JPS6311680Y2 - - Google Patents
Info
- Publication number
- JPS6311680Y2 JPS6311680Y2 JP14341681U JP14341681U JPS6311680Y2 JP S6311680 Y2 JPS6311680 Y2 JP S6311680Y2 JP 14341681 U JP14341681 U JP 14341681U JP 14341681 U JP14341681 U JP 14341681U JP S6311680 Y2 JPS6311680 Y2 JP S6311680Y2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- water
- microwave
- container
- carbon dioxide
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 29
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 26
- 238000006297 dehydration reaction Methods 0.000 claims description 18
- 230000018044 dehydration Effects 0.000 claims description 17
- 239000001569 carbon dioxide Substances 0.000 claims description 13
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 13
- 238000001816 cooling Methods 0.000 claims description 11
- 238000001179 sorption measurement Methods 0.000 claims description 10
- 241001465754 Metazoa Species 0.000 claims description 9
- YZCKVEUIGOORGS-NJFSPNSNSA-N Tritium Chemical compound [3H] YZCKVEUIGOORGS-NJFSPNSNSA-N 0.000 claims description 6
- 238000007254 oxidation reaction Methods 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- 229910052722 tritium Inorganic materials 0.000 claims description 6
- 238000010521 absorption reaction Methods 0.000 claims description 5
- 230000005540 biological transmission Effects 0.000 claims description 5
- OKTJSMMVPCPJKN-NJFSPNSNSA-N Carbon-14 Chemical compound [14C] OKTJSMMVPCPJKN-NJFSPNSNSA-N 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 4
- 230000003647 oxidation Effects 0.000 claims description 4
- 230000001590 oxidative effect Effects 0.000 claims description 4
- 108010004350 tyrosine-rich amelogenin polypeptide Proteins 0.000 claims description 3
- XLYOFNOQVPJJNP-PWCQTSIFSA-N Tritiated water Chemical compound [3H]O[3H] XLYOFNOQVPJJNP-PWCQTSIFSA-N 0.000 claims 1
- 239000010828 animal waste Substances 0.000 description 22
- 239000007789 gas Substances 0.000 description 19
- 230000002285 radioactive effect Effects 0.000 description 9
- 239000012857 radioactive material Substances 0.000 description 8
- 239000002699 waste material Substances 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 235000019645 odor Nutrition 0.000 description 7
- 239000000941 radioactive substance Substances 0.000 description 7
- 238000001035 drying Methods 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 5
- 239000005416 organic matter Substances 0.000 description 5
- 241000251468 Actinopterygii Species 0.000 description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 4
- 238000000354 decomposition reaction Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 239000010868 animal carcass Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 238000007602 hot air drying Methods 0.000 description 2
