JP2002052070A - Steam sterilizer and hot-air sterilizer - Google Patents
Steam sterilizer and hot-air sterilizerInfo
- Publication number
- JP2002052070A JP2002052070A JP2000241129A JP2000241129A JP2002052070A JP 2002052070 A JP2002052070 A JP 2002052070A JP 2000241129 A JP2000241129 A JP 2000241129A JP 2000241129 A JP2000241129 A JP 2000241129A JP 2002052070 A JP2002052070 A JP 2002052070A
- Authority
- JP
- Japan
- Prior art keywords
- heat storage
- heating
- heat
- storage material
- water
- 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
- 238000010438 heat treatment Methods 0.000 claims abstract description 90
- 230000001954 sterilising effect Effects 0.000 claims abstract description 80
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 77
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 75
- 239000007787 solid Substances 0.000 claims abstract description 56
- 239000007788 liquid Substances 0.000 claims abstract description 27
- 238000005338 heat storage Methods 0.000 claims description 211
- 239000011232 storage material Substances 0.000 claims description 100
- 238000012546 transfer Methods 0.000 claims description 36
- 239000002245 particle Substances 0.000 claims description 27
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 18
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 9
- 239000000395 magnesium oxide Substances 0.000 claims description 9
- 229910002651 NO3 Inorganic materials 0.000 claims description 6
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate group Chemical group [N+](=O)([O-])[O-] NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 4
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 claims description 4
- 239000000377 silicon dioxide Substances 0.000 claims description 4
- 230000005611 electricity Effects 0.000 abstract description 17
- 239000008236 heating water Substances 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 4
- 238000013021 overheating Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 15
- 238000010586 diagram Methods 0.000 description 7
- 239000011810 insulating material Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 238000012856 packing Methods 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 238000007599 discharging Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical class C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Landscapes
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、滅菌室内に飽和水
蒸気を充填して被滅菌物を滅菌する蒸気滅菌装置、およ
び乾燥した熱風を用いて滅菌室内の被滅菌物を滅菌する
乾熱滅菌装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a steam sterilizer for sterilizing an object to be sterilized by filling a sterilization chamber with saturated steam, and a dry heat sterilizer for sterilizing an object to be sterilized in a sterilization chamber using dry hot air. About.
【0002】[0002]
【従来の技術】病院等で使用される医療用器具や実験等
で使用される器具類の滅菌を行う滅菌装置として、蒸気
を用いた蒸気滅菌装置がある。蒸気滅菌装置といって
も、大きさや蒸気の発生方法によって様々な違いがあ
る。以下に説明する蒸気滅菌装置は、飽和水蒸気発生器
が圧力容器としての滅菌室内に設けられているものであ
る。つまり、滅菌室を構成する缶体の下部が水を貯留で
きる貯留部として設けられており滅菌室内で直接水蒸気
を発生させるものである。このような蒸気滅菌装置は卓
上に載置できるような程度まで小型化が図られた卓上型
蒸気滅菌装置や、あるいは缶体が上下に向くように配置
された縦型蒸気滅菌装置として構成される。2. Description of the Related Art As a sterilizer for sterilizing medical instruments used in hospitals and the like and instruments used in experiments, there is a steam sterilizer using steam. The steam sterilizer has various differences depending on the size and the method of generating steam. In the steam sterilizer described below, a saturated steam generator is provided in a sterilization chamber as a pressure vessel. That is, the lower part of the can constituting the sterilization chamber is provided as a storage part capable of storing water, and generates steam directly in the sterilization chamber. Such a steam sterilizer is configured as a table-top steam sterilizer whose size has been reduced to such a degree that it can be placed on a table, or as a vertical steam sterilizer in which cans are arranged so as to face up and down. .
【0003】図7に卓上型蒸気滅菌装置の配管系統図に
ついて示す。卓上型蒸気滅菌装置10の被滅菌物が収容
される滅菌室12は、圧力容器としての缶体11内に設
けられている。缶体11の内部には被滅菌物を載置する
ことができる載置板13が設けられており、缶体11内
の載置板13よりも上方が滅菌室12に形成される。缶
体11内の載置板13よりも下方には水を貯留すること
ができる貯留部14が形成されている。貯留部14内に
は水を加熱するためのヒータ16が設けられている。ヒ
ータ16は電気ヒータである。かかる卓上型蒸気滅菌装
置は、ヒータ16が発熱することによって貯留部14内
の水を蒸発させて水蒸気を発生させ、缶体11内に充満
した水蒸気の温度、湿度、圧力によって滅菌を行う。FIG. 7 shows a piping diagram of a tabletop steam sterilizer. A sterilization chamber 12 in which the object to be sterilized of the tabletop steam sterilizer 10 is stored is provided in a can 11 as a pressure vessel. A mounting plate 13 on which an object to be sterilized can be mounted is provided inside the can body 11, and a portion above the mounting plate 13 in the can body 11 is formed in the sterilization chamber 12. A storage portion 14 that can store water is formed below the mounting plate 13 in the can body 11. A heater 16 for heating water is provided in the storage unit 14. The heater 16 is an electric heater. In such a tabletop steam sterilizer, the heater 16 generates heat to evaporate water in the storage unit 14 to generate steam, and sterilizes the steam by filling the can 11 with the temperature, humidity, and pressure of the steam.
【0004】次に、図8に基づいて乾熱滅菌装置につい
て説明する。乾熱滅菌装置20は、水蒸気を用いて滅菌
を行うものではなく、乾燥した熱風によって滅菌を行う
装置である。したがって、滅菌効率は蒸気を用いる蒸気
滅菌装置よりも悪く、蒸気滅菌装置と比較して滅菌終了
まで時間がかかるが、被滅菌物に水分を付着させたくな
い場合などにはよく用いられる。Next, a dry heat sterilizer will be described with reference to FIG. The dry heat sterilizer 20 does not perform sterilization using steam, but is a device that performs sterilization using dry hot air. Therefore, the sterilization efficiency is lower than that of a steam sterilizer using steam, and it takes a longer time to complete the sterilization than a steam sterilizer, but it is often used when it is not desired to attach moisture to an object to be sterilized.
【0005】乾熱滅菌槽装置20は、被滅菌物を収容す
るための滅菌室22と、滅菌室22に隣接し、滅菌室2
2と二カ所でつながって設けられた加熱室23とを備え
ている。滅菌室22と加熱室23とをつなげた部分に
は、加熱室23内の加熱された空気を滅菌室22内へ送
り込むと共に、滅菌室22内の空気を加熱室23内に送
り込む空気循環手段24が設けられている。加熱室23
内には、空気を加熱するためのヒータ26が設けられて
いる。ヒータ26は、電気で加熱する電気ヒータが用い
られている。このように加熱手段としては電気ヒータを
採用することによって簡単な構造にすることができる。[0005] The dry heat sterilization tank device 20 includes a sterilization chamber 22 for accommodating the object to be sterilized, and a sterilization chamber 2 adjacent to the sterilization chamber 22.
2 and a heating chamber 23 connected at two locations. Air circulating means 24 that feeds the heated air in the heating chamber 23 into the sterilization chamber 22 and sends the air in the sterilization chamber 22 into the heating chamber 23 at a portion where the sterilization chamber 22 and the heating chamber 23 are connected. Is provided. Heating room 23
Inside, a heater 26 for heating air is provided. As the heater 26, an electric heater for heating with electricity is used. Thus, a simple structure can be achieved by employing an electric heater as the heating means.
