示すように、液化窒素の冷熱で冷却して
極低温にしても良いし、
気化手段の調整により、液化窒素を気化した
時点で窒素ガスを極低温状態にするようにして
も差し支えない(但し、この場合には、低温使
用の可能な過装置が必要である)。 The nitrogen gas supplied to the freezing chamber is the nitrogen gas heated to high temperature by vaporization, and is
As shown in the invention, the nitrogen gas may be cooled to an extremely low temperature by using the cold energy of liquefied nitrogen, or the nitrogen gas may be brought to an extremely low temperature at the time the liquefied nitrogen is vaporized by adjusting the vaporization means ( However, in this case, a filtration device that can be used at low temperatures is required.)
上記凍結室は、極低温窒素ガスを被処理物に直
接吹き付けて凍結するようにしても、
室内に極低温窒素ガスを充満させて、窒息ガス
雰囲気に被処理物を接触させるように構成しても
差し支えない。 The above-mentioned freezing chamber is configured so that the object to be processed is directly sprayed with cryogenic nitrogen gas to freeze it, or the chamber is filled with cryogenic nitrogen gas and the object to be processed is brought into contact with a suffocating gas atmosphere. There is no problem.
<作用> (1) 第1発明では、下記のとおり作用する。<Effect> (1) The first invention operates as follows.
液化窒素供給源7から導出された液化窒素
は、気化手段で一旦窒素ガスの気体にされたの
ち、過装置3を通過する際に、
細菌、糸状菌、酵母などの微生物を除菌さ
れ、
微細な塵埃を徐塵される。 The liquefied nitrogen derived from the liquefied nitrogen supply source 7 is once converted into nitrogen gas by the vaporization means, and then, when passing through the filtration device 3, microorganisms such as bacteria, filamentous fungi, and yeast are removed and microorganisms are removed. Dust is removed.
この場合、過装置3の過対象は気体であ
つて液体ではないので、過精度を高めてより
微細な微生物或は塵埃を有効に除去できる。 In this case, since the target of the filtering device 3 is gas and not liquid, the precision can be increased and finer microorganisms or dust can be effectively removed.
一般に、微生物は、液化窒素を気化手段で加
熱して窒素ガスにする際に、ある程度は死滅す
るはずであるが、当該加熱によつても殺菌の容
易でないバチルス属(Bacillus)、クロストリ
ジウム属(Clostridium)などの耐熱性芽胞を
作る細菌をも過装置3で有効に除菌できる。 In general, microorganisms should be killed to some extent when liquefied nitrogen is heated with a vaporization means to turn it into nitrogen gas. ) and other bacteria that produce heat-resistant spores can be effectively sterilized using the filtration device 3.
また、気体を過処理するので、通過抵抗が
少なくなつて過装置3を小型化できる。 Furthermore, since the gas is overtreated, the passage resistance is reduced and the overtreatment device 3 can be made smaller.
過装置3を通過した液化窒素は、極低温の
状態で凍結室5に供給され、凍結室3内の被処
理物20を無菌化凍結する。 The liquefied nitrogen that has passed through the filtration device 3 is supplied to the freezing chamber 5 at an extremely low temperature to sterilize and freeze the object 20 in the freezing chamber 3 .
(2) 第2発明では、上記液化窒素供給源7から導
出された液化窒素は気化手段8で気化して、高
温の窒素ガスになるが、熱交換器15を通る際
に、液化窒素の冷熱で冷却されて極低温の窒素
ガスとなる。(2) In the second invention, the liquefied nitrogen derived from the liquefied nitrogen supply source 7 is vaporized by the vaporization means 8 to become high-temperature nitrogen gas, but when passing through the heat exchanger 15, the cold heat of the liquefied nitrogen is It is cooled down and becomes cryogenic nitrogen gas.
一方、液化窒素供給源7から出た直後の液化
窒素は、熱交換器15で窒素ガスから温熱をも
らつて昇温するので、気化手段15で付与され
る熱を低減して、気化エネルギーを省力化でき
る。 On the other hand, the liquefied nitrogen immediately after coming out of the liquefied nitrogen supply source 7 receives heat from the nitrogen gas in the heat exchanger 15 and increases its temperature, so the heat applied by the vaporization means 15 is reduced and the vaporization energy is saved. can be converted into
<発明の効果>
(1) 従来技術では、薬剤などの凍結手段である液
化窒素自体を除菌するという技術的思想はなか
つたのに対し、第1及び2発明では、液化窒素
を窒素ガスにしたうえで、過装置で除菌、徐
塵するので(除菌手段が過なので、特に、耐
熱性芽胞を作る細菌をもスムーズに除去できる
ので)、薬剤を初めとする被処理物を無菌化凍
結して、人体への安全を確保できる。<Effects of the Invention> (1) In the prior art, there was no technical idea to sterilize liquefied nitrogen itself, which is a means of freezing drugs, etc., whereas in the first and second inventions, liquefied nitrogen is converted into nitrogen gas. After that, it sterilizes and removes dust using a filtration device (because the sterilization method is filtration, even bacteria that produce heat-resistant spores can be smoothly removed), making the objects to be treated, including drugs, sterilized. Can be frozen to ensure safety for humans.