- 230000008520 organization Effects 0.000 description 2
- 239000003755 preservative agent Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 241001474374 Blennius Species 0.000 description 1
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 1
- 239000005751 Copper oxide Substances 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 238000010171 animal model Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000009933 burial Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000010849 combustible waste Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229910000431 copper oxide Inorganic materials 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005672 electromagnetic field Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- -1 paper or cloth Chemical compound 0.000 description 1
- 235000015277 pork Nutrition 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000002901 radioactive waste Substances 0.000 description 1
- 235000015170 shellfish Nutrition 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- HUAUNKAZQWMVFY-UHFFFAOYSA-M sodium;oxocalcium;hydroxide Chemical compound [OH-].[Na+].[Ca]=O HUAUNKAZQWMVFY-UHFFFAOYSA-M 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001256 steam distillation Methods 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Processing Of Solid Wastes (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Description
本考案は脱水装置に関し、特に放射性物質で汚
染された動物廃棄物或は汚染の疑いのある動物死
体の如き放射性汚染動物の脱水装置に関する。
従来、物体を乾燥させるためには一般に熱風乾
燥法が広く採用されており、特に比較的高速度で
乾燥を行う必要のある場合には他の、例えば赤外
線法等に比較して極めて有利なものであると認め
られている。
周知のように熱風等による乾燥では、乾燥され
るべき、即ち脱水されるべき物体の表面のみに熱
エネルギーが与えられるために、物体の表面積に
より乾燥時間が左右され従つて表面積が小さい場
合には乾燥に長い時間が必要となる。また表面に
与えられる熱エネルギーを高くして時間短縮をは
かる場合には、物体、特に有機物である物体につ
いてはその表面から分解ガスが多量に発生し、臭
気の問題が新たに生じると共に物体そのものを損
傷する可能性が高くなる。
例えば現在極めて多数の実験動物が種々の目的
のために使用されており、使用後の動物廃棄物は
焼却あるいは地中埋没等によつて処理されるのが
普通である。しかしながら、この動物が放射性同
位体の投与実験に供されたものである場合には上
記のごとき通常の処理を行うことが出来ない。周
知のように放射性動物廃棄物の最終的な処理の困
難性は廃棄物の保存方法に最大の原因がある。す
なわち動物廃棄物は腐敗し易いから放射性廃棄物
を特定の処理機関に引渡すまでその防止をはから
ねばならずその手段としてホルマリン、その他の
防腐剤を用いて廃棄物の保存を行うのが普通であ
る。しかしながらこの方法では特定機関における
その後の処理、例えば焼却処理等が著しく困難と
なる。
従つて例えば動物廃棄物を従来のごとくに防腐
剤を用いることなくしかも焼却し易い形で保存出
来るようにすれば上記のごとき問題は生じない。
このための方法として考えられるのは動物廃棄物
の乾燥であるが、前述のように例えば熱風乾燥等
では時間の問題および分解ガスの問題があり、こ
れを用いることは極めて困難である。また動物廃
棄物を乾燥のため脱水処理すると異臭が発生し、
またこの廃棄物が放射性物質で汚染されている場
合に廃棄物から発生する水蒸気やガスにはこれら
物質が含まれている恐れがある。
本考案の目的は、放射性汚染動物を焼却し易い
形で保存できるように脱水処理すると共に異臭や
放射性物質の系外散逸を防止するようにした脱水
装置を提供することである。
以下図面に基づいて放射性物質で汚染された動
物廃棄物(以下放射性動物廃棄物又は動物廃棄物
という)の脱水に適用した場合の本考案の実施例
を説明する。
本考案の装置を概略的に部分断面で示す図面に
於いて、本装置は点線により区分出来る脱水部分
Aと、処理対称が放射性物質を含む場合の安全部
分Bから構成されている。