【0006】[0006]
【発明が解決しようとする課題】このような卓上型蒸気
滅菌装置および乾熱滅菌装置は、比較的簡単な構造で滅
菌作業を行うことができる。しかし、水や空気を加熱す
る際の加熱手段たるヒータとしては、通常、電気ヒータ
が用いられている。このため、滅菌工程中は常にヒータ
へ通電しておかなければならない。このような滅菌工程
は、通常は日中に行われることが多く深夜に滅菌工程を
行う場合よりも電気代がかさんでいるという課題があ
る。一方、電気料金が安い深夜に滅菌装置を稼動しよう
としても、滅菌装置を操作する操作者の問題から、その
案は採用することができない。そこで本発明者等は、上
記課題を解決すべく検討した結果、滅菌工程を日中に行
う場合であっても、そこで使用する電力を予め深夜に使
用して蓄熱しておくことができれば上記課題を解決でき
ることを見い出し、本発明に到達した。Such a tabletop steam sterilizer and dry heat sterilizer can perform a sterilization operation with a relatively simple structure. However, an electric heater is usually used as a heater as a heating means when heating water or air. For this reason, the heater must always be energized during the sterilization process. Such a sterilization process is usually performed during the daytime, and has a problem that the electricity cost is higher than when the sterilization process is performed at midnight. On the other hand, even if an attempt is made to operate the sterilizer at midnight when the electricity rate is low, the idea cannot be adopted due to the problem of the operator operating the sterilizer. Therefore, the present inventors have studied to solve the above-mentioned problems. As a result, even if the sterilization process is performed during the day, if the electric power used there can be used in advance at midnight to store heat, the above-described problems can be solved. Can be solved, and arrived at the present invention.
【0007】すなわち、本発明の目的とするところは、
水や空気の加熱時の電気代の節約を図ることで、装置の
ランニングコストを低減できる蒸気滅菌装置および乾熱
滅菌装置を提供することにあるThat is, the object of the present invention is to
An object of the present invention is to provide a steam sterilizer and a dry heat sterilizer that can reduce the running cost of the apparatus by saving electricity costs when heating water or air.
【0008】[0008]
【課題を解決するための手段】本発明にかかる蒸気滅菌
装置によれば、圧力容器としての缶体内に設けられ、被
滅菌物を収容する滅菌室と、前記缶体内に設けられ、水
が貯留される貯留部と、該貯留部の水を加熱して缶体内
に水蒸気を発生させる加熱手段とを具備する蒸気滅菌装
置において、前記加熱手段は、固体蓄熱材と液体蓄熱材
が充填されて成る蓄熱部と、該蓄熱部を加熱するヒータ
と、蓄熱部内を通過するように配設されると共に蓄熱部
内に供給された水を過熱して過熱水蒸気を吐出する伝熱
管とが設けられている蓄熱槽と、該伝熱管に接続され、
前記蓄熱部で過熱されて生成される過熱水蒸気が前記貯
留部内を通過するように配設されている過熱水蒸気供給
管とを備えることを特徴としている。この構成を採用す
ることによって、滅菌工程を行っていない時間中に予め
蓄熱された蓄熱槽の熱を、水加熱用に用いることができ
る。つまり、蓄熱槽を安価な深夜電力によって深夜に通
電して蓄熱しておけば、昼間滅菌を行う際には加熱用の
電気を利用しなくともよいため、安価に水を加熱するこ
とができ、滅菌工程時の電気代節約によるランニングコ
ストの低減を図ることができる。According to the present invention, there is provided a steam sterilizer according to the present invention, which is provided in a can serving as a pressure vessel and accommodates an object to be sterilized, and is provided in the can and stores water. A steam sterilizer comprising: a storage section to be heated; and heating means for heating water in the storage section to generate water vapor in the can body, wherein the heating means is filled with a solid heat storage material and a liquid heat storage material. Heat storage provided with a heat storage unit, a heater for heating the heat storage unit, and a heat transfer tube that is disposed to pass through the heat storage unit and that overheats water supplied to the heat storage unit and discharges superheated steam. A tank, connected to the heat transfer tube,
And a superheated steam supply pipe arranged so that superheated steam generated by being superheated in the heat storage unit passes through the storage unit. By employing this configuration, the heat of the heat storage tank that has been stored in advance during the time when the sterilization process is not performed can be used for water heating. In other words, if the heat storage tank is energized with inexpensive midnight power at midnight to store heat, it is not necessary to use electricity for heating when performing daytime sterilization, so water can be heated at low cost, The running cost can be reduced by saving electricity costs during the sterilization process.
【0009】また、前記蓄熱部内の固体蓄熱材が、粒径
の異なる固体蓄熱材から成り、前記蓄熱部内には、大粒
径の固体蓄熱材の間隙に小粒径の固体蓄熱材が入り込む
ように形成されていると共に、固体蓄熱材の間隙に液体
蓄熱材が充填されていることを特徴とするので、蓄熱部
内の単位体積あたりの固体蓄熱材と液体蓄熱材との充填
密度を大きく取ることができる。このため、蓄熱部内に
蓄熱される熱量も大とすることができ、なるべく少ない
電力で多くの熱を蓄熱してランニングコスト低減をさら
に図ることができる。Further, the solid heat storage material in the heat storage section is composed of solid heat storage materials having different particle diameters, and a small particle size solid heat storage material enters the gap between the large particle size solid heat storage materials in the heat storage section. And the gap between the solid heat storage materials is filled with the liquid heat storage material, so that the packing density of the solid heat storage material and the liquid heat storage material per unit volume in the heat storage unit is increased. Can be. Therefore, the amount of heat stored in the heat storage unit can be increased, and more heat can be stored with as little power as possible to further reduce running costs.
【0010】さらに、前記蓄熱部内の固体蓄熱材が、マ
グネシア、マグタイト、シリカ及びアルミナから選ばれ
た一種又は二種以上の粒体であることを特徴とすれば、
熱量の蓄熱効果を高めることができ、少ない電力で多く
の熱を蓄熱してランニングコスト低減をさらに図ること
ができる。また、前記蓄熱部内の液体蓄熱材が、硝酸塩
であることとしても熱量の蓄熱効果を高めることがで
き、少ない電力で多くの熱を蓄熱してランニングコスト
低減をさらに図ることができる。[0010] Further, the solid heat storage material in the heat storage unit is characterized in that it is one or more particles selected from magnesia, magnetite, silica and alumina.
The heat storage effect of the amount of heat can be enhanced, and more heat can be stored with less electric power, thereby further reducing running costs. Further, even if the liquid heat storage material in the heat storage section is a nitrate, the heat storage effect of the heat amount can be enhanced, and more heat can be stored with a small amount of electric power to further reduce the running cost.
【0011】本発明にかかる乾熱滅菌装置によれば、被
滅菌物を収容する滅菌室と、加熱室内の空気を加熱する
加熱手段と、該加熱手段によって加熱された加熱室内の
空気を前記滅菌室内へ送り込むと共に、滅菌室内の空気
を加熱室内に送り込む空気循環手段とを具備する乾熱滅
菌装置において、前記加熱手段は、固体蓄熱材と液体蓄
熱材が充填されて成る蓄熱部と、該蓄熱部を加熱するヒ
ータと、蓄熱部内を通過するように配設されると共に蓄
熱部内に供給された水を過熱して過熱水蒸気を吐出する
伝熱管とが設けられている蓄熱槽と、該蓄熱槽に接続さ
れ、蓄熱槽で生成される過熱水蒸気が前記加熱室内を通
過するように配設されている過熱水蒸気供給管とを備え
ることを特徴としている。この構成を採用することによ
って、滅菌工程を行っていない時間中に予め蓄熱された
蓄熱槽の熱を、空気を加熱する加熱用に用いることがで
きる。つまり、蓄熱槽を安価な深夜電力によって深夜に
通電して蓄熱しておけば、昼間滅菌を行う際には加熱用
の電気を利用しなくともよいため、安価に空気を加熱す
ることができ、滅菌工程時の電気代節約によるランニン
グコストの低減を図ることができる。[0011] According to the dry heat sterilization apparatus of the present invention, a sterilization chamber for accommodating an object to be sterilized, heating means for heating air in the heating chamber, and air in the heating chamber heated by the heating means for sterilizing the air in the heating chamber. In a dry heat sterilization apparatus including an air circulation unit that sends air in a sterilization chamber into a heating chamber while sending air into the room, the heating unit includes a heat storage unit filled with a solid heat storage material and a liquid heat storage material; A heat storage tank provided with a heater for heating the heat storage unit, and a heat transfer tube disposed to pass through the heat storage unit and discharging superheated steam by superheating water supplied to the heat storage unit; and And a superheated steam supply pipe arranged so that superheated steam generated in the heat storage tank passes through the heating chamber. By employing this configuration, the heat of the heat storage tank that has been stored in advance during the time when the sterilization process is not performed can be used for heating the air. In other words, if the heat storage tank is energized at midnight with inexpensive midnight power to store heat, it is not necessary to use electricity for heating when performing daytime sterilization, so air can be heated at low cost, The running cost can be reduced by saving electricity costs during the sterilization process.