(2) 第1・2発明では、窒素を液体から気体に交
換したうえで過処理するので、より微細な雑
菌、塵埃まで強力に除去でき、安全度を高めら
れる。(2) In the first and second inventions, since nitrogen is exchanged from liquid to gas and then overtreated, even the smallest germs and dust can be strongly removed, increasing safety.
(3) 第2発明では、液化窒素の冷熱及び窒素ガス
の温熱を互いにうまく利用し合えるので、熱交
換効率を高め、気化手段を小型化できる。(3) In the second invention, since the cold heat of liquefied nitrogen and the warm heat of nitrogen gas can be effectively utilized, the heat exchange efficiency can be increased and the vaporization means can be downsized.
<実施例>
以下、本発明の実施例を図面に基づいて述べ
る。<Example> Hereinafter, an example of the present invention will be described based on the drawings.
図面は液化窒素使用式無菌化凍結装置の概略説
明図であつて、当該凍結装置は、液化窒素供給ラ
イン1、ヒータ式加熱器8、窒素ガス導入ライン
2、除菌フイルター3、窒素ガス導出ライン4及
び凍結室5を順番に接続して構成される。 The drawing is a schematic explanatory diagram of a sterilization freezing device using liquefied nitrogen, and the freezing device includes a liquefied nitrogen supply line 1, a heater type heater 8, a nitrogen gas introduction line 2, a sterilization filter 3, and a nitrogen gas outlet line. 4 and freezing chamber 5 are connected in order.
複数の液化窒素ボンベ6を組み合わせて液化窒
素供給源7を構成し、液化窒素供給源7を上記液
化窒素供給ライン1でヒータ式加熱器8に接続す
る。 A plurality of liquefied nitrogen cylinders 6 are combined to form a liquefied nitrogen supply source 7, and the liquefied nitrogen supply source 7 is connected to a heater type heater 8 through the liquefied nitrogen supply line 1.
上記加熱器8を窒素ガス導入ライン2を介して
除菌フイルター3に接続し、除菌フイルター3を
窒素ガス導出ライン4で凍結室5に接続する。 The heater 8 is connected to the sterilizing filter 3 via the nitrogen gas introduction line 2, and the sterilizing filter 3 is connected to the freezing chamber 5 via the nitrogen gas leading line 4.
上記除菌フイルター3はセラミツクス製の過
膜に被処理ガスを通す構造であつて、下記の特性
を持つ。 The sterilization filter 3 has a structure in which the gas to be treated passes through a ceramic membrane, and has the following characteristics.
過精度:0.2μm
常用圧力:2.0Kg/cm2
使用温度:−20℃〜0℃
最大流量:150m3/Hr
上記窒素ガス導入ライン2に温度センサ11を
臨ませ、加熱器8に温度制御装置12を連動し
て、温度センサ11からの検知温度信号を受けた
温度制御装置12が加熱器8の加熱温度を制御
し、導入ライン2を流れる窒素ガスを所定温度に
保持するように構成する。Overaccuracy: 0.2 μm Normal pressure: 2.0 Kg/cm 2 Operating temperature: -20°C to 0°C Maximum flow rate: 150 m 3 /Hr The temperature sensor 11 is placed on the nitrogen gas introduction line 2, and the temperature control device is placed on the heater 8. 12, the temperature control device 12 receives the detected temperature signal from the temperature sensor 11, controls the heating temperature of the heater 8, and maintains the nitrogen gas flowing through the introduction line 2 at a predetermined temperature.
上記窒素ガス導入ライン2の途中部を二股状に
分岐して、一方に可変絞り弁9aを、他方に可変
絞り弁9bと流量調整弁10とを各々付設する。 A midway portion of the nitrogen gas introduction line 2 is branched into two, and a variable throttle valve 9a is attached to one side, and a variable throttle valve 9b and a flow rate adjustment valve 10 are attached to the other side.