脱水部分Aはマイクロ波発生器20、このマイ
クロ波発生器により発生されるマイクロ波電磁界
を限定する収容室つまりマイクロ波照射室30、
この収容室30に空気を供給するための流量調節
装置14、収容室30から空気を連続的に取り出
すための排出口18、排出口18からの気体を冷
却するための冷却装置22、冷却装置22により
冷却されて液化した液体を捕集するための捕集容
器24、および収容室30での脱水完了後のいわ
ゆる空びき状態に検知するための装置50から成
つている。この装置50は後述するように脱水プ
ロセスのモニターとしても使用出来る。
安全部分Bは、脱水されるべき物体が放射性有
機物を含む場合に、捕集容器24に存在する可能
性のある微量の低分子の放射性気体を捕獲してそ
れが系外に散逸するのを防止するためのものであ
つて、捕集容器24から気体を引き出し、それを
酸化するための例えば電気炉のような加熱装置2
6、この加熱装置26に接続し、ソーダ石灰、シ
リカゲル等の吸湿剤29および活性炭等の吸着剤
41を充填してなる吸着装置28、トリチウム水
を捕集するためのコールドトラツプ43、14CO2
を吸収するための炭酸ガス吸収装置44および吸
引ポンプ45から成つている。コールドトラツプ
43と炭酸ガス吸収装置44については任意でよ
いが例えば特開昭51−119286号(特願昭50−
43623号)に開示されているものを用いれば効率
よく目的をはたすことが出来る。
図面に示す装置を放射性動物廃棄物を対象とし
て詳細に説明すると、まず動物廃棄物40を直接
または紙あるいは布等の水蒸気の通過を妨げない
もの42で包み、これを収容器30にあるいは第
2図に示すようにマイクロ波に対して透明なつま
り透過性のある例えばプラスチツクまたは耐熱ガ
ラスのような材料からなり且つ空気供給口16′
および排出口18′を備えたマイクロ波透過容器
30′に封入したものを収容室30に配置する。
収容室30または容器30′には空気が供給され
る。空気は適当な空気源からパイプ12を通じて
供給つまり強制的に供給されるようになつてお
り、この流路内に設けられた適当な流量調節装置
14によりその流量を調節する。この調節は収容
室30または容器30′内の動物廃棄物より取り
出された水を効率よく排出口18を通じて引き出
すために必要である。
例えばマグネトロンからなるマイクロ波発生器
20はこのような状態において作動されて動物廃
棄物40をマイクロ波電磁界内に置く。これによ
り動物廃棄物40の水分子が選択的に励起されて
それより水蒸気が発生する。この水蒸気は供給さ
れている空気により運ばれて速かに冷却装置22
に導かれて液化され、捕集装置24内に累積す
る。この際発生した水蒸気をマイクロ波の系外に
迅速に取り出すことが効果的な脱水には必要であ
り、このために前述の流量調節を行う必要があ
る。
また、冷却装置22には動物体内に含まれる低
分子化合物、例えば脂質の一部等が水蒸気蒸留に
より流入することがある。これらも捕集装置24
に同時に集められる。
動物廃棄物をこのように処理する場合にしばし
ば問題となるのは異臭であり、またこの廃棄物が
放射性物質を含む場合には安全上これらの物質の
系外散逸を防ぐための充分な対策が必要である。
このため本考案においては、捕集装置24から
パイプ25を通じて気体分を取り出し、これを酸
化銅等の酸化触媒を充填した加熱装置26に導
き、ここで完全な酸化反応を行わせる。酸化後に
得られる水、炭酸ガスその他は前述の吸着装置2
8により吸着除去される。
吸着装置28を用いることにより放射性物質特
に3H、14Cがあつてもこれらは殆んど大部分系内
に止まることになる。更に安全性を高めるため
に、吸着装置28に接続するコールドトラツプ4
3と炭酸ガス吸収装置44からなる放射性物質を
捕捉して取り除く装置を用いて各々水および炭酸
ガスの形で存在しうるトリチウムと炭素14の系
外散逸を防止している。
前述のように本考案においてはマイクロ波を用
い水分子に選択的にエネルギーを与えることによ
り水蒸気として水を取り出すために、最高到達温
度は100℃前後であり、このような温度では有機
物表面の分解を伴うことはなく分解ガスの発生は
殆んどない。さらに脱水反応のみが極めて効率良
く進行し、しかも試料固体の形状には殆んど変化
は生じない。
また前述のように比較的低分子の有機物が捕集
装置24に集められることがあり、またこの有機
物中に放射性物質が含まれることもありうる。そ
のような場合にはエーテル、ヘキサン等による抽
出により溶媒を除き、有機物を油状または固体と
して単離するようにし、この形で廃棄物としても
よい。あるいは水溶液をそのまま活性炭層を通す
ことにより吸着除去を行い、この活性炭と共に可
燃廃棄物として処理してもよい。また吸着装置2
8における吸着剤等は固体廃棄物として処理出来
る。
通常マイクロ波加熱では処理試料に水が存在し
ない場合あるいは試料の脱水が完了した場合、マ
イクロ波エネルギーが吸収されなくなり、それが
室内に蓄積してついには放電現象を生じさせる可
能性があり、マグネトロン自体を損傷させる危険
がある。このために図示の装置においてはマイク
ロ波に対して透明なパイプを用いてそれに水を流
しておくことにより上記の問題を解決する。
図示の装置においては、これはU字形のパイプ
50からなり、これへの水の供給は冷却装置22
で用いられた水を直接に送ることにより行つてい
る。このような構成を用いた場合、脱水完了によ
りパイプ50を流れる水の温度が急上昇する。従
つてこの温度上昇を検知することにより脱水の過
程をモニターすることが出来る。パイプ50の水
の温度の測定および表示は当業者には明らかであ
るので詳述しない。
本装置を放射性動物廃棄物の脱水に用いる場合
の放射能の系外散逸防止はほゞ完全である。しか
しながら実施例においては、本装置自体を一つの
減圧状態の下に維持することにより、系外散逸の
可能性を完全になくしている。すなわち空気供給
口16、排出口46および水の供給排出系を除き
完全に密閉されたハウジング10内に本装置を収
納し、このハウジングを排気口52により排気し
て減圧状態に維持している。
例 1