【0012】[0012]
【発明の実施の形態】以下、本発明の好適な実施の形態
を添付図面に基づいて詳細に説明する。 (卓上型蒸気滅菌装置)まず、図1に基づいて卓上型蒸
気滅菌装置30について説明する。従来の技術でも説明
したように、卓上型蒸気滅菌装置30は、病院等で使用
される医療用器具や実験等で使用される器具類の滅菌を
行う小型の滅菌装置であって、水蒸気を用いて滅菌を行
うものである。かかる卓上型蒸気滅菌装置30は、滅菌
室32を備えた圧力容器である缶体31と、缶体31の
下部に設けられた水を貯留する貯留部34と、貯留部3
4内の水を加熱する加熱手段39とを備えている。加熱
手段39は、貯留部34内に設けられているヒータ36
と、ヒータ36を加熱する蓄熱槽60とを有している。
なお、かかる蓄熱槽60は、滅菌室32が設けられた装
置本体30aとは別体に設けられている。Preferred embodiments of the present invention will be described below in detail with reference to the accompanying drawings. (Tabletop Steam Sterilizer) First, the tabletop steam sterilizer 30 will be described with reference to FIG. As described in the related art, the tabletop steam sterilizer 30 is a small-sized sterilizer that sterilizes medical instruments used in hospitals and the like and instruments used in experiments and the like. Sterilization. The tabletop steam sterilizer 30 includes a can 31 which is a pressure vessel having a sterilization chamber 32, a storage section 34 provided below the can 31 for storing water, and a storage section 3.
And heating means 39 for heating the water in 4. The heating means 39 includes a heater 36 provided in the storage section 34.
And a heat storage tank 60 for heating the heater 36.
The heat storage tank 60 is provided separately from the apparatus main body 30a in which the sterilization chamber 32 is provided.
【0013】蓄熱槽60には水供給槽64が接続されて
おり、水供給槽64内の水を、蓄熱槽60内で過熱(su
perheating)して過熱水蒸気として過熱水蒸気供給管3
6へ供給している。過熱水蒸気供給管36で貯留部34
内の水と熱交換した過熱水蒸気は凝縮して水供給槽64
内へ戻されて、再度過熱されて使用される。A water supply tank 64 is connected to the heat storage tank 60, and the water in the water supply tank 64 is overheated (su) in the heat storage tank 60.
superheated steam supply pipe 3 as superheated steam
6. The storage section 34 is connected to the superheated steam supply pipe 36.
The superheated steam which has exchanged heat with the water in the water is condensed and is
It is returned to the inside and heated again for use.
【0014】缶体31は密閉可能に設けられた圧力容器
であって、被滅菌物(図示せず)を載置することができ
る載置板33が設けられている。缶体31内の載置板3
3よりも下部は、タンク状であって、水が貯留される貯
留部34として形成されている。滅菌工程時には、この
貯留部34内の水は加熱されて水蒸気となり、水蒸気が
缶体31内に充満する。この貯留部34には、補給水が
補給される貯水タンク42から三方制御弁44が途中に
設けられた給水配管40を経由して給水が行われる。三
方制御弁44のもう一方の側は、配管45を介して貯水
タンク42内の消蒸パイプ48に接続されている。な
お、貯水タンク42には排水パイプ兼推移水位計61が
設けられている。The can body 31 is a pressure vessel which can be hermetically sealed, and has a mounting plate 33 on which an object to be sterilized (not shown) can be mounted. Mounting plate 3 in can body 31
The lower part than 3 has a tank shape and is formed as a storage part 34 for storing water. During the sterilization process, the water in the storage section 34 is heated to become steam, and the steam fills the can 31. Water is supplied to the storage section 34 from a water storage tank 42 to which replenishment water is supplied via a water supply pipe 40 in which a three-way control valve 44 is provided in the middle. The other side of the three-way control valve 44 is connected via a pipe 45 to a dewatering pipe 48 in the water storage tank 42. The water storage tank 42 is provided with a drainage pipe and a transition water level gauge 61.
【0015】缶体31の滅菌室32内には大気を吸引す
るように、先端にエアポンプ47が装着されるととも
に、中途部にフィルター49、制御弁50および乾燥ヒ
ータ51が設けられた配管52が連結されている。ま
た、滅菌室32内の排気は、排気管54を通して行われ
る。この排気管54にはトラップ電磁弁55が接続され
ており、排気時の水蒸気は、このトラップ電磁弁55を
介して貯水タンク42内の消蒸パイプ56に導入され
る。また、排気管54は圧力計59、排気圧力スイッチ
57、および貯水タンク42内に設けられた安全弁58
にも連結されている。An air pump 47 is mounted on the distal end of the sterilization chamber 32 of the can body 31 so as to suck air, and a pipe 52 provided with a filter 49, a control valve 50, and a drying heater 51 is provided in the middle. Are linked. Further, the exhaust in the sterilization chamber 32 is performed through an exhaust pipe 54. A trap solenoid valve 55 is connected to the exhaust pipe 54, and water vapor at the time of exhaust is introduced into a dewatering pipe 56 in the water storage tank 42 through the trap solenoid valve 55. The exhaust pipe 54 includes a pressure gauge 59, an exhaust pressure switch 57, and a safety valve 58 provided in the water storage tank 42.
Is also linked.
【0016】貯留部34内に設けられた、水を加熱する
過熱水蒸気供給管36は、蓄熱槽60で生成した過熱水
蒸気を通過させる金属パイプから構成されている。この
金属パイプが貯留部34の水の中に浸されており、過熱
水蒸気の熱が水に伝導して水が加熱される。過熱水蒸気
供給管36は、水との接触面積を増加させるために、コ
イル状に巻回されているかあるいは波形状に形成されて
いるとよい。The superheated steam supply pipe 36 provided in the storage section 34 for heating water is formed of a metal pipe through which the superheated steam generated in the heat storage tank 60 passes. The metal pipe is immersed in the water in the storage section 34, and the heat of the superheated steam is transmitted to the water to heat the water. The superheated steam supply pipe 36 is preferably wound in a coil shape or formed in a corrugated shape in order to increase the contact area with water.
【0017】蓄熱槽60内には、伝熱管62が配設され
ており、伝熱管62の一方の端部には水供給槽64から
の供給パイプ65が接続されている。蓄熱槽60内の伝
熱管62には、ポンプ66によって水供給槽64内の水
が供給される。そして、伝熱管62の他方の端部から
は、蓄熱槽60内の蓄熱材によって水が過熱されて発生
した過熱水蒸気が取り出される。伝熱管62の他方の端
部には貯留部34内へ向かう配管68が接続されてい
る。配管68は貯留部34内の過熱水蒸気供給管36の
一方の端部に接続されており、過熱水蒸気を貯留部34
内へ供給する。A heat transfer tube 62 is provided in the heat storage tank 60, and a supply pipe 65 from a water supply tank 64 is connected to one end of the heat transfer tube 62. The water in the water supply tank 64 is supplied to the heat transfer tube 62 in the heat storage tank 60 by the pump 66. Then, from the other end of the heat transfer tube 62, superheated steam generated by overheating water by the heat storage material in the heat storage tank 60 is extracted. The other end of the heat transfer pipe 62 is connected to a pipe 68 that goes into the storage section 34. The pipe 68 is connected to one end of the superheated steam supply pipe 36 in the storage section 34 to store the superheated steam in the storage section 34.
Supply inside.