また、前記凍結室5に温度センサ13を付設
し、上記流量調整弁10に温度制御装置14を連
動して、温度センサ13からの検知温度信号を受
けた温度制御装置14が流量調整弁10の流量を
制御して凍結室5内の雰囲気を所定温度に保持す
るように構成する。 Further, a temperature sensor 13 is attached to the freezing chamber 5, and a temperature control device 14 is linked to the flow rate adjustment valve 10, so that the temperature control device 14, which receives the detected temperature signal from the temperature sensor 13, controls the flow rate adjustment valve 10. The atmosphere in the freezing chamber 5 is maintained at a predetermined temperature by controlling the flow rate.
一方、上記窒素ガス導出ライン4に熱交換器1
5を介在させ、窒素ガス導出ライン4の窒素ガス
と、前記液化窒素供給ライン1の液化窒素とを熱
交換可能に当該熱交換器15内に流し、除菌フイ
ルター3で除菌された窒素ガスを液化窒素の冷熱
で冷却するように構成する。 On the other hand, a heat exchanger 1 is connected to the nitrogen gas derivation line 4.
5, the nitrogen gas in the nitrogen gas derivation line 4 and the liquefied nitrogen in the liquefied nitrogen supply line 1 are passed through the heat exchanger 15 so as to be able to exchange heat, and the nitrogen gas sterilized by the sterilization filter 3 is passed through the heat exchanger 15. is configured to be cooled by the cold energy of liquefied nitrogen.
上記凍結室5には、窒素ガス導出ライン4で送
給された極低温窒素ガスが噴射ノズル16から噴
き込まれ、換気フアン17で撹拌されて、凍結室
5内を極低温に保持し、搬送ライン18により搬
送される被処理物20(例えば、点滴用薬液)を
凍結室5内で凍結して粉末化する。 Cryogenic nitrogen gas supplied through the nitrogen gas derivation line 4 is injected into the freezing chamber 5 from the injection nozzle 16, stirred by the ventilation fan 17 to maintain the inside of the freezing chamber 5 at an extremely low temperature, and then transported. The object to be treated 20 (for example, a medical solution for intravenous drip) conveyed by the line 18 is frozen and powdered in the freezing chamber 5 .
そこで、上記凍結装置の機能を説明する。 Therefore, the functions of the above-mentioned freezing device will be explained.
(1) 液化窒素供給ライン1から供給される−180
℃の液化窒素を熱交換器15で予め昇温したの
ち、加熱器8で気化して0℃の窒素ガスにす
る。(1) −180 supplied from liquefied nitrogen supply line 1
After the temperature of liquefied nitrogen at 0.degree. C. is raised in advance in a heat exchanger 15, it is vaporized in a heater 8 to become nitrogen gas at 0.degree.
この場合、加熱器8から排出される窒素ガス
は、上述のように、比較的高温での使用が条件
付けられた除菌フイルター3を通すために、一
旦0℃にまで昇温する必要があるが、当該窒素
ガスの温度は、温度制御装置12で温度制御さ
れる。 In this case, the nitrogen gas discharged from the heater 8 needs to be heated once to 0°C in order to pass through the sterilization filter 3, which is required to be used at relatively high temperatures, as described above. The temperature of the nitrogen gas is controlled by a temperature control device 12.
(2) 高温化された窒素ガスは、窒素ガス導入ライ
ン2で除菌フイルター3に通されて、細菌、糸
状菌などの微生物(特に、耐熱性芽胞を作る細
菌)を除菌され、微細な塵埃を除塵されて清浄
化される。(2) The heated nitrogen gas is passed through a sterilization filter 3 in the nitrogen gas introduction line 2, where microorganisms such as bacteria and filamentous fungi (especially bacteria that produce heat-resistant spores) are sterilized, and microorganisms are removed. Dust is removed and cleaned.
(3) 清浄化された高温の窒素ガスは、窒素ガス導
出ライン4で熱交換器15に送られて、−180℃
の液化窒素の冷熱を付与され、−170℃の極低温
に冷却される。(3) The purified high-temperature nitrogen gas is sent to the heat exchanger 15 through the nitrogen gas outlet line 4, and is heated to -180°C.
It is given the cold energy of liquefied nitrogen and cooled to an extremely low temperature of -170℃.
(4) 極低温の窒素ガスを吹き込まれた凍結室5
は、送給される窒素ガスの流量を流量調整弁1
0で制御されて、室温−80〜−100℃の範囲内
に低温保持される。(4) Freezing chamber 5 injected with cryogenic nitrogen gas
is the flow rate adjustment valve 1 of the nitrogen gas to be fed.