14C−グルコースで汚染された動物組織(豚肉)
180gを周波数2500MHz出力450Wのマイクロ波照
射装置を取り付けた第1図及び第2図に示す装置
を用いて脱水を行つた。15分間で110gの脱水を
行つたが、これは完全脱水であつた。脱水後の組
織をビニール袋に入れ1ヶ月間保存した。腐敗等
の変化は全く無く安定であつた。脱水中、異臭の
発生は全くなく放射性物質の散逸は全く認められ
なかつた。
例 2
例1と同じ装置を用いてかつ同じ条件下で14C
−グルコースで汚染された魚150gを15分間処理
し、110gの完全脱水を行つた。脱水した魚をビ
ニール袋に入れて1ヶ月間保存した後腐敗等の変
化は全くなく、安定であつた。異臭および放射能
散逸は全く認められなかつた。
The present invention relates to a dehydration device, and more particularly to a dehydration device for radioactively contaminated animals, such as animal waste contaminated with radioactive substances or animal carcasses suspected of being contaminated. Conventionally, hot air drying has been widely used to dry objects, and it is extremely advantageous compared to other methods such as infrared rays, especially when drying needs to be done at a relatively high speed. It is recognized that As is well known, in drying using hot air, etc., thermal energy is applied only to the surface of the object to be dried, that is, to be dehydrated, so the drying time depends on the surface area of the object. It takes a long time to dry. In addition, when increasing the thermal energy applied to the surface to shorten the time, a large amount of decomposed gas is generated from the surface of the object, especially for organic objects, which creates new odor problems and damages the object itself. more likely to be damaged. For example, currently a large number of experimental animals are used for various purposes, and animal waste after use is usually disposed of by incineration or burial underground. However, if this animal has been subjected to a radioisotope administration experiment, the above-mentioned normal treatment cannot be performed. As is well known, the difficulty in final disposal of radioactive animal waste is largely due to the method of waste storage. In other words, since animal waste is easily decomposed, measures must be taken to prevent radioactive waste from decomposing until it is handed over to a specific processing organization, and the usual way to do this is to preserve the waste using formalin or other preservatives. be. However, this method makes subsequent processing in a specific institution, such as incineration, extremely difficult. Therefore, for example, if animal waste could be stored in a form that is easily incinerated without using preservatives as in the past, the above problems would not occur.
One possible method for this purpose is the drying of animal waste, but as mentioned above, for example, hot air drying poses problems of time and decomposition gas, and it is extremely difficult to use this method. Also, when animal waste is dehydrated for drying, a strange odor is generated.