【0018】貯留部34内の過熱水蒸気供給管36の他
方の端部には、水供給槽34への配管69が接続されて
いる。この配管69は、貯留部34内で熱交換して凝縮
した過熱水蒸気を水供給槽64へ戻すものである。この
ようにして、水供給槽64内の水は蓄熱槽60や過熱水
蒸気供給管36を循環する。なお、蓄熱槽60で過熱さ
れるべく水供給槽64に蓄えられている水としては、伝
熱管62および過熱水蒸気供給管36のスケールを防止
する観点からマグネシウムやカルシウム等のイオンをイ
オン交換樹脂等で除去した処理水を用いることが望まし
い。At the other end of the superheated steam supply pipe 36 in the storage section 34, a pipe 69 to the water supply tank 34 is connected. The pipe 69 returns superheated steam condensed by heat exchange in the storage section 34 to the water supply tank 64. Thus, the water in the water supply tank 64 circulates through the heat storage tank 60 and the superheated steam supply pipe 36. The water stored in the water supply tank 64 so as to be superheated in the heat storage tank 60 includes ions such as magnesium and calcium in the form of an ion exchange resin from the viewpoint of preventing the scale of the heat transfer pipe 62 and the superheated steam supply pipe 36. It is desirable to use the treated water removed in the above.
【0019】以下、蓄熱槽の構造について説明する。図
1に示す飽和水蒸気発生装置で用いる蓄熱槽60の詳細
な構造を図2に示す。図2に示す蓄熱槽60は、個体蓄
熱材と液体蓄熱材とが混合されて成る蓄熱材が充填され
て成る蓄熱部70内に、蓄熱材を加熱する電気ヒータ7
2とポンプ66によって水が供給される伝熱管62とが
配設されている。更に、この蓄熱部70は、その外周面
が断熱材74によって覆われており、蓄熱部70からの
放熱を防止している。かかる蓄熱部70に充填された蓄
熱材は、粒径の異なる固体蓄熱材と液体蓄熱材とから成
り、大粒径の固体蓄熱材の間隙に小粒径の固体蓄熱材が
入り込むように充填されている。更に、大粒径の固体蓄
熱材と小粒径の固体蓄熱材との間隙には、液体蓄熱材が
充填されている。Hereinafter, the structure of the heat storage tank will be described. FIG. 2 shows a detailed structure of the heat storage tank 60 used in the saturated steam generator shown in FIG. A heat storage tank 60 shown in FIG. 2 includes an electric heater 7 for heating a heat storage material in a heat storage unit 70 filled with a heat storage material formed by mixing a solid heat storage material and a liquid heat storage material.
2 and a heat transfer tube 62 to which water is supplied by a pump 66 are provided. Further, the outer periphery of the heat storage unit 70 is covered with a heat insulating material 74 to prevent heat radiation from the heat storage unit 70. The heat storage material filled in the heat storage unit 70 is composed of a solid heat storage material and a liquid heat storage material having different particle sizes, and is filled such that the small particle size solid heat storage material enters the gap between the large particle size solid heat storage materials. ing. Further, a gap between the solid heat storage material having a large particle diameter and the solid heat storage material having a small particle diameter is filled with a liquid heat storage material.
【0020】かかる蓄熱部における蓄熱材の充填の状態
を図3に示す。図3(a)は、大粒径の固体蓄熱材76
aと小粒径の固体蓄熱材76bとの粒径が二種類の固体
蓄熱材76と液体蓄熱材78とが充填された状態であっ
て、大粒径の固体蓄熱材78aの間隙に小粒径の固体蓄
熱材78bが入り込んで充填され、固体蓄熱材76の間
隙には液体蓄熱材78が充填されている。FIG. 3 shows a state where the heat storage material is filled in the heat storage section. FIG. 3A shows a large-diameter solid heat storage material 76.
a and the solid heat storage material 76b having a small particle diameter are filled with two types of solid heat storage material 76 and a liquid heat storage material 78, and a small particle A solid heat storage material 78b having a diameter enters and is filled, and a gap between the solid heat storage materials 76 is filled with a liquid heat storage material 78.
【0021】また、図3(b)は、粒径が三種類の固体
蓄熱材と液体蓄熱材とが充填された蓄熱部の状態を示
す。この固体蓄熱材は、大粒径の固体蓄熱材76a、小
粒径の固体蓄熱材76b及び固体蓄熱材の中間の粒径で
ある中粒径の固体蓄熱材76cから成り、大粒径の固体
蓄熱材76aの間隙に中粒径の固体蓄熱材76cが入り
込んで充填されていると共に、これら大粒径の固体蓄熱
材76aと中粒径の固体蓄熱材76cとの間隙に小粒径
の固体蓄熱材76bが入り込むように充填されている。
更に、充填された固体蓄熱材76同士の間隙には、液体
蓄熱材78が充填されている。この様に、図3(a)
(b)に示す様に、大粒径の固体蓄熱材76aの間隙
に、それよりも小粒径の固体蓄熱材76b,76cが入
り込むように充填され、且つ固体蓄熱材76の間隙に液
体蓄熱材78が充填されている蓄熱部70では、固体蓄
熱材76と液体蓄熱材78との充填密度を、粒径が一種
類の固体蓄熱材76と液体蓄熱材78との充填密度に比
較して向上でき、蓄熱量及び伝熱管62への熱伝導を向
上できる。FIG. 3B shows a state of the heat storage unit filled with a solid heat storage material and a liquid heat storage material having three kinds of particle diameters. The solid heat storage material is composed of a large-diameter solid heat storage material 76a, a small-diameter solid heat storage material 76b, and a medium-diameter solid heat storage material 76c having an intermediate particle size between the solid heat storage materials. The gap between the heat storage materials 76a is filled with the solid heat storage material 76c having a medium particle size, and the gap between the solid heat storage material 76a having a large particle size and the solid heat storage material 76c having a medium size has a small particle size solid. The heat storage material 76b is filled so as to enter.
Further, a gap between the filled solid heat storage materials 76 is filled with a liquid heat storage material 78. Thus, FIG.
As shown in (b), the gaps between the large-diameter solid heat storage materials 76a are filled so that the smaller-diameter solid heat storage materials 76b and 76c enter the gaps. In the heat storage unit 70 filled with the material 78, the packing density of the solid heat storage material 76 and the liquid heat storage material 78 is compared with the packing density of the solid heat storage material 76 and the liquid heat storage material 78 having one kind of particle diameter. The heat storage amount and the heat conduction to the heat transfer tube 62 can be improved.
【0022】蓄熱槽の具体例について説明する。図3
(a)(b)に示す固体蓄熱材76としては、マグネシ
ア、マグネタイト、シリカ及びアルミナから選ばれた一
種又は二種以上の粒体を好適に用いることができ、液体
蓄熱材78としては、硝酸塩を好適に用いることができ
る。硝酸塩は、室温では固体であるが、142℃以上で
は溶融して液体となる。ここで、固体蓄熱材76として
の粒径7〜10mmの大粒径マグネシア及び粒径1mm
以下の小粒径マグネシアから成るマグネシア1800k
gと、液体蓄熱材78としての硝酸塩370kgとを充
填して蓄熱部70を形成した。蓄熱部70を形成する蓄
熱材の組成は、大粒径マグネシア55%、小粒径マグネ
シア25%、及び硝酸塩20%である。A specific example of the heat storage tank will be described. FIG.
As the solid heat storage material 76 shown in (a) and (b), one or two or more kinds of particles selected from magnesia, magnetite, silica, and alumina can be suitably used. Can be suitably used. Nitrate is solid at room temperature, but melts above 142 ° C. to become a liquid. Here, a large-diameter magnesia having a particle diameter of 7 to 10 mm as the solid heat storage material 76 and a particle diameter of 1 mm
Magnesia 1800k consisting of the following small particle size magnesia
g and 370 kg of nitrate as the liquid heat storage material 78 were filled to form the heat storage section 70. The composition of the heat storage material forming the heat storage unit 70 is 55% of large-diameter magnesia, 25% of small-diameter magnesia, and 20% of nitrate.
【0023】かかる蓄熱部70に、27kWの電気ヒー
タ72と伝熱面積が3.4m2となるように伝熱管62
を挿入し、且つ蓄熱部70を断熱材74で取り囲み蓄熱
槽60を形成した。この断熱材74としては、主成分が
酸化ケイ素と酸化チタンから成る微細多孔構造の厚さ5
0mmの断熱材を用いた。形成した蓄熱槽60は、幅8
30mm、横1200mm、高さ1900mmのサイズ
で且つ重さ3000kgのものであった。The heat storage section 70 is provided with a 27 kW electric heater 72 and a heat transfer tube 62 so that the heat transfer area is 3.4 m 2.