The temperature is maintained within the range of -80 to -100°C.
この結果、搬送ライン18で間欠的に搬送され
て凍結室5に入つた被処理物20は、液体状態P
から粉末状態Qに凍結粉末化される。 As a result, the workpiece 20 that has been intermittently transported by the transport line 18 and entered the freezing chamber 5 is in a liquid state P
It is frozen and powdered into a powder state Q.
図面は液化窒素使用式無菌化凍結装置の概略説
明図である。
1……液化窒素供給ライン、2……窒素ガス導
入ライン、3……過装置、4……窒素ガス導出
ライン、5……凍結室、7……液化窒素供給源、
8……気化手段、15……熱交換器、20……被
処理物。
The drawing is a schematic illustration of a sterilization freezing device using liquefied nitrogen. DESCRIPTION OF SYMBOLS 1...Liquefied nitrogen supply line, 2...Nitrogen gas introduction line, 3...Performance device, 4...Nitrogen gas derivation line, 5...Freezing chamber, 7...Liquid nitrogen supply source,
8... Vaporization means, 15... Heat exchanger, 20... Material to be treated.
Claims (1)
装置3に接続し、過装置3を窒素ガス供給路4
で凍結室5に接続して、液化窒素を気化手段8で
気化して窒素ガスとし、窒素ガスを過装置3に
通し、極低温状態の窒素ガスを窒素ガス供給路4
で凍結室5に送り、凍結室5に収容した被処理物
に当該窒素ガスを接触させて、被処理物を極低温
の窒素ガスで凍結するように構成したことを特徴
とする液化窒素を用いた無菌化凍結装置 2 窒素ガス供給路4に熱交換器15を介在さ
せ、窒素ガス供給路4を通る窒素ガスと、液化窒
素供給源7から導出された液化窒素とを熱交換器
15内に熱交換可能に流し、当該液化窒素を熱交
換器15から気化手段8に流すように構成して、 気化手段8での気化により高温になつた上記窒
素ガスに液化窒素の冷熱を付与して、熱交換器1
5内で高温の窒素ガスを極低温に冷却するによう
に構成したことを特徴とする請求項1に記載の液
化窒素を用いた無菌化凍結装置[Claims] 1. The liquefied nitrogen supply source 7 is connected to the filter device 3 via the vaporization means 8, and the filter device 3 is connected to the nitrogen gas supply path 4.
is connected to the freezing chamber 5, the liquefied nitrogen is vaporized into nitrogen gas by the vaporization means 8, the nitrogen gas is passed through the filtration device 3, and the nitrogen gas in a cryogenic state is passed through the nitrogen gas supply path 4.
The method uses liquefied nitrogen characterized in that it is configured to be sent to the freezing chamber 5 and brought into contact with the object to be treated stored in the freezing chamber 5, thereby freezing the object to be treated with extremely low temperature nitrogen gas. A heat exchanger 15 is interposed in the nitrogen gas supply path 4, and the nitrogen gas passing through the nitrogen gas supply path 4 and the liquefied nitrogen derived from the liquefied nitrogen supply source 7 are transferred into the heat exchanger 15. The liquefied nitrogen is configured to flow in a heat exchangeable manner from the heat exchanger 15 to the vaporizing means 8, and the cold heat of the liquefied nitrogen is imparted to the nitrogen gas which has become high temperature due to vaporization in the vaporizing means 8. heat exchanger 1
5. The sterilization freezing device using liquefied nitrogen according to claim 1, wherein the sterilization freezing device uses liquefied nitrogen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2009446A JPH03216174A (en) | 1990-01-17 | 1990-01-17 | Aseptic freezing device using liquefied nitrogen |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2009446A JPH03216174A (en) | 1990-01-17 | 1990-01-17 | Aseptic freezing device using liquefied nitrogen |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03216174A JPH03216174A (en) | 1991-09-24 |
| JPH051024B2 true JPH051024B2 (en) | 1993-01-07 |
Family
ID=11720521
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2009446A Granted JPH03216174A (en) | 1990-01-17 | 1990-01-17 | Aseptic freezing device using liquefied nitrogen |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03216174A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5046621B2 (en) * | 2006-11-24 | 2012-10-10 | 三菱重工業株式会社 | Refrigeration system and method of operating refrigeration system |
-
1990
- 1990-01-17 JP JP2009446A patent/JPH03216174A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03216174A (en) | 1991-09-24 |
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