Furthermore, if this waste is contaminated with radioactive materials, there is a possibility that the water vapor and gas generated from the waste may contain these materials. The purpose of the present invention is to provide a dehydration device that dehydrates radioactively contaminated animals so that they can be preserved in a form that is easy to incinerate, and also prevents unpleasant odors and radioactive materials from dissipating outside the system. DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention applied to dehydration of animal waste contaminated with radioactive materials (hereinafter referred to as radioactive animal waste or animal waste) will be described below based on the drawings. In the drawing schematically showing the apparatus of the present invention in partial cross section, the apparatus is composed of a dehydration section A that can be divided by dotted lines and a safety section B when the object to be treated includes radioactive materials. The dehydration section A includes a microwave generator 20, a storage chamber or microwave irradiation chamber 30 that limits the microwave electromagnetic field generated by the microwave generator,
A flow rate adjustment device 14 for supplying air to the storage chamber 30, an exhaust port 18 for continuously taking out air from the storage chamber 30, a cooling device 22 for cooling the gas from the exhaust port 18, a cooling device 22 It consists of a collection container 24 for collecting liquid cooled and liquefied by the storage chamber 30, and a device 50 for detecting a so-called empty state after completion of dehydration in the storage chamber 30. This device 50 can also be used as a monitor of the dehydration process, as described below. Safety part B captures trace amounts of low-molecular radioactive gas that may be present in the collection container 24 and prevents it from escaping outside the system when the object to be dehydrated contains radioactive organic matter. A heating device 2, such as an electric furnace, for drawing out gas from the collection container 24 and oxidizing it.
6. An adsorption device 28 connected to this heating device 26 and filled with a moisture absorbent 29 such as soda lime or silica gel and an adsorbent 41 such as activated carbon, a cold trap 43 for collecting tritium water, and 14 CO 2
It consists of a carbon dioxide absorption device 44 and a suction pump 45 for absorbing carbon dioxide. The cold trap 43 and carbon dioxide absorption device 44 may be optional, but for example, they are described in Japanese Patent Application Laid-open No. 119286/1986 (Japanese Patent Application No.
43623), the purpose can be achieved efficiently. To explain in detail the apparatus shown in the drawings for radioactive animal waste, first, the animal waste 40 is wrapped directly or in something 42 that does not impede the passage of water vapor, such as paper or cloth, and then it is placed in the container 30 or in a second container. As shown in the figure, the air supply port 16' is made of a material transparent or transparent to microwaves, such as plastic or heat-resistant glass.
and sealed in a microwave transmission container 30' equipped with an outlet 18', which is placed in the storage chamber 30.
Air is supplied to the storage chamber 30 or container 30'. Air is supplied or forced through the pipe 12 from a suitable air source, and its flow rate is regulated by a suitable flow regulating device 14 provided in the flow path. This adjustment is necessary in order to efficiently draw water removed from the animal waste in the holding chamber 30 or container 30' through the outlet 18. A microwave generator 20, for example a magnetron, is activated in these conditions to place the animal waste 40 within a microwave field. This selectively excites the water molecules in the animal waste 40 and generates water vapor. This water vapor is carried by the supplied air and is quickly transported to the cooling device 22.
The liquid is liquefied and accumulated in the collection device 24. It is necessary for effective dehydration to quickly extract the water vapor generated at this time out of the microwave system, and for this purpose it is necessary to perform the above-mentioned flow rate adjustment. Furthermore, low-molecular compounds contained within the animal's body, such as a portion of lipids, may flow into the cooling device 22 by steam distillation. These are also the collection devices 24
are collected at the same time. When animal waste is disposed of in this way, odor is often a problem, and if this waste contains radioactive materials, sufficient safety measures must be taken to prevent these materials from escaping outside the system. is necessary. Therefore, in the present invention, the gas is taken out from the collection device 24 through the pipe 25 and guided to the heating device 26 filled with an oxidation catalyst such as copper oxide, where a complete oxidation reaction is carried out. Water, carbon dioxide, and other gas obtained after oxidation are transferred to the adsorption device 2 described above.
It is adsorbed and removed by 8. By using the adsorption device 28, even if radioactive substances, especially 3 H and 14 C, are present, almost all of them remain in the system. To further increase safety, a cold trap 4 connected to the adsorption device 28 is provided.