And the heat storage part 70 was surrounded by the heat insulating material 74 to form the heat storage tank 60. The heat insulating material 74 has a thickness of 5 microporous structure whose main component is silicon oxide and titanium oxide.
A heat insulating material of 0 mm was used. The formed heat storage tank 60 has a width of 8
The size was 30 mm, the width was 1200 mm, the height was 1900 mm, and the weight was 3000 kg.
【0024】次いで、形成した蓄熱槽60の電気ヒータ
に深夜10時間ほど通電した後、伝熱管62の出口圧力
が0.5MPaとなる様に、ポンプ66によって伝熱管
62の入口に水を連続供給し、伝熱管62の出口から吐
出される蒸気温度及び蓄熱材温度を調査した。その結果
を図4に示す。図4において、蓄熱材温度の曲線Aは伝
熱管の入口近傍の蓄熱材温度曲線、曲線Bは伝熱管62
の中間近傍の蓄熱材温度曲線、及び曲線Cは伝熱管62
の出口近傍の蓄熱材温度曲線を各々示す。また、発生蒸
気温度とは、伝熱管62の出口から吐出される蒸気温度
である。更に、伝熱管62の出口から吐出される蒸気温
度と伝熱管に供給される水量とから出熱量を計算し、出
熱量の経時変化を図4に併せて示した。Then, after the electric heater of the formed heat storage tank 60 is energized for about 10 hours at midnight, water is continuously supplied to the inlet of the heat transfer tube 62 by the pump 66 so that the outlet pressure of the heat transfer tube 62 becomes 0.5 MPa. Then, the temperature of the steam discharged from the outlet of the heat transfer tube 62 and the temperature of the heat storage material were examined. FIG. 4 shows the results. In FIG. 4, a curve A of the heat storage material temperature is a temperature curve of the heat storage material near the inlet of the heat transfer tube, and a curve B is a heat transfer material 62.
The temperature curve of the heat storage material near the middle of
Respectively shows the heat storage material temperature curves near the outlet of the above. The generated steam temperature is the temperature of the steam discharged from the outlet of the heat transfer tube 62. Further, the amount of heat output was calculated from the steam temperature discharged from the outlet of the heat transfer tube 62 and the amount of water supplied to the heat transfer tube, and the change over time in the amount of heat output is also shown in FIG.
【0025】図4から明らかな様に、蓄熱槽60の蓄熱
材は、電気ヒータ72の加熱によって500℃もの高温
に加熱されており、伝熱管62から吐出される水蒸気も
500℃の過熱水蒸気である。しかも、500℃の過熱
水蒸気を連続して4時間ほど吐出することができる。吐
出される過熱水蒸気の温度が500℃以下に低下して
も、依然として過熱水蒸気を吐出することができ、過熱
水蒸気を連続して8時間以上も吐出することができる。
その結果、出熱量は出熱開始から7時間30分程度まで
安定していた。As is apparent from FIG. 4, the heat storage material in the heat storage tank 60 is heated to a high temperature of 500 ° C. by the heating of the electric heater 72, and the steam discharged from the heat transfer tube 62 is also superheated steam of 500 ° C. is there. In addition, superheated steam at 500 ° C. can be continuously discharged for about 4 hours. Even if the temperature of the discharged superheated steam drops to 500 ° C. or lower, the superheated steam can still be discharged, and the superheated steam can be continuously discharged for 8 hours or more.
As a result, the heat output was stable until about 7 hours 30 minutes from the start of heat output.
【0026】このことは、蓄熱材の温度も、出熱開始と
共に伝熱管62の入口近傍が低下し、出熱開始から2時
間30分経過後に伝熱管62の中央部近傍が低下し始
め、5時間経過後に伝熱管62の出口近傍が低下し始め
ることからも理解される。つまり、蓄熱部70内に蓄熱
された熱の取り出し箇所が、出熱に伴って伝熱管62の
入口近傍の蓄熱材から出口近傍の蓄熱材へと順次移動し
ているため、伝熱管62から吐出される過熱蒸気の温度
及び出熱量を安定化できる。このように、且つ低コスト
な深夜電力によって蓄熱材を加熱できるため、クリーン
で且つ安価な過熱水蒸気を得ることができる。そして、
蒸気滅菌装置の蒸気の発生には、このような安価な深夜
電力を用いて予め蓄熱してあった熱を利用した過熱水蒸
気を電気ヒータ代わりに用いて加熱を行うので、ランニ
ングコストを低減できる。This means that the temperature of the heat storage material also decreases near the inlet of the heat transfer tube 62 with the start of heat output, and begins to decrease near the center of the heat transfer tube 62 two and a half hours after the start of heat output. It is also understood from the fact that the vicinity of the outlet of the heat transfer tube 62 starts to decrease after the elapse of time. In other words, since the location where the heat stored in the heat storage unit 70 is taken out moves sequentially from the heat storage material near the inlet of the heat transfer tube 62 to the heat storage material near the outlet with the heat output, the heat is discharged from the heat transfer tube 62. The temperature of the superheated steam and the amount of heat output can be stabilized. As described above, since the heat storage material can be heated by the low-cost late-night power, clean and inexpensive superheated steam can be obtained. And
In order to generate steam from the steam sterilizer, superheated steam utilizing heat previously stored using such inexpensive late-night power is used for heating instead of an electric heater, so that running costs can be reduced.
【0027】(縦型蒸気滅菌装置)以下、蒸気滅菌装置
の他の実施形態として、縦型蒸気滅菌装置について、図
5に基づいて説明する。縦型蒸気面滅菌装置は、病院で
使用される医療用器具や実験等で使用される器具類の滅
菌を行う小型の滅菌装置であって、水蒸気を用いて滅菌
を行うものである点は、卓上型蒸気滅菌装置と同様であ
る。ここに示す縦型蒸気滅菌装置80は、缶体31の開
口側31aが上方を向くように缶体31が縦型に設置さ
れている点が、上述してきた卓上型蒸気滅菌装置30と
は異なるところである。したがって、本実施形態におい
て上述した実施形態と同一の構成要素については同じ符
号を付し、説明を省略する。(Vertical Steam Sterilizer) Hereinafter, as another embodiment of the steam sterilizer, a vertical steam sterilizer will be described with reference to FIG. The vertical steam surface sterilizer is a small sterilizer that sterilizes medical instruments used in hospitals and instruments used in experiments, etc., and sterilizes using steam. It is the same as a tabletop steam sterilizer. The vertical steam sterilizer 80 shown here is different from the tabletop steam sterilizer 30 described above in that the can body 31 is installed vertically so that the opening side 31a of the can body 31 faces upward. By the way. Therefore, in the present embodiment, the same components as those in the above-described embodiment are denoted by the same reference numerals, and description thereof will be omitted.
【0028】この縦型蒸気滅菌装置80は、滅菌室32
を備えた圧力容器である缶体31と、缶体31の下部に
設けられた、水を貯留する貯留部34と、貯留部34内
の水を加熱する加熱手段39とを有している。貯留部3
4には、補給水が補給される貯水タンクが連結されてい
る場合もあるがが、ここでは省略して図示している。そ
して、貯留部34の排水は配管83に接続された排水バ
ルブ82を経由して行われる。滅菌室32には、フィル
ター86およびドレントラップ88が設けられた配管8
9が、排気バルブ90が設けられた排気管91と連結し
て排気ボトル92へ接続されている。The vertical steam sterilizer 80 is provided in the sterilization chamber 32
A can 31 which is a pressure vessel provided with the above, a storage part 34 provided at a lower portion of the can 31 for storing water, and a heating means 39 for heating the water in the storage part 34. Reservoir 3
4 may be connected to a water storage tank for supplying replenishing water, but is omitted here. And the drainage of the storage part 34 is performed via the drainage valve 82 connected to the pipe 83. In the sterilization chamber 32, a pipe 8 provided with a filter 86 and a drain trap 88 is provided.
9 is connected to an exhaust bottle 92 in connection with an exhaust pipe 91 provided with an exhaust valve 90.
【0029】そして、このような構造をなす縦型蒸気滅
菌装置であっても、貯留部34の水を加熱する際には、
上述してきた実施形態における加熱手段39を採用する
ことができる。すなわち、加熱手段39は、個体蓄熱材
と液体蓄熱材とが混合されて成る蓄熱材が充填されて成
る蓄熱部70内に、蓄熱材を加熱する電気ヒータ72と
ポンプ66によって水が供給される伝熱管62とが配設
されている蓄熱槽60と、蓄熱槽60で生成された過熱
水蒸気を貯留部34内に導入して水を加熱する過熱水蒸
気供給管36とを有している。なお、かかる蓄熱槽60
は、滅菌室32が設けられた装置本体80aとは別体に
設けられている。Even in the vertical steam sterilizer having such a structure, when heating the water in the storage section 34,
The heating means 39 in the embodiment described above can be employed. That is, in the heating means 39, water is supplied by the electric heater 72 and the pump 66 for heating the heat storage material into the heat storage unit 70 filled with the heat storage material formed by mixing the solid heat storage material and the liquid heat storage material. It has a heat storage tank 60 in which a heat transfer tube 62 is provided, and a superheated steam supply pipe 36 for introducing superheated steam generated in the heat storage tank 60 into the storage section 34 to heat the water. In addition, such a heat storage tank 60
Is provided separately from the apparatus main body 80a in which the sterilization chamber 32 is provided.
【0030】過熱水蒸気供給管36内を通過した過熱水
蒸気は、貯留部34内の水と熱交換して凝縮し、水供給
槽34へ戻される。そして水供給槽34内の水は再度蓄
熱槽60内に供給されて過熱水蒸気となる。このような
構成のため、蒸気滅菌装置の蒸気の発生には、安価な深
夜電力を用いて予め蓄熱してあった熱を利用した過熱水
蒸気を用いて加熱を行うので、蒸気滅菌装置のランニン
グコストを低減できる。The superheated steam that has passed through the superheated steam supply pipe 36 exchanges heat with water in the storage section 34, condenses, and returns to the water supply tank 34. Then, the water in the water supply tank 34 is again supplied into the heat storage tank 60 and becomes superheated steam. Due to such a configuration, the steam sterilizer generates steam by using superheated steam that utilizes heat previously stored using inexpensive midnight power, so that the running cost of the steam sterilizer is reduced. Can be reduced.
【0031】(乾熱滅菌装置)次に、本発明の乾熱滅菌
装置について、図6に基づいて説明する。従来の技術で
も説明したように、乾熱滅菌器は、水蒸気を用いずに、
乾燥した熱風によって滅菌を行う装置である。したがっ
て、滅菌効率は蒸気滅菌装置よりも悪く、蒸気滅菌装置
と比較して滅菌終了まで時間がかかるが、被滅菌物に水
分を付着させたくない場合などにはよく用いられる。(Dry Heat Sterilizer) Next, the dry heat sterilizer of the present invention will be described with reference to FIG. As described in the prior art, a dry heat sterilizer uses no steam,
This is a device that sterilizes with hot dry air. Therefore, the sterilization efficiency is lower than that of the steam sterilizer, and it takes more time to complete the sterilization than the steam sterilizer. However, it is often used when it is not desired to attach moisture to the object to be sterilized.
【0032】ここに示す乾熱滅菌器100は、被滅菌物
(図示せず)を収容するための滅菌室102と、滅菌室
102に隣接し、滅菌室102と二カ所の連結部10
3,104でつながって設けられた加熱室106とを備
えている。加熱には、上述した蒸気滅菌装置で説明した
ものと同様の加熱手段39が用いられる。加熱手段39
は、加熱室106内に設けられた過熱水蒸気供給管11
0と、過熱水蒸気供給管110に接続された蓄熱槽60
とを有している。ここで、蓄熱槽60は、上述してきた
実施形態のものと全く同一構造のものであって、供給さ
れた水を過熱して過熱水蒸気を吐出するものである。な
お、かかる蓄熱槽60は、滅菌室102が設けられた装
置本体100aとは別体に設けられている。The dry heat sterilizer 100 shown here has a sterilization chamber 102 for accommodating an object to be sterilized (not shown), and a connecting portion 10 adjacent to and adjacent to the sterilization chamber 102.
And a heating chamber 106 connected to the heating chambers 3 and 104. For heating, the same heating means 39 as that described in the above-described steam sterilizer is used. Heating means 39
Is a superheated steam supply pipe 11 provided in the heating chamber 106.
0 and the heat storage tank 60 connected to the superheated steam supply pipe 110
And Here, the heat storage tank 60 has exactly the same structure as that of the above-described embodiment, and superheats supplied water to discharge superheated steam. The heat storage tank 60 is provided separately from the apparatus main body 100a in which the sterilization chamber 102 is provided.
【0033】連結部103,104のうちのどちらか一
方には、滅菌室102と加熱室106との間で空気を循
環させる循環手段が設けられている。本実施形態では、
連結部104に、送風機108が設けられている。送風
機108は、滅菌室102内の空気を加熱室106内に
送り込んでいる。加熱室106内に送り込まれた空気
は、加熱されて加熱室106上方にある連結部103か
ら滅菌室102へ移動する。A circulating means for circulating air between the sterilizing chamber 102 and the heating chamber 106 is provided in one of the connecting portions 103 and 104. In this embodiment,
A blower 108 is provided in the connecting portion 104. The blower 108 sends the air in the sterilization chamber 102 into the heating chamber 106. The air sent into the heating chamber 106 is heated and moves from the connecting portion 103 above the heating chamber 106 to the sterilization chamber 102.
【0034】過熱水蒸気供給管110は、蓄熱槽60で
発生した過熱水蒸気を通過させる金属パイプから構成さ
れている。この金属パイプが加熱室106内を上下方向
に貫通して配設されている。過熱水蒸気供給管110の
両端側は蓄熱槽からの配管68,69に接続されてい
る。そして過熱水蒸気供給管110内を通過する過熱水
蒸気の熱が加熱室106内の空気に伝導して空気が加熱
されるのである。なお、この過熱水蒸気供給管110
は、空気との接触面積を増加させるために、コイル状に
巻回されているかあるいは波形状に形成されているとよ
い。The superheated steam supply pipe 110 is formed of a metal pipe through which the superheated steam generated in the heat storage tank 60 passes. The metal pipe extends vertically through the heating chamber 106. Both ends of the superheated steam supply pipe 110 are connected to pipes 68 and 69 from the heat storage tank. Then, the heat of the superheated steam passing through the inside of the superheated steam supply pipe 110 is conducted to the air in the heating chamber 106 to heat the air. Note that this superheated steam supply pipe 110
In order to increase the contact area with air, it is preferable that the is wound in a coil shape or formed in a wave shape.
【0035】乾熱滅菌装置によれば、200℃の熱風を
約6時間滅菌室102へ送り込んで滅菌を行う必要があ
るが、蓄熱槽60を用いて空気の加熱を行うことによ
り、予め蓄熱してあった熱を用いて加熱できる。すなわ
ち、滅菌工程時にはヒータ用の電源を用いなくともよ
く、安価な深夜電力で蓄熱した熱を利用した過熱水蒸気
を用いて加熱を行うので、ランニングコストを低減でき
る。According to the dry heat sterilizer, it is necessary to send hot air at 200 ° C. into the sterilization chamber 102 for about 6 hours for sterilization. However, by using the heat storage tank 60 to heat the air, heat is stored in advance. It can be heated using the heat. In other words, a power source for the heater need not be used during the sterilization process, and heating is performed using superheated steam utilizing heat stored with inexpensive midnight power, so that running costs can be reduced.