A device for trapping and removing radioactive substances consisting of 3 and a carbon dioxide absorption device 44 is used to prevent tritium and carbon 14, which may exist in the form of water and carbon dioxide, from escaping out of the system. As mentioned above, in this invention, water is extracted as water vapor by selectively imparting energy to water molecules using microwaves, so the maximum temperature reached is around 100°C, and at such temperatures the decomposition of the surface of organic matter occurs. There is almost no decomposition gas generation. Furthermore, only the dehydration reaction proceeds extremely efficiently, and there is almost no change in the shape of the sample solid. Furthermore, as described above, relatively low-molecular organic substances may be collected in the collection device 24, and radioactive substances may also be included in these organic substances. In such cases, the solvent may be removed by extraction with ether, hexane, etc., and the organic matter may be isolated as an oil or solid, and this form may be used as waste. Alternatively, the aqueous solution may be adsorbed and removed by directly passing through the activated carbon layer, and the activated carbon may be treated as combustible waste. Also, the adsorption device 2
The adsorbent etc. in 8 can be treated as solid waste. Normally, in microwave heating, if there is no water in the sample to be processed or if the sample is completely dehydrated, the microwave energy will no longer be absorbed, and it may accumulate in the chamber and eventually cause a discharge phenomenon. There is a risk of damaging itself. For this purpose, the illustrated apparatus solves the above problem by using a pipe that is transparent to microwaves and allowing water to flow through it. In the illustrated device, this consists of a U-shaped pipe 50, to which the water supply is supplied to the cooling device 22.
This is done by directly sending the water used in When such a configuration is used, the temperature of the water flowing through the pipe 50 rises rapidly upon completion of dehydration. Therefore, the dehydration process can be monitored by detecting this temperature rise. Measuring and indicating the temperature of the water in pipe 50 is obvious to those skilled in the art and will not be described in detail. When this device is used to dehydrate radioactive animal waste, the prevention of radioactivity dissipation outside the system is almost complete. However, in the embodiment, the possibility of extra-system dissipation is completely eliminated by maintaining the device itself under a vacuum. That is, the apparatus is housed in a housing 10 that is completely sealed except for the air supply port 16, the discharge port 46, and the water supply and discharge system, and the housing is evacuated through the exhaust port 52 to maintain a reduced pressure state. Example 1 Animal tissue contaminated with 14C -glucose (pork)
180 g was dehydrated using the apparatus shown in FIGS. 1 and 2 equipped with a microwave irradiation device with a frequency of 2500 MHz and an output of 450 W. 110 g of water was removed in 15 minutes, which was complete dehydration. The dehydrated tissue was placed in a plastic bag and stored for one month. It remained stable with no changes such as corruption. During dehydration, no strange odor was generated and no radioactive substances were observed to dissipate. Example 2 Using the same equipment and under the same conditions as Example 1, 14C
- 150 g of fish contaminated with glucose was treated for 15 minutes, resulting in complete dehydration of 110 g. After the dehydrated fish was stored in a plastic bag for one month, there was no change such as rotting and the fish remained stable. No strange odor or radioactivity dissipation was observed.