【0036】なお、上述した蒸気滅菌装置および乾熱滅
菌装置においては、各1台の蓄熱槽60につき1個の過
熱水蒸気供給管36が接続されているものであった。し
かしながら、1台の蓄熱槽60に複数台の過熱水蒸気供
給管36を接続しても好適である。すなわち、上述した
ような本蓄熱槽60は、連続8時間程度は過熱水蒸気を
供給可能であるので、実際の水または空気の加熱時間を
少しずらすだけで複数台の滅菌装置の滅菌工程を1つの
蓄熱槽で行えるのである。このようにすれば、深夜電力
を利用した蓄熱槽で電気代を節約し、さらに複数台分の
電気代を節約でき、さらにランニングコストの低減を図
ることができる。In the steam sterilizer and the dry heat sterilizer described above, one superheated steam supply pipe 36 is connected to each heat storage tank 60. However, it is also preferable to connect a plurality of superheated steam supply pipes 36 to one heat storage tank 60. That is, since the above-described heat storage tank 60 can supply superheated steam for about eight continuous hours, the sterilization process of a plurality of sterilizers can be performed by only slightly shifting the actual heating time of water or air. It can be done in a heat storage tank. In this way, the electricity bill can be saved in the heat storage tank using the late-night power, the electricity bill for a plurality of cars can be saved, and the running cost can be further reduced.
【0037】以上、本発明につき好適な実施例を挙げて
種々説明したが、本発明はこの実施例に限定されるもの
ではなく、発明の精神を逸脱しない範囲内で多くの改変
を施し得るのはもちろんである。Although the present invention has been described in detail with reference to the preferred embodiments, the present invention is not limited to these embodiments, and many modifications can be made without departing from the spirit of the invention. Of course.
【0038】[0038]
【発明の効果】本発明に係る蒸気滅菌装置によれば、圧
力容器としての缶体内に設けられ、被滅菌物を収容する
滅菌室と、缶体内に設けられ、水が貯留される貯留部
と、貯留部の水を加熱して缶体内に水蒸気を発生させる
加熱手段とを具備する蒸気滅菌装置において、加熱手段
は、固体蓄熱材と液体蓄熱材が充填されて成る蓄熱部
と、蓄熱部を加熱するヒータと、蓄熱部内を通過するよ
うに配設されると共に蓄熱部内に供給された水を過熱し
て過熱水蒸気を吐出する伝熱管とが設けられている蓄熱
槽と、伝熱管に接続され、蓄熱部で過熱されて生成され
る過熱水蒸気が貯留部内を通過するように配設されてい
る過熱水蒸気供給管とを備える。このため、滅菌工程を
行っていない時間、すなわち電気料金が安い深夜に予め
蓄熱槽に蓄熱しておき、それを水加熱用に用いることが
できる。つまり、昼間滅菌を行う際には加熱用の電気を
利用しなくとも蓄熱槽からの熱を利用できるので、安価
に水を加熱することができ、滅菌工程時の電気代節約に
よるランニングコストの低減を図ることができる。According to the steam sterilization apparatus of the present invention, a sterilization chamber provided in a can as a pressure vessel and containing an object to be sterilized, and a storage section provided in the can and storing water. In a steam sterilizer having heating means for heating water in a storage part to generate water vapor in a can body, the heating means includes a heat storage part filled with a solid heat storage material and a liquid heat storage material, and a heat storage part. A heat storage tank provided with a heater for heating, and a heat transfer tube disposed to pass through the heat storage unit and discharging superheated steam by superheating water supplied to the heat storage unit, and connected to the heat transfer tube. And a superheated steam supply pipe disposed so that superheated steam generated by being superheated in the heat storage unit passes through the storage unit. Therefore, heat can be stored in the heat storage tank in advance during the time when the sterilization step is not performed, that is, at midnight when the electricity rate is low, and the stored heat can be used for water heating. In other words, during daytime sterilization, heat from the heat storage tank can be used without using electricity for heating, so water can be heated at low cost, and running costs can be reduced by saving electricity costs during the sterilization process. Can be achieved.
【0039】本発明に係る乾熱滅菌装置によれば、被滅
菌物を収容する滅菌室と、加熱室内の空気を加熱する加
熱手段と、加熱手段によって加熱された加熱室内の空気
を滅菌室内へ送り込むと共に、滅菌室内の空気を加熱室
内に送り込む空気循環手段とを具備する乾熱滅菌装置に
おいて、加熱手段は、固体蓄熱材と液体蓄熱材が充填さ
れて成る蓄熱部と、蓄熱部を加熱するヒータと、蓄熱部
内を通過するように配設されると共に蓄熱部内に供給さ
れた水を過熱して過熱水蒸気を吐出する伝熱管とが設け
られている蓄熱槽と、伝熱管に接続され、蓄熱部で過熱
されて生成される過熱水蒸気が加熱室内を通過するよう
に配設されている過熱水蒸気供給管とを備える。このた
め、滅菌工程を行っていない時間、すなわち電気料金が
安い深夜に予め蓄熱槽に蓄熱しておき、それを空気加熱
用に用いることができる。つまり、昼間滅菌を行う際に
は加熱用の電気を利用しなくとも蓄熱槽からの熱を利用
できるので、安価に水を加熱することができ、滅菌工程
時の電気代節約によるランニングコストの低減を図るこ
とができる。According to the dry heat sterilization apparatus of the present invention, the sterilization chamber accommodating the object to be sterilized, the heating means for heating the air in the heating chamber, and the air in the heating chamber heated by the heating means are introduced into the sterilization chamber. In a dry heat sterilization apparatus including an air circulation unit that sends air in a sterilization chamber into a heating chamber while feeding air, the heating unit heats a heat storage unit filled with a solid heat storage material and a liquid heat storage material, and a heat storage unit. A heat storage tank provided with a heater and a heat transfer tube that is disposed to pass through the heat storage unit and that discharges superheated steam by superheating water supplied to the heat storage unit; A superheated steam supply pipe disposed so that superheated steam generated by being superheated in the section passes through the heating chamber. Therefore, heat can be stored in the heat storage tank in advance during the time when the sterilization process is not performed, that is, at midnight when the electricity rate is low, and the stored heat can be used for air heating. In other words, during daytime sterilization, heat from the heat storage tank can be used without using electricity for heating, so water can be heated at low cost, and running costs can be reduced by saving electricity costs during the sterilization process. Can be achieved.
【図1】本発明に係る蒸気滅菌装置のうちの一例として
の卓上型蒸気滅菌装置の構成を示す配管系統図である。FIG. 1 is a piping diagram showing a configuration of a tabletop steam sterilizer as an example of a steam sterilizer according to the present invention.
【図2】蓄熱槽の構造を示す断面図である。FIG. 2 is a sectional view showing the structure of a heat storage tank.
【図3】蓄熱槽の蓄熱部における蓄熱材の充填の様子を
示す説明図である。FIG. 3 is an explanatory diagram showing a state of filling a heat storage material in a heat storage unit of a heat storage tank.
【図4】蓄熱槽の出力特性の経時変化を示すグラフであ
る。FIG. 4 is a graph showing a change over time in output characteristics of a heat storage tank.
【図5】本発明に係る蒸気滅菌装置のうちの一例として
の縦型蒸気滅菌装置の構成を示す配管系統図である。FIG. 5 is a piping diagram showing the configuration of a vertical steam sterilizer as an example of the steam sterilizer according to the present invention.
【図6】本発明に係る乾熱滅菌装置の構成を示す配管系
統図である。FIG. 6 is a piping diagram showing a configuration of a dry heat sterilizer according to the present invention.
【図7】従来の蒸気滅菌装置の構成を示す配管系統図で
ある。FIG. 7 is a piping diagram showing a configuration of a conventional steam sterilizer.
【図8】従来の乾熱滅菌装置の構成を示す配管系統図で
ある。FIG. 8 is a piping diagram showing the configuration of a conventional dry heat sterilizer.