【表】
本考案を放射性動物廃棄物を例にとつて説明し
たが、これに限られるものでなく、天燃試料中の
微量物、例えば有害金属あるいは原子力発電等に
伴う放射性物質の生物体への濃縮等を調べるた
め、例えば汚染の疑いのある魚、海草、貝類等の
動物死体を脱水する場合にも利用出来る。
以上説明した様に、本考案は叙上の様に構成さ
れたので次の効果を有する。
(1) 放射性物質で汚染された動物廃棄物をマイク
ロ波透過容器内に収容し、マイクロ波照射によ
り廃棄物自体の中から発熱させて水蒸気その他
を伴つた気体をマイクロ波透過容器から取出す
ので、有機物の分解ガスを殆んど発生させるこ
となく脱水が迅速かつほゞ完全に行われ、滅菌
の上、特定機関での焼却がし易くかつ相当期間
腐敗することなく保存し易い乾燥物体を得るこ
とができ、これにより従来、特定機関に引渡す
までのホルマリン漬による保存及びその後の処
理に腐心していた放射性汚染動物の保存及び焼
却処理がきわめて簡便に行える。
(2) マイクロ波照射中放射性動物廃棄物から発生
した気体を冷却装置で先ず冷却して液化した液
体を捕集容器で捕集するので、動物廃棄物に含
まれていた放射性物質を含む有機物を捕集容器
中に捕捉することができる。
(3) マイクロ波透過容器に空気供給口を設けて該
容器内に空気を強制的に送入するので、放射性
動物廃棄物から発生した水蒸気その他を効率よ
く排出口を通じて引出すことができると共に、
マイクロ波透過容器内を真空にしながらマイク
ロ波照射を行つた場合に乾燥が或程度進行する
と該容器内にプラズマを誘発し勝ちなマイクロ
波真空加熱に比してプラズマの発生する恐れは
全くない。
(4) マイクロ波透過容器から取出した気体のうち
液化されなかつた残気を酸化装置に導いて酸化
反応させるので、残気中に存在し得るトリチユ
ウや炭素14を吸着除去し易い水や炭酸ガスの形
にすることができる。
(5) 酸化後に得られる水、炭酸ガスその他を吸着
装置により吸着除去するので、放射性物質の殆
んど大部分や臭気を系内に止めることができる
と共に、さらに吸着装置からの排気中に水及び
炭酸ガスの形で存在しうるトリチユウ及び炭素
14を捕捉して取り除く装置により放射性物質を
捕捉するので、放射性物質の系外散逸の防止が
ほゞ完全に行われ、この種放射性汚染動物の脱
水処理において万全を期すことができる。[Table] Although the present invention has been explained using radioactive animal waste as an example, it is not limited to this, but the present invention is not limited to this. It can also be used, for example, to dehydrate animal carcasses such as fish, seaweed, and shellfish that are suspected of being contaminated, in order to investigate the concentration of substances. As explained above, since the present invention is constructed as described above, it has the following effects. (1) Animal waste contaminated with radioactive substances is stored in a microwave-transparent container, heat is generated from within the waste itself by microwave irradiation, and gases containing water vapor and other substances are extracted from the microwave-transparent container. To obtain a dry object which can be quickly and almost completely dehydrated without generating almost any decomposition gas of organic matter, can be easily sterilized and incinerated in a specific institution, and can be easily stored without spoiling for a considerable period of time. This makes it extremely easy to preserve and incinerate radioactively contaminated animals, which previously required preservation in formalin until handing over to a specific organization and subsequent processing. (2) During microwave irradiation, the gas generated from radioactive animal waste is first cooled with a cooling device and the liquefied liquid is collected in a collection container, so organic matter containing radioactive materials contained in the animal waste can be collected. It can be captured in a collection container. (3) Since the microwave transmission container is provided with an air supply port and air is forcibly introduced into the container, water vapor and other substances generated from radioactive animal waste can be efficiently drawn out through the discharge port.
When microwave irradiation is performed while the inside of a microwave transmitting container is evacuated, there is no risk of plasma generation compared to microwave vacuum heating, which tends to induce plasma inside the container once drying has progressed to a certain extent. (4) Since the residual gas that has not been liquefied out of the gas taken out from the microwave transmission container is led to the oxidizer and subjected to an oxidation reaction, water and carbon dioxide gas that can easily adsorb and remove tritium and carbon-14 that may exist in the residual gas It can be in the form of (5) Since water, carbon dioxide, and other gas obtained after oxidation are adsorbed and removed by the adsorption device, most of the radioactive substances and odors can be stopped within the system, and water is also removed from the exhaust gas from the adsorption device. and tritium and carbon, which may be present in the form of carbon dioxide gas.
Since the radioactive material is captured by a device that captures and removes 14, radioactive material is almost completely prevented from dissipating outside the system, making it possible to ensure complete dehydration of this type of radioactively contaminated animal.