30 卓上型蒸気滅菌装置 31 缶体 32 滅菌室 33 載置板 34 貯留部 36 過熱水蒸気供給管 39 加熱手段 40,45,52,68,69,83,89 配管 42 貯水タンク 44 三方制御弁 47 エアポンプ 48 消蒸パイプ 49,86 フィルター 50 制御弁 51 乾燥ヒータ 54 排気管 55 トラップ電磁弁 56 消蒸パイプ 60 蓄熱槽 62 伝熱管 64 水供給槽 65 供給パイプ 66 ポンプ 70 蓄熱部 72 電気ヒータ 74 断熱材 76 固体蓄熱材 78 液体蓄熱材 80 縦型蒸気滅菌装置 82 排水バルブ 88 ドレントラップ 90 排気バルブ 91 排気管 92 排気ボトル 100 乾熱滅菌装置 102 滅菌室 103,104 連結部 106 加熱室 108 送風機 110 過熱水蒸気供給管 REFERENCE SIGNS LIST 30 desktop steam sterilizer 31 can body 32 sterilization chamber 33 mounting plate 34 storage section 36 superheated steam supply pipe 39 heating means 40, 45, 52, 68, 69, 83, 89 pipe 42 water storage tank 44 three-way control valve 47 air pump 48 Dehumidifying pipe 49, 86 Filter 50 Control valve 51 Drying heater 54 Exhaust pipe 55 Trap solenoid valve 56 Dehumidifying pipe 60 Heat storage tank 62 Heat transfer pipe 64 Water supply tank 65 Supply pipe 66 Pump 70 Heat storage section 72 Electric heater 74 Insulation material 76 Solid heat storage material 78 Liquid heat storage material 80 Vertical steam sterilizer 82 Drain valve 88 Drain trap 90 Exhaust valve 91 Exhaust pipe 92 Exhaust bottle 100 Dry heat sterilizer 102 Sterilization chamber 103, 104 Connecting section 106 Heating chamber 108 Blower 110 Superheated steam supply tube
Claims (8)
滅菌物を収容する滅菌室と、 前記缶体内に設けられ、水が貯留される貯留部と、 該貯留部の水を加熱して缶体内に水蒸気を発生させる加
熱手段とを具備する蒸気滅菌装置において、 前記加熱手段は、 固体蓄熱材と液体蓄熱材が充填されて成る蓄熱部と、該
蓄熱部を加熱するヒータと、蓄熱部内を通過するように
配設されると共に蓄熱部内に供給された水を過熱して過
熱水蒸気を吐出する伝熱管とが設けられている蓄熱槽
と、 該伝熱管に接続され、前記蓄熱部で過熱されて生成され
る過熱水蒸気が前記貯留部内を通過するように配設され
ている過熱水蒸気供給管とを備えることを特徴とする蒸
気滅菌装置。1. A sterilization chamber provided in a can as a pressure vessel and containing an object to be sterilized; a storage provided in the can and storing water; and heating the water in the storage by heating the water in the storage. In a steam sterilizer having a heating means for generating water vapor in a can body, the heating means comprises: a heat storage unit filled with a solid heat storage material and a liquid heat storage material; a heater for heating the heat storage unit; A heat storage tank provided with a heat transfer tube that is disposed so as to pass through and heats the water supplied into the heat storage unit and discharges superheated steam, and is connected to the heat transfer tube and is heated by the heat storage unit. And a superheated steam supply pipe disposed so that the superheated steam generated by passing through the storage section is provided.
なる固体蓄熱材から成り、前記蓄熱部内には、大粒径の
固体蓄熱材の間隙に小粒径の固体蓄熱材が入り込むよう
に形成されていると共に、固体蓄熱材の間隙に液体蓄熱
材が充填されていることを特徴とする請求項1記載の蒸
気滅菌装置。2. The solid heat storage material in the heat storage section is made of solid heat storage materials having different particle diameters, and the small-diameter solid heat storage material enters the gaps between the large-diameter solid heat storage materials in the heat storage section. The steam sterilizer according to claim 1, wherein the liquid heat storage material is filled in a gap between the solid heat storage materials.
ア、マグタイト、シリカ及びアルミナから選ばれた一種
又は二種以上の粒体であることを特徴とする請求項1ま
たは2記載の蒸気滅菌装置。3. The steam sterilizer according to claim 1, wherein the solid heat storage material in the heat storage unit is one or more particles selected from magnesia, magnetite, silica, and alumina. .
あることを特徴とする請求項1,2または3記載の蒸気
滅菌装置。4. The steam sterilizer according to claim 1, wherein the liquid heat storage material in the heat storage unit is a nitrate.
菌室内へ送り込むと共に、滅菌室内の空気を加熱室内に
送り込む空気循環手段とを具備する乾熱滅菌装置におい
て、 前記加熱手段は、 固体蓄熱材と液体蓄熱材が充填されて成る蓄熱部と、該
蓄熱部を加熱するヒータと、蓄熱部内を通過するように
配設されると共に蓄熱部内に供給された水を過熱して過
熱水蒸気を吐出する伝熱管とが設けられている蓄熱槽
と、 該伝熱管に接続され、前記蓄熱部で過熱されて生成され
る過熱水蒸気が前記加熱室内を通過するように配設され
ている過熱水蒸気供給管とを備えることを特徴とする乾
熱滅菌装置。5. A sterilization chamber for accommodating an object to be sterilized, heating means for heating air in the heating chamber, air in the heating chamber heated by the heating means is sent into the sterilization chamber, and air in the sterilization chamber is removed. In a dry heat sterilization apparatus including an air circulation unit that feeds into a heating chamber, the heating unit includes: a heat storage unit that is filled with a solid heat storage material and a liquid heat storage material; a heater that heats the heat storage unit; A heat storage tank provided with a heat transfer tube that is disposed so as to pass therethrough and discharges superheated steam by superheating water supplied to the heat storage unit; and a heat storage tank connected to the heat transfer tube and overheated by the heat storage unit. And a superheated steam supply pipe disposed so that the superheated steam generated in the heating chamber passes through the heating chamber.
なる固体蓄熱材から成り、前記蓄熱部内には、大粒径の
固体蓄熱材の間隙に小粒径の固体蓄熱材が入り込むよう
に形成されていると共に、固体蓄熱材の間隙に液体蓄熱
材が充填されていることを特徴とする請求項5記載の乾
熱滅菌装置。6. The solid heat storage material in the heat storage section is made of solid heat storage materials having different particle diameters, and the small heat storage material having a small particle diameter enters a gap between the large particle diameter solid heat storage materials in the heat storage section. 6. The dry heat sterilizer according to claim 5, wherein a liquid heat storage material is filled in a gap between the solid heat storage materials.
ア、マグタイト、シリカ及びアルミナから選ばれた一種
又は二種以上の粒体であることを特徴とする請求項5ま
たは6記載の乾熱滅菌装置。7. The dry heat sterilization according to claim 5, wherein the solid heat storage material in the heat storage unit is one or more particles selected from magnesia, magnetite, silica, and alumina. apparatus.
あることを特徴とする請求項5,6または7記載の乾熱
滅菌装置。8. The dry heat sterilizer according to claim 5, wherein the liquid heat storage material in the heat storage unit is a nitrate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000241129A JP2002052070A (en) | 2000-08-09 | 2000-08-09 | Steam sterilizer and hot-air sterilizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000241129A JP2002052070A (en) | 2000-08-09 | 2000-08-09 | Steam sterilizer and hot-air sterilizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2002052070A true JP2002052070A (en) | 2002-02-19 |
Family
ID=18732363
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000241129A Pending JP2002052070A (en) | 2000-08-09 | 2000-08-09 | Steam sterilizer and hot-air sterilizer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2002052070A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011156225A (en) * | 2010-02-02 | 2011-08-18 | Hiruson Dekku Kk | High pressure steam sterilizer |
| US8168132B2 (en) | 2006-07-07 | 2012-05-01 | Scican Ltd. | Apparatus and method for drying instruments using superheated steam |
| CN108680232A (en) * | 2018-07-16 | 2018-10-19 | 黄河水利委员会山东水文水资源局 | A kind of multifunction electronic water gauge |
| JP2022055182A (en) * | 2020-09-28 | 2022-04-07 | 株式会社ナカニシ | Sterilization unit |
-
2000
- 2000-08-09 JP JP2000241129A patent/JP2002052070A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8168132B2 (en) | 2006-07-07 | 2012-05-01 | Scican Ltd. | Apparatus and method for drying instruments using superheated steam |
| JP2011156225A (en) * | 2010-02-02 | 2011-08-18 | Hiruson Dekku Kk | High pressure steam sterilizer |
| CN108680232A (en) * | 2018-07-16 | 2018-10-19 | 黄河水利委员会山东水文水资源局 | A kind of multifunction electronic water gauge |
| JP2022055182A (en) * | 2020-09-28 | 2022-04-07 | 株式会社ナカニシ | Sterilization unit |
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