第1図は本考案を実施するための装置の概略
図、第2図は第1図の一部の変更例を示す図であ
る。
10……減圧ハウジング、14……流量調節装
置、20……マイクロ波発生装置、22……冷却
装置、24……捕集装置、26……酸化装置、2
8……吸着装置、30……マイクロ波照射室、3
0′……マイクロ波透過容器、40……廃棄物、
43……コールドトラツプ、44……炭酸ガス吸
収装置、45……ポンプ。
FIG. 1 is a schematic diagram of an apparatus for implementing the present invention, and FIG. 2 is a diagram showing a partial modification of FIG. 1. DESCRIPTION OF SYMBOLS 10... Decompression housing, 14... Flow rate adjustment device, 20... Microwave generator, 22... Cooling device, 24... Collection device, 26... Oxidizing device, 2
8...Adsorption device, 30...Microwave irradiation chamber, 3
0'...Microwave transparent container, 40...Waste,
43...cold trap, 44...carbon dioxide absorption device, 45...pump.
Claims (1)
置され脱水すべき放射性汚染動物を収容するマ
イクロ波透過容器30′を備え、マイクロ波照
射により前記放射性汚染動物から発生する水蒸
気その他を伴つた気体を取出すための排出口1
8′を前記マイクロ波透過容器に設け、前記気
体を冷却する冷却装置22を前記排出口に接続
し、気体のうち冷却されて液化した液体を捕集
する捕集容器24を備えた脱水装置であつて、
前記マイクロ波透過容器に空気を強制的に供給
するための空気供給口16′を設けると共に、
前記冷却装置により液化されなかつた残気を酸
化する酸化装置26を前記捕集容器に接続し、
酸化後に得られる水、炭酸ガスその他を吸着除
去する吸着装置28を備え、さらに前記吸着装
置からの排気中に水及び炭酸ガスの形で存在し
うるトリチウム及び炭素14を捕捉して取り除
く装置43及び44を備えてなる放射性汚染動
物の脱水装置。 2 前記トリチウム及び炭素14を捕捉して取り
除く装置が、トリチウム水を捕集するためのコ
ールドトラツプ43と、14CO2を吸収するた
めの炭酸ガス吸収装置44からなつている実用
新案登録請求の範囲第1項に記載の脱水装置。[Claims for Utility Model Registration] 1. A microwave irradiation chamber 30 and a microwave transmitting container 30' which is placed in the irradiation chamber and houses a radioactively contaminated animal to be dehydrated; Exhaust port 1 for taking out gas with water vapor and other substances
8' is provided in the microwave transmission container, a cooling device 22 for cooling the gas is connected to the outlet, and a collection container 24 is provided for collecting liquid cooled and liquefied from the gas. It's hot,
An air supply port 16' is provided for forcibly supplying air to the microwave transmission container, and
An oxidizing device 26 for oxidizing residual gas that has not been liquefied by the cooling device is connected to the collection container,
an adsorption device 28 for adsorbing and removing water, carbon dioxide, etc. obtained after oxidation, and a device 43 for capturing and removing tritium and carbon-14 that may be present in the form of water and carbon dioxide in the exhaust gas from the adsorption device; A dehydration device for radioactively contaminated animals, comprising: 44. 2 Claims for registration of a utility model in which the device for capturing and removing tritium and carbon-14 is comprised of a cold trap 43 for collecting tritiated water and a carbon dioxide absorption device 44 for absorbing 14-CO 2 The dehydration device according to item 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14341681U JPS6311680Y2 (en) | 1981-09-29 | 1981-09-29 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14341681U JPS6311680Y2 (en) | 1981-09-29 | 1981-09-29 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57138100U JPS57138100U (en) | 1982-08-28 |
JPS6311680Y2 true JPS6311680Y2 (en) | 1988-04-05 |
Family
ID=29936402
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14341681U Expired JPS6311680Y2 (en) | 1981-09-29 | 1981-09-29 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6311680Y2 (en) |
-
1981
- 1981-09-29 JP JP14341681U patent/JPS6311680Y2/ja not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS57138100U (en) | 1982-08-28 |
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